Guest Editorial: The Digitalisation of Data at Johnson Matthey

Johnson Matthey Technol. Rev., 2022, 66, (2), 120

Introduction

Over the last decade, the term ‘digital transformation’ has become prevalent across a wide variety of organisations. It refers to converting existing manual processes to create a more efficient and agile business environment. In 2018, >70% of organisations were reported as having a digital strategy or working to implement one (1). Johnson Matthey has established both key innovation programmes and the Digital Johnson Matthey programme to bridge between IT and the business to deliver ‘digital spearhead’ initiatives to meet this goal.

Digital transformation initiatives are part of a global shift towards so-called Industry 4.0 programmes. Evolving from established industrialisation practices, this future way of working builds upon the foundations of streamlined value-chain operations and automation by embedding data, modern smart technology, artificial intelligence and robotics in a seamless manner.

In order to stay competitive, organisations need to improve their internal processes to deliver faster innovation across research and development (R&D) and manufacturing, while accommodating the shifting needs of customers and macroeconomic factors. Additionally, companies are increasing external collaborations with networks of partnerships and innovation centres, to access new technology and capabilities that complement in-house competencies (2). A modern digital infrastructure can facilitate this by providing effective exchange of information alongside a culture of continuous improvement, with an emphasis on operational agility and experimentation to drive the desired outcomes.

Expected benefits of recognising that data is an asset are operational efficiency gains, with the ability to improve product quality and reduce development time and cost. This directly yields an improved competitive position in the marketplace. Moreover, there may also be opportunities to develop new revenue streams by aligning physical product offerings with ancillary software optimisation applications. The Johnson Matthey LevoTM application for plant optimisation is a good example of this.

The global impact of COVID-19 was widespread and transformative in its own right, as organisations rapidly adapted. With remote working and a need for business continuity, companies accelerated digitisation of systems supporting all manner of business functions. The response to the pandemic and mitigating actions to ensure business continuity have helped to speed the adoption of digital technologies. Many of these changes are embedded and expected to be long lasting. The value of the digital strategic initiative is recognised: 53% of companies plan to cut or defer capital investments because of COVID-19, but just 9% will make cuts in digital transformation efforts (3).

Driving Value from FAIR Data

Data is the new digital fuel that is the heart of the Industry 4.0 initiative. Both legacy and current research data are used to create and power the artificial intelligence algorithms and modelling approaches that lead to break-through product innovations.

Historically, attempts at mining legacy data were challenging because data was often in disparate systems and formats, which took time to find, and transcribing information from paper records was cumbersome and error prone. Across many organisations, there has often been fragmentation of ownership of data across disparate groups, as well as segmentation across the organisation, creating barriers to shared information.

The industry-recognised approach is now for data to adhere to Findable, Accessible, Interoperable and Reusable (FAIR) guidelines. By moving to electronic records and systems that allow for structured data capture, i.e., with well-defined metadata and results fields, data scientists and modellers will have near real-time access to a wealth of research and process engineering records.

Culture of Change

As technology plays a more pivotal and crucial role in creating an agile business environment, organisations need to recognise that embracing digital tools and analytics helps to unlock the full potential of data. This in itself requires a shift in mindset, necessitating behavioural changes and learnings to manage data more effectively on a day-to-day basis. The community needs to store data in a meaningful manner, to open data repositories and to apply data governance and agreed practices that make the data accessible and clear for other people to use. This task is not insignificant, and conscious effort is required to align to this new way of working and for people to recognise the opportunities that their data presents.

The transformation process is essentially facilitating communication and exchange between stakeholders i.e., between different research, analytical, development and manufacturing departments, to those that ultimately service the external customer. As an organisation transitions from paper to spreadsheets to smart applications for managing these interactions, there is an opportunity to reconsider how processes are performed and how information is communicated, using digital technology.

As organisations work to overcome obstacles and drive operational efficiencies towards improved competitiveness, it is important to recognise that a digital transformation initiative cannot simply be solved by introducing a suite of new tools and applications. In a 2016 survey, 87% of companies thought that digital would disrupt their industry, while only 44% felt prepared for these potential digital changes, and little has changed since then (4, 5). As such, there needs to be a company-wide shift in thinking and process, alongside training and support. With CEO and senior management encouragement, the culture of change across the entire organisation needs to be prioritised. Importantly, there is also a converse ‘bottom up’ alignment, with engagement from end-users who recognise inefficiencies in current practices and who are enthusiastic and contribute ideas about new ways of working.

Conclusions

The challenges of creating a world that is cleaner and healthier, today and for future generations, will only be solved by engaging with disruptive innovation that is driven by digital transformation. As a result, organisations are rapidly developing, adjusting or accelerating strategies to provide the required technical and business agility. This extends from how their employees work and collaborate to how they engage with partners, suppliers and customers. The technology disruptors of today will help make the workplace a data-driven organisation, leveraging technology and culture change to drive business strategy in ways that help promote growth, spur innovation, reduce costs, streamline operations and create satisfied, loyal customers.

By |2022-03-01T11:11:18+00:00March 1st, 2022|Weld Engineering Services|Comments Off on Guest Editorial: The Digitalisation of Data at Johnson Matthey

Discrete Simulation Model of Industrial Natural Gas Primary Reformer in Ammonia Production and Related Evaluation of the Catalyst Performance

The process described herein is based on the Kellogg Inc catalytic high-pressure reforming method for producing ammonia starting with natural gas feed. An ammonia plant steam reforming unit can produce 1360 tonnes per day of liquid ammonia. Figure 2 presents the steady-state flow sheet of the SMR unit build in UniSim® Design R470 with the main process flow designated with the red line.

Fig. 2.

SMR steady-state flowsheet

SMR steady-state flowsheet

Natural gas feed at a pressure of about 32 bar enters the natural gas knock-out drum 120-F for elimination of entrained liquid. The outlet line of 120-F feeds the one-stage centrifugal natural gas feed compressor 102-J driven by back-pressure (40/4 bar) steam turbine 102-JT. Outlet pressure of natural gas is at the level of 42 bar. Hydrogen required for desulfurisation of the natural gas is injected into the paralleled natural gas stream entering the natural gas fired heater 103-B. The outlet temperature of 103-B is 400°C. The heated natural gas stream flows through two reactors in series. The first is the hydrogenator 101-D, which contains a single bed of cobalt-molybdenum catalyst. It converts the organic sulfur compounds to hydrogen sulfide in the presence of the hydrogen injected upstream of 103-B. The natural gas stream next passes into the desulfuriser reactor 102-D, which contains a single bed of zinc-oxide catalyst. In this reactor the hydrogen sulfide is converted to zinc sulfide which remains in the catalyst.

The desulfurised natural gas, plus residual hydrogen, leaves 102-D with a sulfur content of 0.25 ppm and at a temperature of 370°C. The natural gas plus residual hydrogen stream is joined by the process steam in the mixer. The process steam is at a pressure of about 40 bar and a temperature of 392°C. The steam flow is controlled with the steam-to-natural gas (S/NG) molar ratio controller.

The SMR feed gas flows to the mixed feed coil, which is located in the convection section of the SMR furnace. In this coil, the SMR feed is heated to about 510°C. After heating, the SMR feed flows down through ten rows of reformer tubes that are suspended in the radiant box of primary reformer 101-B. Eleven rows of forced draught down fired burners are located in parallel rows to the catalyst tubes, in total 198 burners. They raise the feed temperature to about 790°C at the outlet of the catalyst tubes. In addition, 11 tunnel burners are used to heat the waste gases passing from the radiant to the convection part of the SMR furnace. 520 catalyst tubes with a total length of 10 m and inside diameter of 0.0857 m contain 30 m3 of nickel reformer catalyst. The reformed gas (syngas) then flows to the secondary reformer for further processing.

In order to predict the performance of the SMR process, it is necessary to simulate the tube side process and provide a detailed profile of the heat flux, gas composition, carbon forming potential and the pressure inside of the reformer tubes incrementally. The calculations involve solving material and energy balance equations along with reaction kinetic expressions for the nickel catalyst.

The general overall reaction for the steam reforming of any hydrocarbons can be defined as Equation (i) (1, 2):

(i)

In this work, steam reforming of the natural gas is described with the following equations, as the methane is the major constituent of the natural gas. Equation (ii) (1, 2):

(ii)

In parallel with this SMR equilibrium, the water gas shift (WGS) reaction proceeds according to Equation (iii) (1, 2):

(iii)

Minette et al. (17) in their work stated that the second SMR reaction is often not accounted for assuming it follows directly from combining Equations (i) and (ii). However, the work of Xu and Froment (78) showed that the second SMR reaction expressed by Equation (iv) follows an independent reaction path and must be accounted for in combination with Equations (i) and (ii), as confirmed by the measurements of Minette et al. (17):

(iv)

As mentioned, the described reactions proceed in indirectly heated reformer tubes filled with nickel-containing reforming catalyst and are controlled to achieve only a partial methane conversion. In a top fired reformer usually up to 65% to 68% conversion based on methane feed can be accomplished, leaving around 10 mol% to 14 mol% methane per dry basis (1, 2).

The overall SMR reaction of methane is endothermic and proceeds with an increase of volume at the elevated pressure of 20 bar to 40 bar and temperatures from 800°C to 1200°C at the exit of the reformer tubes in the presence of metallic nickel catalyst as an active component. Besides pressure and temperature, the S/NG molar ratio has a beneficial effect on the equilibrium methane concentration (18).

Another reason for applying the appropriate (higher) S/NG molar ratio is to prevent carbon deposition on the reforming catalyst. The side effect of carbon deposition is a higher pressure drop and the reduction of catalyst activity. As the rate of endothermic reaction is lowered, this can cause local overheating of the reformer tubes (hot spots and bands) and the premature failure of the tube walls. The carbon formation may occur via Boudouard reaction, methane cracking and carbon monoxide and carbon dioxide reduction. These reactions are reversible with dynamic equilibrium between carbon formation and removal. Under typical steam reforming conditions, Boudouard reaction and carbon monoxide and carbon dioxide reduction cause carbon removal, whilst methane cracking leads to carbon formation in the upper part of the reformer tube (19). Greenfield SMR units based on natural gas regularly use a S/NG molar ratio of around 3.0, while older installations are in the range from 3.5 to 4.0 (1). From the theoretical point of view any S/NG molar ratio which is slightly over 1.0 will prevent cracking, because the rate of carbon removing reactions is faster than the rate of carbon deposition reactions. However, from the practical point of view (catalyst limitations and sufficient quantity of steam for the downstream process step of WGS conversion), the minimum molar ratio which applies at the industrial level is 2.5. To account for all these facts, the model was validated for S/NG molar ratios in the range from 2.0 to 6.0.

The nickel content in relation to the composition and structure of the support differs considerably from one catalyst supplier to another. This is the reason why it is difficult to relate data from industrial plants to laboratory experiments. Reformer simulations frequently use a numerical approach in which the experimental data serves for reaction rate calculations which are described by closed analytical expressions. From the reaction rates perspective, it is possible to calculate the equilibrium gas composition for a given pressure and S/NG molar ratio at different temperatures. On top of this, the equilibrium curve which is defined by the corresponding enthalpy changes versus temperature also presents a useful parameter in the estimation of the catalyst performance. The comparison of the mentioned equilibrium curves with the working curves (working point) and the subsequent operator’s adjustments of the influencing process parameters according to the evaluated recommendations seem a useful tool to improve the catalyst performance.

In order to describe the kinetic conditions which are necessary for the determination of equilibrium methane molar concentration (a measure for the theoretical conversion) and enthalpy change over different nickel catalysts in relation with temperature at different S/NG molar ratios and reforming pressures, the model uses the following reaction rates for the equilibrium Equations (ii) to (iv) (78, 20), Equations (v)(viii):

(v)

(vi)

(vii)

(viii)

where r presents the reaction rates for methane, carbon monoxide and carbon dioxide in kmol m–3 s–1; p stands for the species partial pressures (in atm); T is the temperature (in K); while R is the gas constant (in kJ kmol–1 K–1).

Kinetic rate constants ki are given by the general Arrhenius relationship, Equation (ix) (78, 20), where i denotes the number of reactions from Equation (i) to (iii):

(ix)

The units of k2 and k4 (Equation (ii) and (iv)) are kmol bar0.5 kg–1cat h–1), while the unit of k3 (Equation (iii) is kmol bar–1 kg–1cat h–1).

Table I (20) gives the parameters for the activation energies, Ei, and for the pre-exponential factors, Ai, used in the model, valid for most of the commercial nickel catalysts with either MgAl2O4 or CaAl12O19 support.

Table I

Parameters for the Activation Energies, E i, and for the Pre-Exponential Factors, Ai

Equilibrium reaction Activation energy, Ei


Pre-exponential factor, Ai


Unit Value Unit Value
Reaction no. 2 kJ mol–1 –240.100 kmol bar0.5 kg–1cat h–1 4.22 × 1015
Reaction no. 3 kJ mol–1 –67.130 kmol bar–1 kg–1cat h–1 1.96 × 106
Reaction no. 4 kJ mol–1 –243.900 kmol bar0.5 kg–1cat h–1 1.02 × 1015

Apparent adsorption equilibrium constants Ki in Equation (x) are defined by the general expression given in (78, 20), where i denotes the species in Equations (i), (ii) and (iii) or methane, water, hydrogen and carbon monoxide:

(x)

Bi is the pre-exponential factor expressed in bar-1 or unitless, while ΔHi is the absorption enthalpy change expressed in kJ mol–1.

Table II presents the pre-exponential factors and the absorption enthalpy changes for species given in Equation (x), and the same is also valid for most of the commercial nickel catalysts with either MgAl2O4 or CaAl12O19 support.

From Equations (v) to (vii) it can be concluded that the concentration of hydrogen cannot be zero, because dividing with zero would make calculated reaction rates infinite. So, according to this, it is necessary to ensure the minimum content of hydrogen in the natural gas stream to ensure applicability of these equations in the model. From the process side, hydrogen is necessary for two reasons. Firstly, it is important for the removal of organic sulfur compounds present in the natural gas by the cobalt-molybdenum catalyst, as sulfur is a poison for the nickel catalyst (reaction between organic sulfur compounds and hydrogen to give hydrogen sulfide which is subsequently absorbed by zinc oxide bed). Secondly, hydrogen will always keep the nickel catalyst in the reduced state of metallic nickel and hence maintain adequate catalyst activity in the reformer tubes.

Table II

Parameters for the Pre-Exponential Factor, Bi, and for the Absorption Enthalpy Changes ΔHi

Species Pre-exponential factor, Bi


Absorption enthalpy change, ΔHi


Unit Value Unit Value
Methane bar–1 6.65 × 10–4 kJ mol–1 38.280
Water 1.77 × 105 kJ mol–1 –88.680
Hydrogen bar–1 6.12 × 10–9 kJ mol–1 82.900
Carbon monoxide bar–1 8.23 × 10–5 kJ mol–1 70.650

From the general stoichiometry and according to defined reaction rates, the model can calculate the molar flow rates of species i in kmol h–1 in the presence of an adequate quantity of nickel catalyst with the ultimate result of methane and water conversions. The relations used to determine the methane and water conversions are as follows (21, 22), Equations (xi)(xii):

(xi)

(xii)

A denotes the catalyst tube cross-sectional area in m2; ρB represents the catalyst bed density in kg m–3; Fi is the molar flow rate of the species methane and water in kmol h–1; while ηi is the effectiveness factor for methane and water.

To account for the variations in reaction rate throughout the catalyst pellet, a parameter called effectiveness factor, η, is defined. This is the ratio of the overall reaction rate in the catalyst pellet and the reaction rate at the external surface of the catalyst pellet. Effectiveness factor is a function of Thiele modulus, Φ, which is related to the catalyst volume and the external surface area of the catalyst pellets. Taking into account reaction rates given by Equations (v)(vii) and following the mechanism given by Xu and Froment (7, 8), the effectiveness factor can be calculated from Equation (xiii):

(xiii)

where p is the partial pressure of the species in bar; r presents the reaction rates for methane, carbon monoxide and carbon dioxide in kmol m–3 s–1; while ξ is the dimensionless intracatalyst coordinate.

Effectiveness factor profiles along the length of the reformer tube are calculated for all key species given in Equations (ii) to (iv) by solving two-point boundary differential equations for the catalyst pellets with the help of scripts and functions in the form of m-files, which was reconciled with the data from the simulator flowsheet.

The algorithm uses the following relationship for calculation of species concentration profiles inside the catalyst layer under reconciled conditions (17), Equations (xiv)(xv):

(xiv)

(xv)

with the corresponding boundary conditions, Equations (xvi)(xvii):

(xvi)

(xvii)

where ξ is the dimensionless intracatalyst coordinate; De,A is the species effective diffusivity in m3fluid m–1catalyst s–1; p denotes the partial pressure of species in bar; R is the universal gas constant in kJ kmol–1 K–1; T is the bulk fluid temperature in K; h is catalytic layer thickness in m and ρs is the active solid density in kgcatalyst m–3catalyst.

The interfacial (gas-solid) mass and heat transfer limitations are negligible and were not accounted for, because the high volume flow velocity and sufficient turbulence have been assumed which reflects the operation conditions inside of the reformer tubes.

Due to model simplification and minimisation of the computational time the simplest geometry of a slab of catalyst has been assumed, which is a satisfactory assumption for the computational routine required for industrial application. The model has been tested with coating thickness in the range from 10 μm to 50 μm and the best fit with the actual process data was achieved with the catalyst coating of 10 μm.

The species effective diffusivity is determined by Equation (xviii):

(xviii)

where ɛs is the internal void fraction or porosity of the catalyst in m3fluid m–3catalyst; τ denotes the catalyst tortuosity and is the average diffusivity of species A.

The average diffusivity of species is determined by Equation (xix):

(xix)

where DA is the diffusivity of the reacting species A given by Equation (xx) and S(rp,i) is the void fraction taken by the pores with radii ranging from rp,i to rp,i +1:

(xx)

where DkA is the Knudsen diffusivity in m3fluid m–1catalyst s–1.

In order to have an appropriate computational speed of effectiveness factor (which is performed by m-file), the actxserver command is used for the interconnection through the COM automation server that controls the simulator. The COM interface establishes a two-way communication between the simulator and MATLAB® through shared memory block, which is built as level-2S-function. The approximation of the catalyst effectiveness factor is determined by correlating the kinetic model results with the plant process data, and the model is validated to get maximum alignment with the actual process data.

Conversions of methane and water are calculated by Equations (xxi)(xxii) (22):

(xxi)

(xxii)

The Ergun equation for the determination of the pressure drop across the plug flow reactor (PFR) is used and solved as an ordinary differential equation (2331), Equation (xxiii):

(xxiii)

where ρ denotes the pressure in bar; ρ is the fluid density in kg m–3; v is the fluid velocity in m s–1; dp is the catalyst particle diameter in m; ∈ is the catalyst void fraction and Re is the particle Reynolds number.

The temperature variation of the reacting mixture (natural gas and steam) along the reformer tube is calculated according to the following relationship, Equation (xxiv):

(xxiv)

where G is the reacting mixture flow rate in kg h–1; denotes average specific heat of the gas mixture in kJ kg–1 K–1; U is the overall heat transfer coefficient between the reformer tubes and their surrounding in m2 h K kJ–1; Tt,0 is the temperature of the furnace that surrounds the reformer tubes; ΔHi is the enthalpy change in kJ kmol–1; ρB represents the catalyst bed density in kg m–3; ηi is the effectiveness factor for each of the species in reacting mixture and ri is the reaction rates in kmol m–3 s–1.

The reformer catalyst tubes are simulated as PFR in which the flow field is modelled as plug flow, implying that the stream is radially isotropic (without mass or energy gradients). According to this, axial mixing is negligible. As the reactants flow the length of the reformer tube, they are continually consumed, hence, there is an axial variation in the concentration. Since reaction rate is a function of concentration, the reaction rate varies axially. To get the solution for the PFR (axial profiles of compositions, temperature and so forth) the reformer tubes are divided into several sub-volumes. Within each sub-volume, the reaction rate is spatially uniform. A mole balance executes routine calculation procedure in each sub-volume j according to Equation (xxv) (28, 29):

(xxv)

Because the reaction rate is spatially uniform in each sub-volume, the third term reduces to rjdV and at steady state, the above expression reduces to Equation (xxvi):

(xxvi)

The firing side (furnace combustion model) was simulated according to the previous work of Zečević and Bolf (32) which is able to calculate adiabatic and real flame temperatures, quality and quantity composition of the waste gases, according to the known composition of the fuel gas and inlet temperatures of fuel and combustion air, with possibility to control all critical process parameters by implementation of proposed gain-scheduled model predictive control.

The basic input requirements for the model are:

  1. Integration information: number of reformer tube segments, minimum step fraction, minimum step length

  2. Tube dimensions: total volume, length and internal diameter of the reformer tube, number of tubes, wall thickness

  3. Tube packing: void fraction

  4. Catalyst data: diameter, sphericity, solid density, solid heat capacity, number of holes, tortuosity, mean pore radius, catalyst characteristic length, catalyst support

  5. Inlet process composition: flow rate, natural gas composition, pressure, temperature

  6. Outside tube wall temperature: measured values

  7. Heat transfer coefficient

  8. Activity coefficient.

By |2022-02-16T08:18:44+00:00February 16th, 2022|Weld Engineering Services|Comments Off on Discrete Simulation Model of Industrial Natural Gas Primary Reformer in Ammonia Production and Related Evaluation of the Catalyst Performance

Accelerating the Design of Automotive Catalyst Products Using Machine Learning

Johnson Matthey Technol. Rev., 2022, 66, (2), 130

Introduction

Domestic and commercial vehicles are leading sources of global pollution, with vehicle emissions risking the health of communities near roads (1). Fine and ultrafine particulate matter, oxides of nitrogen, hydrocarbons and carbon monoxide are key road traffic pollutants that are associated with adverse health effects (2). Catalytic converters have been used since the 1970s to reduce the emission of these pollutants by catalysing their reaction into less-toxic substances, typically carbon dioxide, nitrogen and water (3). However, current catalytic converters are not 100% efficient in their reactions of pollutants and moreover have variable efficiency at different operating temperatures.

This work uses machine learning modelling to analyse current catalytic converter performance and identify which future experimental tests would add most value to the ongoing development of improved catalytic converters. Previous work using machine learning in the catalysis domain has tended to focus on either augmenting quantum mechanical models of catalyst function (48), screening potential new catalysts (711), or predicting properties from carefully-selected chemical descriptors of catalysts (6, 8, 1214). In contrast, in this work we focus on modelling catalyst properties from the formulation ingredients and processing variables of the catalyst. The ingredients and processing conditions of samples are easily accessible during the development process, lowering the barrier to application of machine learning in active development projects. In the following section we discuss the project objectives, detail the machine learning methodology used and the results it delivers, before looking forward to potential future applications of machine learning for materials science in the automotive field and beyond.

Objectives

We collated data on 612 catalytic converter test sets that have been manufactured and experimentally tested by Johnson Matthey as part of an ongoing catalyst development project. The data contained information on the formulation used for the catalysts, including amounts and properties of 34 ingredients; 10 test parameters describing the testing process for each catalyst; and 16 experimentally measured properties for each catalyst including target gas conversions and selectivities. These output properties consisted of eight sets of tests, with each test run at both a high (approx. 500°C) and low (approx. 225°C) temperature on different samples of the same catalyst formulation. Each experimental property was reported as a steady-state average over 50–100 s of gas stream.

Using this data, we aimed to build understanding of the performance of this class of catalyst, using a machine learning model trained on the data to extract information on which input features of the formulation and processing parameters have most impact on the performance. Using this model, we then designed catalysts that offer both high performance and also add value to the machine learning model, which once made and measured can be added to the training dataset to enable more accurate modelling of high performance catalysts.

Methods

To model the catalyst data we used the AlchemiteTM multi-target machine learning platform. This method is described in detail in the literature (1517), but in brief consists of iteratively generating predictions for all data series, both input and output, and using these predictions to impute missing data on the input side, before the final iteration of predictions are reported as the predictions for the output series. This method is designed to handle sparse input data, as was found in this work where up to 10% of the catalysts were missing information on each of the input properties. As the method is multi-target, generating predictions for all output properties simultaneously, we trained a model to predict all 16 experimentally measured properties at once. AlchemiteTM also generates estimates of the uncertainty in each prediction, which is vital to prioritise suggestions for future experiments that are most likely to achieve specified objectives. To test the performance of the model, data on 61 catalysts (10% of the data) was randomly held back; the model was trained on data for the remaining 551 catalysts. Hyperparameters of the model were optimised using Bayesian Tree of Parzen Estimators via five-fold cross-validation within the training set only (17, 18).

To test the performance of the model we simultaneously predicted all 16 output properties for each of the 61 held-back catalysts and measured the coefficient of determination R2, for each output property. The coefficient of determination is defined as Equation (i):

(i)

where i indexes each catalyst in the validation set; yi are the true experimental values, with mean ȳ; and fi are the model predictions. A value of 1 indicates a perfect fit between model and experimental values; a value of 0 indicates a fit that is no better than random chance; and negative values indicate predictions that are worse than random. The performance of the model is shown in light blue in Figure 1. The median R2 across all the output properties is 0.71, indicating highly successful predictive accuracy. In Figure 1 we also compare to two robust standard machine learning approaches: support vector regression with radial basis function kernel and K nearest neighbours with 20 neighbours, implemented in scikit-learn (19), which were trained on a mean-imputed version of the ingredient and test parameter data and achieve baseline median R2 values of 0.52 and 0.49 respectively.

Fig. 1.

The coefficient of determination in prediction of each output property against the holdout test set, showing predictions of both high and low temperature tests in light blue and predictions using the high temperature experimental results to help predict the low temperature results in dark blue. Results from support vector regression and K nearest neighbours models are shown in grey for comparison

The coefficient of determination in prediction of each output property against the holdout test set, showing predictions of both high and low temperature tests in light blue and predictions using the high temperature experimental results to help predict the low temperature results in dark blue. Results from support vector regression and K nearest neighbours models are shown in grey for comparison

We observed that the predictions for Property 6, at both high and low temperatures, were poor: we identified that although changes in Property 6 are observable, a key physical mechanism directly influencing the value of Property 6 is driven by a chemical species not easily measurable by any analytical method and so is not fully captured in the dataset used to train the models. This explains the poor performance of the models in this aspect. The addition of (perhaps heuristic) descriptors to capture the physical mechanism may improve the modelling performance (14), but at the cost of increasing the barrier to usage of the method compared to taking only ingredients and processes as input.

Because the experimental tests on the catalysts are each repeated, run first at high temperature and then at low temperature, these results can be correlated so there is the possibility of increasing the efficiency of the testing process by using machine learning to replace one of the rounds of testing. To validate this, we trained a machine learning model that took as inputs the formulation ingredients and test parameters as well as the experimentally measured results on all eight tests at high temperature, and predicted the results of the eight tests at low temperature. This order (using high temperature results as input to predict low temperature results) was selected to align with the current testing methodology.

The improved performance by using the high temperature measurements to help predict the low temperature performance is exemplified in dark blue in Figure 1. For five of the eight experimental properties the accuracy significantly increased (increase in R2 of more than 0.1), and for Properties 1, 2 and 3 the resulting accuracy, with R2>0.95, is effectively equivalent to the experimental uncertainty in the measurement. For these three properties in particular, machine learning predictions could reliably replace experimental measurements, offering a saving in the time and effort required to run the experimental tests on new catalysts. The three experimental properties that were not improved by using the high temperature measurements are all related to the same target gas’ conversion rates, although it is not clear why these properties are not improved by access to increased experimental data. These three experimental properties are less commercially important than Property 1, which is the property with most commercial relevance.

Machine Learning Results

Now that we have confirmed the accuracy of the model we are well-positioned to extract actionable insights. Therefore, we first analyse the relationships that the model identified between inputs and outputs. To do so we examined which input features are used by the model when making predictions for each of the output properties, by evaluating the overall relative weights assigned to each input feature by the trained model, i.e. what fraction of the model prediction for each output is attributable to each input feature, on average across the whole model. This is calculated using the information gain attributable to each input feature (20). The results are summarised in Figure 2, separately for the model trained to predict both high and low temperature properties and the model trained to predict low temperature properties only. Averaging across each of the output properties, we find that for the high and low temperature model the test parameters and formulation ingredients are utilised in the proportion 0.59:1, and for the low temperature only model the test parameters, formulation ingredients and experimental high temperature measurements are utilised in the proportion 0.60:1:1.19. The consistent ratio of 0.6:1 in utilisation of the test parameters and formulation ingredients between the two models indicates that the high temperature experimental measurements (especially Properties 1, 2 and 3) are adding distinct information to the model that it was not capable of identifying from either the test parameters or formulation ingredients.

Fig. 2.

Importance of each input factor (horizontal axis) for making predictions of each output property (vertical axis). The upper plot shows the model trained to predict both high and low temperature results, whilst the lower plot shows the model trained to use the high temperature results to help predict the low temperature results. Higher values (darker colours) indicate more importance given to a variable. The importance values sum to one for each output property

Importance of each input factor (horizontal axis) for making predictions of each output property (vertical axis). The upper plot shows the model trained to predict both high and low temperature results, whilst the lower plot shows the model trained to use the high temperature results to help predict the low temperature results. Higher values (darker colours) indicate more importance given to a variable. The importance values sum to one for each output property

The key operational insight derived from this analysis was that although the formulation ingredients provide important information for the simultaneous modelling of the high and low temperature results, the variation in the test parameters also provides a key contribution. Historically the test parameters have been controlled within specification ranges but the impact of variation within these ranges has not been considered. These results show that the test parameters have an impact on the resulting properties and that control and understanding of these parameters improves the value of the data.

Machine Learning Formulation Design

With increased understanding of the importance of the test parameters for measured catalyst performance, we used the machine learning model to design catalyst formulations. For performance targets, we focussed on the most commercially important property (Property 1), aiming to maximise its value at both high and low temperatures, and for that value to be stable with temperature. Although Property 1 is the most commercially important property, the values of the other properties are also required for product success.

As well as looking for the formulations that would be most likely to succeed against these performance targets (‘exploitation’ of the model) we also searched for formulations that, when measured, would increase the model’s understanding of the formulation landscape and so improve future rounds of predictive modelling and formulation design (‘exploration’ of the model), as well as a balanced mix of the two objectives. We used a Bayesian search of the formulation space using Tree of Parzen Estimators (18) built into the AlchemiteTM platform, taking as the cost function the probability of simultaneously achieving all the performance targets, including a contribution from the uncertainty in each formulation’s predicted performance calculated as standard errors across the AlchemiteTM platform’s internal ensemble of sub-models (21). This cost function is the commercially relevant metric to aim to propose successful and useful new formulations. Exploitation-focused suggestions prioritise formulations with high probability of success, while exploration-focused suggestions prioritise formulations whose predictions are currently uncertain and will also help improve predictions over a wide range of formulation space.

A two-dimensional Uniform Manifold Approximation and Projection (UMAP) embedding (22) of the formulations is shown in Figure 3. The dark blue points show the historic experimental results, with more opaque points having higher performance against Property 1 and more transparent points having lower performance. We observe that there are several clusters of dissimilar formulations that had previously been measured, but that most of the formulations were relatively similar and are clustered in the centre of the plot (this clustering analysis being a key strength of the UMAP approach). Figure 3 also shows the formulations proposed by the machine learning approach, labelled by whether they are focused on exploration, exploitation or a balanced mixture. We observe that, as expected, the exploitation-focused suggestions are clustered more tightly at the centre of the plot, demonstrating that they are attempting to exploit a class of formulations with a high probability (up to 60%) of achieving all of the design targets simultaneously. In contrast, the exploration-focused suggestions are more varied, focusing particularly on gaps in the existing coverage of the formulation space where additional information will improve the model. The balanced suggestions show aspects of both behaviours. A subset of the formulations suggested by the machine learning, including samples from the exploration, exploitation and balanced suggestions, are currently undergoing experimental validation.

Fig. 3.

Two-dimensional UMAP embedding of the training data (blue points), with darker points those with higher performance on Property 1. Also shown are the experiments suggested by the machine learning approach, in light blue (exploration focused), purple (balanced search) and orange (exploitation focused)

Two-dimensional UMAP embedding of the training data (blue points), with darker points those with higher performance on Property 1. Also shown are the experiments suggested by the machine learning approach, in light blue (exploration focused), purple (balanced search) and orange (exploitation focused)

Conclusions

In this work we have shown how machine learning analysis of catalyst formulations enables new insights into the factors that affect catalyst performance, including particularly that the test parameters more strongly impact the eventual performance than was initially anticipated: this will have operational significance for the future of this product development. We have also shown how the use of a machine learning platform, rather than a single predictive tool, can enable full design workflows, including prioritising exploration of the formulation space or exploitation of a model to achieve high product performance, accelerating the design process by enabling a holistic view of the formulation opportunities. Future progress in this project could focus on achieving multiple target properties simultaneously, beyond only Property 1, or utilising the accurate predictions of low temperature measurements based on experimental high temperature measurements to halve the amount of experimental effort required when screening new formulations.

The machine learning approach here is applicable beyond catalytic converters, including the design of metal alloys (15, 23), batteries (24), and pharmaceutical drugs (21). A machine learning platform that can carry out the full cycle of formulation development, handling sparse real-world experimental data, building predictive models and proposing and interpreting new formulation designs adds value in each of these areas, with reduced barrier to entry by working directly on the composition and processing variables immediately accessible to project scientists.

Acknowledgements

Gareth Conduit acknowledges financial support from the Royal Society. There is Open Access to this paper online.

The Authors


Thomas Whitehead holds a PhD in theoretical physics from the University of Cambridge, UK, and is now leading the application of Intellegens’ novel deep learning approaches to a wide variety of industrial applications. His work focuses on developing a series of application-specific machine learning modules to address high-value data analysis bottlenecks.


Flora Chen is the Data Science Lead at Johnson Matthey. She has 15 years’ experience in global high-tech companies and has held technical and management roles spanning engineering, operations, R&D and quality. Since Flora joined Johnson Matthey in 2018, she has led several digital analytics projects, discovering and delivering the business value of data. Flora holds a PhD in Mechanical Engineering from Bristol University, UK, and is a chartered engineer.


Christopher Daly received an MChem (2008) and PhD (2012) in Chemistry from the University of Leicester, UK, where his research focused on the synthesis of organometallic compounds of the late transition metals and their applications in bifunctional catalysis. Since 2013 he has worked on automotive catalyst development at Johnson Matthey across several technologies, where he is currently a Senior Chemist.


Gareth Conduit has a track record of developing and applying machine learning methods to solve real-world problems. The approach, originally developed for materials design, is now being commercialised by startup Intellegens in materials design, healthcare and drug discovery. Gareth also has research interests in strongly correlated phenomena, in particular proposing spin spiral state in the itinerant ferromagnet that was later observed in CeFePO. Gareth’s group is based at the University of Cambridge.

By |2022-02-03T08:00:57+00:00February 3rd, 2022|Weld Engineering Services|Comments Off on Accelerating the Design of Automotive Catalyst Products Using Machine Learning

Emacs as a Tool for Modern Science

Johnson Matthey Technol. Rev., 2022, 66, (2), 122

Introduction

FAIR data principles have been held as the gold standard for ensuring data across the sciences and across individual institutions is generated and kept in as sustainable a way as possible (1). FAIR data principles unlock powerful ‘data lake’ workflows that allow for multiple interactions, machine learning and deep insight to be gained, adding value to already collected data (2). Reports and peer reviewed publications are needed to share knowledge with others at both an inter- and intra-institution level.

One nemesis to this approach is the use of proprietary software and proprietary data standards. It has been suggested that all research software should be free open source software (FOSS) and that closed source software should be the exception (3). The use of FOSS and open source hardware has been shown to offer flexibility and insight in a range of practical applications within chemical R&D (46).

A wealth of new software is available every year including productivity tools, document management, data analysis suites and code produced via individuals or research groups. One recent report showed that ~51,000 publications in the life sciences had 25,900 unique pieces of software cited (7). In addition to the wealth of new software offerings humans are keenly biased towards additive problem solving (8). Adding to an existing system rather than taking away in order to solve a problem is seen across sectors, job roles and in the digital tools used to enable science. An exemplar of this type of approach in software was seen with the introduction of the ribbon into Microsoft Office. Those more experienced with the software were more likely to be dissatisfied and impeded by the addition of the ribbon into the Office suite (9). Frustration stemming from unclear error messages, poor wording and lack of training lead to a loss of as much as 40% of a user’s time trying to solve software related issues (10).

As we train the next generation of scientists, and during the course of professional development, it is imperative that individuals reflect on and take control of the digital tools used to plan, conduct and share work. Frustration can be avoided if the tool being used is understood. Ideally, any skills learned during any part of an individual’s scientific career should be transferable. This is not possible if proprietary software solutions are used as there is no guarantee the software will be available at a new role either due to funding, dropped support or incompatibility with other systems.

One part of the solution to this, as demonstrated clearly by software projects like GNU/Linux (referred to herein as Linux), is the use of open source plain file formats like text files. Text files are human and computer readable, have demonstrable longevity and, crucially, are free and open source. Coupling this with tools that allow users to build, maintain and deploy their own solutions could resolve many of the frustrations seen with modern computer use.

Herein a demonstration of a workflow using a single tool, working with just text files, that can be used to radically change the workflow of a modern, flexible and agile scientist. The key benefits are increased productivity, return on investment, cost and environment, health and safety via improved ergonomics. In this viewpoint it will be demonstrated that such a solution exists and how it can be used in the context of corporate R&D.

Emacs and Org-Mode

Figure 1 shows two simplified workflows. Figure 1(a) shows the current state for many scientists. Each box in this flow represents a separate piece of software. These often have different shortcut keys, require many open programs and limit the user in terms of customisability and automatic flows. Each box may represent a different piece of software with separate associated upkeep costs, adding to both R&D expenditure and cost to monitor and ensure compliance with licenses. Figure 1(b) shows one possible solution where a single software solution replaces all the programs in a digital workflow. This workflow is possible with the open source and free program: Emacs.

Fig. 1.

Two simplified scientific workflows using: (a) current offerings; and (b) Emacs

Two simplified scientific workflows using: (a) current offerings; and (b) Emacs

Emacs

Emacs is a fully programmable and extensible text editor. It is used widely in the IT and programming fields. Originally developed in the 1970s, the version used today (GNU Emacs – referred to herein as Emacs) was developed in the 1980s by Richard Stallman. It may seem retrograde that a decades old software solution can compete with newer offerings, but its longevity speaks to its utility. Emacs has been maintained and updated throughout this period with versions available across Windows, macOS and Linux.

Out of the box Emacs is a blank canvas. The decades of use mean that many contributors have written, maintained and updated a large number of packages that can be downloaded and used for free. These packages are completely user customisable and self-documenting. Emacs allows the user to employ these packages to build what is needed from the ground up. The below examples demonstrate how this approach can be used in a range of tasks in corporate R&D. This was built and personalised in-house with speed and ease of use being key. By building this tool from the ground up there is no bloat or incompatibilities that come with other, long lived, commercial solutions.

Figure 2(a) and 2(b) shows the software loaded in either its unmodified form or after the application of one of the many distributions, in this case Spacemacs. These distributions come preconfigured for ease of use and with many quality of life features. It is possible for a user to use one of these or to build their own version.

Fig. 2.

(a) Emacs splash screen; (b) Spacemacs splash screen

(a) Emacs splash screen; (b) Spacemacs splash screen

Because the below use cases can be achieved from within one piece of software, productivity and focus can be retained with the use of suite-wide shortcuts and hot keys. This reduces the possibility of fragmented work which can reduce productivity (11). Emacs is also fully controllable from the keyboard, again improving speed, productivity and ergonomics.

Org-Mode

Org-mode is a major mode (a set of instructions for how certain files should be handled) for Emacs which was developed in 2003 by astrophysicist Carsten Dominik. Initially as a way to organise Dominik’s work, it has grown into a full suite. Allowing for everything from ‘todo’ task management to note taking and scientific manuscript preparation.

Importantly, it allows for a single document to contain data, working code and prose (12). Org mode has several minor modes (options that can be turned on or off) which can unlock advanced features impossible with other free or commercial solutions. These will be discussed in the following sections.

Scientific Overhead

Data generation does not happen in a vacuum. A scientist’s work day includes ‘scientific overheads’ that can dramatically lower the time spent by an individual on the act of conducting high quality science (13). Indeed only ~40% of young researchers’ time in academia is spent on research, with the majority of the remaining time spent on writing and administration (14).

This is represented pictographically as the first set of software in Figure 1(a). This can be thought of as everything up to the act of experimentation along with all the administration tasks associated with modern knowledge work. Emails, meetings and conferences all add to the overhead workers face. The following section is not an exclusive list of what can be done but aims to demonstrate a few case studies of how Emacs can remove the burden of scientific overheads by consolidation of tasks with Emacs and Org-mode.

Daily Planning

The act of producing, reviewing and executing a plan is an essential component of problem solving (15). Time management behaviours improve job satisfaction and health while negatively impacting stress (16). Org-mode allows for easy task management and planning from within the Emacs environment.

By setting up ‘Org-capture’, a package that works with Org-mode, todos can be captured and stored centrally from anywhere within Emacs. This makes capturing and recording tasks without interruption to flow trivial. Agendas and todo lists can be automatically populated from multiple sources (for example, reading list, meeting notes, project files). Importantly this approach works well with systems like ‘getting things done’ while staying flexible enough to allow for individual customisation (17). Examples of todo management as well as automatically generated agenda views can be found in Figure 3(a) and 3(b) respectively.

Fig. 3.

(a) Todo lists; (b) agenda views

(a) Todo lists; (b) agenda views

Administration

Additionally other tedious tasks can be automated. The use of tools like ‘Yasnippet’ allow for chunks of text to be stored and pasted into a document with only a few key presses. The production of meeting notes, for example, can be sped up by producing a template which can be imported. These can be exported via a .tex file and rendered into a PDF using LaTeX. This may seem arduous but, once set up, this is completely automated.

Macros can also be recorded and called when needed. If any task is done repeatedly then tools with Emacs can be used to automate that process. This reduction of overheads frees up a scientist to allow them to do what generates value for companies and academic institutions alike.

In a world where scientists are not just expected to produce data but be fully fledged knowledge workers, tools like this are invaluable. Their flexibility and utility can be tailored to the user’s workflow, enabling high productivity work to be conducted.

Reference Management

The act of collecting, reading and making notes on reference materials is a key aspect of scientific work. Importantly any possible solution to digitalise this should allow for citations to be placed within documents as well as easy access to referencing styles. This is possible with commercial solutions and even some open source options. Where an Emacs workflow outshines all is that the reference manager, note taking, citation tools and writing program are all one.

Packages like ‘Org-ref’ allow for import of PDFs from digital object identifiers (DOIs) allowing for fast import and conversion into a defined bibtex file (the plain text file used by LaTeX to generate citations). Notes can be accessed quickly using a package like ‘Interleave’ or ‘Org-noter’ which allows for automated note taking during the reading of a document, Figure 4.

Fig. 4.

An example of note taking while viewing a PDF using Interleave

An example of note taking while viewing a PDF using Interleave

Linking of notes and PDFs is extremely powerful and a rarity in the reference manager space. Due to the notes being in plain text they are also searchable unlike PDF highlighting or other, non-text or paper based, approaches.

Post Experiment Workload

Data Analytics

One of the benefits of multidisciplinary teams is learning about best practices outside of one’s field. One concept that has taken hold in the computer science world is that of literate programming. Literate programming is the idea that written code should not just tell a computer what to do but that it is imperative that the code also informs a human about what is running (18).

This approach should be common to scientists. The aim of written reports, manuscripts and presentations is to display complex data and analysis in an easy to understand form for humans. The problem, as we approach more complex analysis, is that: (a) the analysis is split from the final report or manuscript which leads to loss of reproducibility; or (b) that the analysis is hidden in proprietary software that does not conform to FAIR principles nor the longevity principles a large corporate or academic institution may expect.

Org-mode, by utilising ‘Org-babel’, allows for chunks of code to be written and executed from within a single document. Variables can be extracted from these code blocks and then embedded in the text or fed into other code blocks. There are clear parallels between this type of approach and that of the IPython/Jupyter notebooks. These notebooks offer similar advantages in combining prose and code, allowing for reproducibility in data analytics. Both Emacs Org-mode and IPython/Jupyter notebooks offer parallelisation as a feature within the language. These notebooks do, however, suffer from the same issues described above as they form part of a fragmented software solution. As will be described below, they also lack the ability to embed analysis to a final manuscript.

Plotting can be done in the same way with direct output to a number of image formats that can, in turn, be embedded into the Org file. If one simply wants a way to record one’s work in an easy to follow format which is completely human readable then Org-mode makes that a simple task. Where the power of this approach becomes evident is when this is linked with manuscript or report production.

Manuscript and Report Preparation

Org files are human readable with any text editor but Emacs unlocks many ways to quickly access the myriad of features not available outside Emacs. Importantly Org files can be exported in a range of formats including PDFs, markdown and open document formats. This manuscript was prepared as a Org file which was automatically processed into a .tex file and rendered into a PDF. Tools like ‘Writeroom-mode’ format documents to allow for a distraction-free writing experience, Figure 5.

Fig. 5.

A view of a draft of this manuscript from within Emacs using Writeroom-mode

A view of a draft of this manuscript from within Emacs using Writeroom-mode

When it comes to reports and manuscripts written in Emacs and Org-mode it is trivial to produce literate documents. Data and analysis can all be included within the manuscript which is also machine accessible. This works well with FAIR principles allowing for a human readable document to also act as metadata and a repository for computer readable data. To demonstrate this Figure 6(a) is a plot rendered by Python code embedded in this document. The values have been calculated from data within the file. The code snippet for this can be seen in Figure 6(b). If any changes are made to the analysis or the data, the plot is updated. This means that a single Org file can be provided and all data and analytics can be reproduced. It also makes the process of data analytics and report writing much easier. Any changes to the analysis will be updated in the text, either via plots or by embedded variables. This reduces the cognitive load associated with making requested changes, either during the peer review cycle or due to feedback from colleagues.

Fig. 6.

Examples of: (a) plot produced from: (b) code written within an Org file

Examples of: (a) plot produced from: (b) code written within an Org file

Previous reports have demonstrated how experimental data can be embedded into PDFs produced from Emacs allowing for a manuscript or report to contain all the data reported (19). The benefits of this are clear for both scientific integrity and rigour but also as a way to ensure a report or manuscript can be understood fully if an employee were to leave an institution, retaining the value of that work indefinitely.

Limitations

Emacs has a reputation of being difficult to learn and this should not be ignored. Emacs has a learning curve however this can be as steep or as shallow as the user needs. Emacs distributions like ‘Spacemacs’ or ‘Doom Emacs’ allow for mnemonics key bindings and other quality of life features. Vanilla Emacs has many of the graphical user interface aspects you would expect, such as menus, which allows for most of the functionality to be explored. Becoming proficient takes time however this comes slowly as utility is unlocked. As summarised by John Kitchin:

“Scientific publishing is a career-long activity, and one should not shy away from learning a tool that can have an impact over this time scale.” (19)

While this still holds true, the author feels it is imperative to add the same is true of all aspects of a scientist’s workflow including productivity, reference management and data analytics.

Additionally, despite best efforts, all aspects of an Emacs workflow may not be possible. Email is possible within Emacs. However due to some institutions’ policies, such as Azure Information Protection, it may not be possible to set up due to issues with accessing confidential information without support from the host organisation. In this case it would not be possible to utilise such a tool. Similarly, while FOSS software allows for flexibility and the ability to create one’s own code, a user will be dependent on the software being correctly maintained. This lack of warranty is an inherent issue with FOSS. With repositories like GitHub (and similar), it is possible to access, fork and publish or maintain one’s own repositories for tools at a personal or institutional level, providing licensing conditions allow.

The maintenance overhead should not be underestimated, especially when considering issues with business continuity. However, this is not a new problem and, if the value is seen, institutions can add resource to deliver long lasting FOSS solutions. Parallels can be drawn to the development of the Linux kernel. Here private companies contribute extensively to the FOSS development because there is an understanding of the value of that project to their business interest (20).

While FOSS approaches offer great benefits, the use of proprietary or closed source software is preferable when that software offers utility not possible by other routes. Complex analysis using statistical software, complex peak fitting or databases requiring subscriptions are still a reality of the profession. When these tools are needed the approach outlined above still works providing the data can be exported from such a program into a plain text format. If this is not possible and FAIR principles cannot be upheld, the use of such a tool should be re-evaluated to determine if its use can facilitate long term and sustainable analysis.

Conclusions

Emacs is a powerful and versatile tool for modern science. It facilitates the production, handling and analysis of data in a FAIR fashion while allowing modern scientists to be as agile as possible. By using tools under one FOSS umbrella huge productivity gains can be realised along with improvements in ergonomics and associated cost benefits with the removal of proprietary software tools. The learning curve should be viewed in the context of a lifelong scientific career. With institutions understanding the value of data beyond a single scientist, applying (or supporting individuals who wish to apply) this type of workflow more widely would have a profound and long last effect beyond the career of just one scientist.

By |2022-01-28T08:33:05+00:00January 28th, 2022|Weld Engineering Services|Comments Off on Emacs as a Tool for Modern Science

“Women in Nanotechnology”

“Women in Nanotechnology” | Johnson Matthey Technology Review

Johnson Matthey Technol. Rev., 2022, 66, (1), 114

doi:10.1595/205651322×16379357955860

“Women in Nanotechnology”

Edited by Pamela M. Norris (University of Virginia, USA) and Lisa E. Friedersdorf (University of Virginia, USA), Women in Engineering and Science Series, Springer Nature Switzerland AG, Cham, Switzerland, 2020, 140 pages, ISBN 978-3-030-19950-0, £74.99, €88.58, US$100.00

  • Sara Coles
  • Johnson Matthey, Gate 2, Orchard Road, Royston, Hertfordshire, SG8 5HE, UK
  • *Email: sara.coles@matthey.com

NON-PEER REVIEWED FEATURE
Received 22nd November 2021; Online 11th January 2022

SHARE THIS PAGE:

**The complete article is available by downloading the PDF. Full text HTML is coming soon!**

BACK TO TOP

SHARE THIS PAGE:


By |2022-01-11T16:37:10+00:00January 11th, 2022|Weld Engineering Services|Comments Off on “Women in Nanotechnology”

Challenges of Coating Textiles with Graphene

Challenges of Coating Textiles with Graphene | Johnson Matthey Technology Review

Johnson Matthey Technol. Rev., 2022, 66, (1), 106

doi:10.1595/205651322×16260813744138

Challenges of Coating Textiles with Graphene

Different types of graphene for different textiles and applications

  • Ana I. S. Neves*, Zakaria Saadi
  • College of Engineering, Mathematics and Physical Sciences, Harrison Building, Streatham Campus, University of Exeter, North Park Road, Exeter, EX4 4QF, UK
  • *Email: a.neves@exeter.ac.uk

PEER REVIEWED
Received 26th March 2021; Revised 22nd June 2021; Accepted 12th July 2021; Online 12th July 2021

SHARE THIS PAGE:

Article Synopsis

Electronic textiles (e-textiles) hold the key for seamless integration of electronic devices for wearable applications. Compared to other flexible substrates, such as plastic films, textiles are, however, challenging substrates to work with due to their surface roughness. Researchers at the University of Exeter, UK, demonstrated that using different coating techniques as well as different types of graphene coatings is the key to overcome this challenge. The results of coating selected monofilament textile fibres and woven textiles with graphene are discussed here. These conductive textiles are fundamental components e-textiles, and some applications will be reviewed in this paper. That includes light-emitting devices, touch and position sensors, as well as temperature and humidity sensors. The possibility of triboelectric energy harvesting is also discussed as the next step to realise self-powered e-textiles.

**The complete article is available by downloading the PDF. Full text HTML is coming soon!**

BACK TO TOP

SHARE THIS PAGE:


By |2022-01-11T16:16:16+00:00January 11th, 2022|Weld Engineering Services|Comments Off on Challenges of Coating Textiles with Graphene

In the Lab: Spotlight on Surface Characterisation Activities at Johnson Matthey

Johnson Matthey Technol. Rev., 2022, 66, (1), 77

Before joining Johnson Matthey, Tuğçe Eralp Erden was a Marie Curie PhD student at the University of Reading, UK, studying model chiral adsorption systems using synchrotron-based structural and spectroscopic techniques (15). After completing her PhD, she joined the advanced characterisation department at Johnson Matthey, Sonning Common, UK, where she is currently leading the surface spectroscopy team.

The Researcher

  • Name: Tuğçe Eralp Erden

  • Position: Principal Scientist

  • Affiliation: Johnson Matthey Plc

  • Address: Blounts Court, Sonning Common, Reading, RG4 9NH, UK

  • Email: tugce.eralperden@matthey.com

The Research

Johnson Matthey’s surface spectroscopy team focuses on providing essential information on the surface chemistry and composition of different materials for Johnson Matthey businesses and their customers. The team develops in situ, ex situ multi-technique surface analysis methods to deliver a more in-depth surface characterisation (6). Using laboratory-based X-ray photoelectron spectroscopy (XPS) as the main surface analysis technique, the team works on the applications of several complementary spectroscopic techniques such as ion scattering spectroscopy (ISS), reflection electron energy loss spectroscopy (REELS), ultraviolet photoelectron spectroscopy (UPS) and Raman.

The surface spectroscopy team is also involved in developing synchrotron-based near-ambient pressure (NAP)-XPS applications to study materials under reaction conditions. The team has been supporting fundamental surface science investigations and has sponsored several PhD projects that involved NAP-XPS characterisation of catalysts under reaction conditions. Two recent PhD projects with the University of Reading involved synchrotron-based NAP-XPS measurements to study supported platinum group metal (pgm) catalysts under methane oxidation reaction conditions in situ.

The first PhD project focused on investigating the chemical and compositional changes in alumina supported palladium catalysts with different particle sizes (4 nm to 10 nm) under reaction conditions similar to those used in the partial oxidation of methane to synthesis gas (syngas) (7). Surface adsorbates, palladium oxidation states and partial pressures of reactants and products were simultaneously tracked using mass spectrometry and NAP-XPS. NAP‐XPS data showed how the oxidation state of the palladium changes with increasing temperature (from Pd[0] to PdO and back to Pd[0]). NAP-XPS data analysis was further enhanced using mass spectrometry which showed an increase in carbon monoxide production over the Pd[II] oxide phase. In this study, a particle size effect was revealed for the catalysts demonstrating that methane conversion starts at lower temperatures with larger sized particles (Figure 1) (8).

Fig. 1

Temperature of carbon monoxide and hydrogen initial production versus particle size (8) Creative Commons CC BY

Temperature of carbon monoxide and hydrogen initial production versus particle size (8) Creative Commons CC BY

For palladium catalysts on different supports such as alumina, silica and a mixture of alumina and silica, NAP-XPS showed that on all the supports studied PdO is the dominant oxidation state and is the active site for complete methane oxidation which occurs at 500–600 K. As the oxygen is consumed and the temperature increases to >650 K, PdO is found to reduce to PdOx, where 0 ≤ x < 1. Mass spectrometry showed a decrease in the partial pressures of complete methane oxidation products (carbon dioxide and water). Syngas formation (hydrogen and carbon monoxide), the product of partial methane oxidation, is dominant, suggesting reduced palladium is the active state for partial methane oxidation. The reactivity of alumina supported palladium materials is found to increase in the order: SiO2 < SiO2-Al2O3 < Al2O3 (Figure 2) (8).

Fig. 2

Catalyst E (Pd/Al2O3 nanoparticles of average size 10 nm). (a) NAP-XP spectra in the palladium 3d region; and (b) methane conversion, calculated from mass spectrometry data, recorded in the temperature range from 450 K to 720 K under 240 mTorr O2:CH4 pressure (1:2). Heating: mass spectrometry at constant temperature during NAP-XPS measurements; cooling: recorded during continuous cooling from 720 K to 450 K. Binding energies are corrected to corresponding aluminium 2p spectra at 74.5 eV (8) Creative Commons CC BY

Catalyst E (Pd/Al2O3 nanoparticles of average size 10 nm). (a) NAP-XP spectra in the palladium 3d region; and (b) methane conversion, calculated from mass spectrometry data, recorded in the temperature range from 450 K to 720 K under 240 mTorr O2:CH4 pressure (1:2). Heating: mass spectrometry at constant temperature during NAP-XPS measurements; cooling: recorded during continuous cooling from 720 K to 450 K. Binding energies are corrected to corresponding aluminium 2p spectra at 74.5 eV (8) Creative Commons CC BY

Another collaborative PhD project (Johnson Matthey; Diamond Light Source, UK; and the University of Reading) involved studying the effect of pgm composition and reaction conditions (dry and wet) on the catalytic behaviour of a range of alumina supported monometallic palladium and bimetallic palladium-platinum nanocatalysts under methane oxidation conditions. NAP-XPS and in situ mass spectrometry were combined to correlate the product formation and the chemical state of the catalyst throughout the temperature ramps under methane and oxygen gas mixture at elevated temperatures under dry and wet conditions (Figure 3). NAP-XPS was used to study the chemical states of monometallic palladium and bimetallic palladium-platinum nanocatalysts, demonstrating that there is a clear link between platinum presence, palladium oxidation and catalyst activity under stoichiometric reaction conditions. Under oxygen-rich conditions this behaviour is found to be less clear, as all of the palladium tends to be oxidised, but there are still benefits to the addition of platinum in place of palladium for complete oxidation of methane (9).

Fig. 3

(a) Overlaid catalytic testing data with Pd[II]% as determined by NAP-XPS for 4 wt% Pd–1 wt% Pt/Al2O3 catalysts under oxygen excess (CH4:O2:H2O = 1:120 (:100) or 1:2 (:2)) methane oxidation conditions. Palladium 3d XP spectra of 4 wt% Pd–1 wt% Pt/Al2O3 catalysts under: (b) dry conditions (0.11 mbar CH4 + 0.22 mbar O2; CH4:O2:H2O= 1:2:0); wet conditions (0.11 mbar CH4 + 0.22 mbar O2 + 0.22 mbar H2O (CH4:O2:H2O=1:2:2). Reprinted from (9) under Creative Commons Attribution 4.0 International (CC BY 4.0)

(a) Overlaid catalytic testing data with Pd[II]% as determined by NAP-XPS for 4 wt% Pd–1 wt% Pt/Al2O3 catalysts under oxygen excess (CH4:O2:H2O = 1:120 (:100) or 1:2 (:2)) methane oxidation conditions. Palladium 3d XP spectra of 4 wt% Pd–1 wt% Pt/Al2O3 catalysts under: (b) dry conditions (0.11 mbar CH4 + 0.22 mbar O2; CH4:O2:H2O= 1:2:0); wet conditions (0.11 mbar CH4 + 0.22 mbar O2 + 0.22 mbar H2O (CH4:O2:H2O=1:2:2). Reprinted from (9) under Creative Commons Attribution 4.0 International (CC BY 4.0)

Acknowledgements

Tuğçe Eralp Erden would like to thank the surface spectroscopy team (Riho Green, Charlotte Wise, Alex Oje, Matthew Forster), Johnson Matthey PhD students Alexander Large and Rachel Price, academic partners Professor Georg Held and Associate Professor Roger A. Bennett, Versox beamline team at Diamond Light Source, Johnson Matthey collaborators Agnes Raj, Luke Tuxworth and Mike Watson, the advanced characterisation department, and the director and technology managers of the Johnson Matthey Technology Centres.

By |2022-01-05T11:31:47+00:00January 5th, 2022|Weld Engineering Services|Comments Off on In the Lab: Spotlight on Surface Characterisation Activities at Johnson Matthey

Using Spraying as an Alternative Method for Transferring Capsules Containing Shea Butter to Denim and Non-Denim Fabrics

The concept of wellness has been talked about in recent times in relation to health and a healthy lifestyle. Similarly the wellness or health-improving finishing processes of textiles have gained importance. Cosmetic textiles, also known as wellness textiles, are considered examples of these clothing products (1, 2). Cosmetic textiles are textile products that release a specific substance or solution to the human body, usually to the skin, at certain time intervals; they are claimed to have properties such as cleaning, perfuming, change in appearance, protection and improvement of body odour (1). Such garments, which are mainly designed to transfer certain active substances for cosmetic purposes through contact with the skin, are in increasing demand today, especially in developed nations, where the desire of people to live a longer and higher quality life and to look younger has created a demand for beautifying and anti-ageing products (3).

Advances in cosmetic textiles have been achieved by physically or chemically bonding microcapsules containing cosmetics to the fibre surface. Microencapsulation, which plays an important role in the development of cosmetic textiles, is a technique of packaging active substances in solid, liquid or gas form into a second substance to protect the active substance from the environment (4, 5).

The encapsulation process produces small spheres covered with a thin shell or film to protect the active substance. Using this technology, it is possible to protect easily perishable substances such as insecticides, antibacterials and antioxidants from environmental factors like heat, light and oxygen. In addition, the wearer is exposed to much lower doses of these substances. Using microcapsules in textile finishing, it is possible to produce resistant-to-wash textile products that are effective even when less active substance is used (615).

Recent studies have shown microencapsulation for cosmetics to be a logical and effective solution in terms of protection and as a carrier for active ingredients. Microencapsulation has the potential to deliver active ingredients in certain difficult situations, such as when these substances contain glycolic acid, alpha hydroxy acids or salicylic acid or when they have high alcohol content or critical water-in-oil or silicone emulsions. They can be used to deliver active ingredients to the skin in a safe, targeted, effective and painless manner, protecting compounds such as antioxidants from oxidation and from degradation by heat, light and moisture or controlling the release rate (16, 17). Microencapsulation can be used in cosmetic applications such as the production of shower and bath gels, lotions and creams, hair products, sunscreens and tanning creams, makeup, perfumes, soaps and toothpastes, among others. Microencapsulation can help improve the cosmetic and personal care industries through innovation, allowing the production of high-added-value products in response to human needs and desires (1821). In other studies, biopolymers (natural polymers) and biodegradable polymers such as chitosan were used as encapsulating materials, with greater interest for applications in the field of skin delivery systems (2224).

In general, the transfer of microcapsules is done using the impregnation and exhaustion method in the textile industry. The spraying method, however, is becoming more commonly used in the textile industry in order to reduce the amount of water, chemicals and energy. This is more sustainable because it works with low liquor ratios and less water, chemical consumption and waste in comparison with traditional methods. Therefore this method was chosen as an alternative to the exhaustion method (25, 26).

Ethyl cellulose, which was chosen as shell material, is a rigid, thermoplastic and hydrophobic material. This polymer is resistant to water, alkali and salt. It is compatible with the spray dryer technique and can be applied to a textile surface. The spray drying method is very popular among users in the pharmaceutical and food industries because of its characteristics of fast heat-transfer, rapid water evaporation and short drying time. It can improve the dissolution rate of certain formulations. In this method, materials can be directly dried into powder. It is easy to change the drying conditions and adjust product quality standards, it has high production efficiency and large production capacity (27, 28). Shea butter is a fat extracted from the nut of the African shea tree (Vitellaria paradoxa). In addition to many nonsaponifiable components, shea butter usually contains the following fatty acids: oleic acid (40–60%), stearic acid (20–50%), linoleic acid (3–11%), palmitic acid (2–9%), linolenic acid (<1%) and arachidic acid (<1%). Shea butter melts at body temperature. Proponents of its use for skin care maintain that it absorbs rapidly into the skin, acts as a ‘refatting’ agent and has good water-binding properties (2932).

In this study, it was aimed to evaluate the behaviour of microcapsules that contain shea butter transferred with the spraying method to become an alternative to conventional methods. Firstly, shea butter carrying ethyl cellulose microcapsules were produced with spray dryer method. As part of characterisation studies of microcapsules, Fourier transform infrared (FTIR) spectroscopy, scanning electron microscopy (SEM) and gas chromatography–mass spectrometry (GC-MS) analyses were performed. The optimum formula was applied to denim and non-denim fabrics by the exhaustion and spraying methods in order to investigate whether the spraying method can be an alternative to the conventional exhaustion method. After application of microcapsules containing shea butter to textile materials, the existence of capsules on the fabrics were examined after five wash cycles. Some physical tests (air permeability, tensile strength and stretching) were performed on the fabrics after treatment with capsules to evaluate the effect of the encapsulation process on denim and non-denim fabric properties. It was also examined whether there is a difference between denim and non-denim fabrics in the presence of microcapsules.

2.1 Material

In this research, desized, 3/1 twill weave, 98% cotton and 2% elastane denim and non-denim fabrics (specific weight 340–370 g m−2) were used. The shell material ethyl cellulose was donated from Acros, Belgium. Shea butter (Tabia, Aydın) were employed as core materials. Tween® 20 was used as a surfactant. The surface active agent, ethanol and ethyl acetate were supplied from Merck, Darmstadt, Germany. Nano polyurethane crosslinker (Tanatex, Switzerland) was used to bond the microcapsules to the fabric surface. All other auxiliary chemicals used in the study were of laboratory-reagent grade.

The fabric properties used in the study are shown in Table I.

Table I

Properties of Denim and Non-Denim Fabrics

Fabric Composition Weight, g m−2 Weaving type Fabric type
98/2 – CO/EA 348.3 ± 3.1 3/1 Z Twill Denim
98/2 – CO/EA 340.0 ± 2.9 3/1 Z Twill Non-denim

2.2 Preparation of the Microcapsules

In order to obtain the microcapsules, the capsules were prepared with the spray dryer method. In this process the interactions of water-insoluble polymers with water are utilised to form the microcapsules. Firstly, shea butter, which is solid at room temperature, was melted at 50°C. Ethyl cellulose and shea butter were dissolved homogenously in organic solvent in a specific ratio. Polymer-rich organic phase was added to polymer-free aqueous phase. Active ingredients were mixed with a Silverson high shear mixer. Afterwards, a spray dryer (SD-Basic LabPlant, Huddersfield, UK) was used to collect the microcapsules. The compositions were fed to the spray dryer at the following conditions for each batch size: feed flow rate of microencapsulating composition 10 ml min−1; inlet air temperature 125°C and outlet air temperature 85°C. Microcapsules were collected from the product vessel using a soft brush in the fume hood and transferred to glass containers for storage. Chemical quantities and test conditions for spray dryer are given in Table II. Three different core:shell ratios were tested to obtain the optimal conditions for microencapsulation of shea butter. The most homogeneously distributed and high yield capsule production was optimised. For this purpose, the ratio of shea butter was varied to examine the encapsulation state of the active substances as shown in Table II.

Table II

Chemical Quantities of Capsules and Test Conditions for Spray Dryer

Code Shea butter, g Ethyl cellulose, g Ethyl acetate, ml Inlet air temperature, °C Outlet air temperature, °C Aspirator, % Pump, %
S1 9 3 500 125 85 90 2.5
S2 6
S3 3

2.3 Particle Morphology of Microcapsules

The morphologic properties of the capsules were evaluated using SEM (QuantaTM 250 FEG, FEI Co, USA). Samples were gold-coated (15 mA, 2 min) to assure electrical conductivity. The measurements were taken at 2 kV accelerating voltage. The images were taken at 5000× magnifcation.

2.4 Particle Size of Microcapsules

To determine the size of the resulting optimum capsule, a Zetasizer Nano S (Malvern Panalytical, UK) particle-size distribution tester was used. Before measurement, an aqueous solution of capsules in a certain ratio was prepared and sonicated in an ultrasonic bath until a good mixture was formed. After that, the capsule dispersion was put in disposable cuvettes. Then, the light emitted by the laser Doppler was passed through the dispersion.

2.5 Mass Yield of Microcapsule

The total powder obtained after spray drying was weighed, and the process yield was calculated as a percentage of the amount of solids added during the preparation process according to Equation (i):

(i)

where R% is the yield of the process, Qi is the amount of solids initially added for the preparation of capsules and Qf is the quantity of microcapsules obtained at the end of the process.

2.6 Fourier Transform Infrared Analysis

FTIR spectroscopy analysis was performed to determine encapsulation performance with the changes in the infrared (IR) spectrum for optimum capsule formulation. Measurements were taken at a wavelength range of 4000–400 cm−1 using a PerkinElmer® FrontierTM FTIR device. The obtained spectra were smoothed to remove noise with the official software of the device.

2.7 Differential Scanning Calorimetry Analysis

Differential scanning calorimetry (DSC) was performed using a PerkinElmer® PYRISTM Diamond differential scanning calorimeter for the purpose of distinguishing complex formation from simple physical mixing with the help of characteristic endothermic or exothermic peaks. The analyses were conducted in nitrogen medium between 0°C and 300°C. The scanning rate was stated as 5°C min−1.

2.8 Application of the Microcapsules to the Denim and Non-Denim Trousers

Denim and non-denim trousers to be used for capsule transfer were first subjected to the denim washing procedure. This procedure covers ageing processes that are made to give denim fabrics an aged appearance and can vary from very light tones to dark tones in line with customer demands. In this study, after rinse washing, stone washing and softening the trousers were turned over and the capsules were transferred.

The application of the selected optimum formulations to the fabrics was carried out with exhaustion and spraying methods. Capsule transfer was carried out according to Table III in the same ratio to compare the application processes. Nano-polyurethane was selected as binder and each experiment was repeated three times. The optimum capsule sample (6 g l−1) and the binding agent (1.2 g l−1) were dissolved in water and then transferred to the trousers with spraying and exhaustion methods.

Table III

Capsule Transfer Prescription for Spray and Exhaustion Methods

Capsule, g l−1 Binder, g l−1 Drying Fixing
Temperature, °C Time, min Temperature, °C Time, min
6 1.2 40 20 120 5

The spraying and exhaustion operations were carried out in the Magic Box model Metaflow MET‐FLW drum machine shown in Figure 1. This system is used to coat denim jeans or any other textile garments with chemicals applied into the drum during tumbling. In the exhaustion method, the fabrics were treated with a bath containing a concentration of 5 g m−2 microcapsules in the presence of binder at 40°C for 20 min in the drum machine. In the spraying method, 5 g m−2 capsules and binder were sprayed at spraying speed of 100 g min−1 with a spray system attached to the same machine. To achieve long lasting effect, fabrics were dried in a circulating air oven at 40°C for 20 min and just after drying, the fabric was mounted on pin frames and exposed for 5 min to 120°C in a laboratory stenter.

Fig. 1

Drum machine used for capsule transfer

Drum machine used for capsule transfer

After microcapsule application, the fabrics were washed according to ISO 3758:2012 (33) standard to determine the resistance to domestic repetitive washing and durability of capsules. In addition, rubbing tests were carried out according to ISO 105-X12:2016 (34) standard, because of the importance of the rubbing test for denim and non-denim trousers.

2.9 Evaluation of Treated Fabrics

SEM images were taken to determine the existence of capsules on the textile surface from washed, unwashed and rubbed samples. Samples were gold-coated (15 mA, 2 min) to assure electrical conductivity. The measurements were taken at 2 V accelerating voltage. The images were taken at 5000× magnifcation.

DSC was performed using a PerkinElmer® Diamond differential scanning calorimeter for the purpose of distinguishing the capsules on the denim and non-denim fabric with the help of characteristic endothermic or exothermic peaks. The analyses were conducted in nitrogen medium between 0°C and 300°C. The scanning rate was stated as 5°C min−1.

Gas chromatography (GC) is a common type of chromatography used in analytical chemistry for separating and analysing compounds that can be vaporised without decomposition. The fabrics were extracted to analyse the contents of the capsules containing shea butter transferred to the fabrics. For GC analysis, an Agilent 7820a model GC‐MS + Headspace Sampler device (Agilent, USA) was used. GC device oven temperature was raised to 40°C and left for 3 min. Later, it was brought to 180°C by increasing at a rate of 7°C min−1. After that, it was brought to 240°C by increasing at a rate of 30°C min−1. It was left for 5 min at 240°C. An injector with a volume of 3 μl was used for sampling. Helium gas was used in the analysis. It was run in the ‘split’ mode at a flow rate of 1:200 at 1.5 ml min−1. The injector temperature was set to 250°C and the column pressure to 37.1 kPa.

Air permeability analysis was performed on both denim and non-denim products according to TS 391 EN ISO 9237:1995 (ASTM D737-18) (35) standard in order to examine the effect of microcapsule application on the comfort properties of the products.

Tear strength of the fabrics were measured according to TS EN ISO 13937–2:2000 (36), using an Instron® 4411 tensile strength tester. Elasticity and elastic recovery analyses were made according to ASTM D3107-072019 (37) standard.

An experimental framework in schematic form is provided in Figure 2.

Fig. 2

Experimental framework

Experimental framework

In this study, capsules containing shea butter were prepared by the spray dryer method. This method is a simple, viable method to obtain microcapsules, suitable to prevent biological activity loss, avoiding exposure to elevated heating and to organic solvents.

3.1 Particle Morphology of Microcapsules

Spray dried microcapsules are usually characterised by spherical shape and narrow particle size distribution. Typical photomicrographs were obtained by SEM of the microcapsules and show that the spray-dried product is composed mainly of spherical shaped particles (Figure 3).

Fig. 3

SEM images of microcapsules

SEM images of microcapsules

According to SEM analysis, microcapsules filled with active substance (shea butter) were obtained. However, when the micrographs of S1 and S2 coded microcapsule were examined, it was observed that not all particles appeared morphologically spherical. Some of the microcapsules’ centres were collapsed and agglomerated due to sudden solvent evaporation when the polymer solution was introduced into the hot air chamber and also capsule distribution was not homogeneous (38). The biggest cause of shea butter-induced collapse in capsules is thought to be failure of the active ingredient to be encapsulated, resulting in its accumulation on the shell material. When SEM images of S2 coded microcapsules were examined it was seen that the size distribution and capsule shapes were not homogeneous. Therefore, according to SEM images of the microcapsules, the optimum shea butter content to get homogenous spherical microspheres was seen in S3 coded microcapsules. So, other characterisation and capsule transfer studies were carried out with the S3 coded capsule.

3.2 Particle Size of Microcapsules

The mean particle size of microparticles was determined by laser diffraction method for microcapsules. Particle size distribution graphs of the microcapsules are indicated in Figures 46.

Fig. 4

Particle size distrubiton of the S1 capsules

Particle size distrubiton of the S1 capsules

Fig. 5

Particle size distrubiton of the S2 capsules

Particle size distrubiton of the S2 capsules

Fig. 6

Particle size distrubiton of the S3 capsules

Particle size distrubiton of the S3 capsules

The particle size of the three formulated capsules (S1, S2 and S3) loaded with shea butter ranged between 369 μm and 420 μm. The particle size results of the microcapsules are presented in Table IV.

Table IV

Particle Size Distribution of Microcapsules

Formulation Particle Size Distribution, nm
S1 400 ± 20
S2 397 ± 18
S3 390 ± 21

When the particle size analysis of the capsules produced at different ratios was evaluated, the S1 coded capsules had a particle size of 400 nm and a high homogeneity. The particle size was 397 nm for S2 coded capsules. According to the data obtained as a result of the analysis, it was determined that 97.9% of the capsules were around 390 nm for S3 coded capsules. It was determined that the particle size analysis graph area showed a uniform distribution. When particle analysis results are evaluated, it was determined that shea butter based capsules with different ratios were homogeneously distributed and had a close value to each other.

3.3 Mass Yield of Microcapsules

The yield of microcapsules produced by a laboratory-scale spray dryer may not be high due to loss of lightweight particles by vacuum suction and adherence to the inside wall of the spray dryer apparatus. The mass yields ranged between 50.9% and 79.4% (w/w) as shown in Table V. A reduction in the amount of active substance in the formulation affected the production efficiency positively. In connection with SEM and particle size analysis, it has been determined that the failure of active substance to be encapsulated caused agglomeration in S1 (3:1 shea:ethyl cellulose) and S2 (2:1 shea:ethyl cellulose) coded capsule formulations.

Table V

Mass Yield of Microcapsules

Formulation Mass yield, ethyl cellulose: Econea®, % w/w
S1 50.9 ± 1.5
S2 55.1 ± 1.7
S3 79.4 ± 2.5

The yield values of the capsule experiments with shea butter and three different molar ratios were calculated and it was concluded that the S3 coded capsules had the highest yield.

After SEM, particle size and mass yield of microcapsules analyses, S3 coded capsules were selected as the optimum ratio. For this reason, FTIR and DSC analyses were carried out over the determined S3 optimum capsules.

3.4 Fourier Transform Infrared Analysis

The FTIR spectra of shea butter capsules and the materials forming them are given in Figure 7.

Fig. 7

FTIR spectra of (a) ethyl cellulose; (b) shea butter; (c) S3 coded capsules

FTIR spectra of (a) ethyl cellulose; (b) shea butter; (c) S3 coded capsules

The characteristic peaks of shea butter were obtained in the FTIR spectra. In the hydrogen stretching region, the following peaks were seen: 2920 cm−1, 2852 cm−1, 2917 cm−1, 2851 cm−1. These bonds signal the presence of symmetric and asymmetric stretching vibration of the aliphatic CH2 group. In the second spectral region of double bond stretching, frequency of 1741 cm−1 occurred, which indicates that the ester carbonyl functional group of the triglycerides is present. The third region of deformation and bending in the functional group showed bonds at 1460 cm−1 as well as 1370 cm−1 and 1475 cm−1 for shea butter. The peaks at 1460 cm−1 indicate bending vibrations of the CH2 and CH3 aliphatic groups while 1370 cm−1 and 1475 cm−1 peaks showed bending vibration of the CH2. In the fingerprint region, the bonds at 1243 cm−1, 1165 cm−1 and 1250 cm−1, 1170 cm−1 indicate the presence of shea butter. These bonds signal the stretching vibration of the C–O ester groups (39, 40).

When the IR spectrum of ethyl cellulose was examined, the stretching vibrations of characteristic –C–O–C– band and –C–H band were observed at 1054 cm−1 and at 2870 cm−1 and 2972 cm−1, respectively. The C–C stretching vibration was located at 1640 cm−1. When the spectra of the capsules were examined, both ethyl cellulose and shea butter peaks were identifed. The strong peak of ethyl cellulose at 1053 cm−1 due to the –C–O–C– band was observed in the capsules. The C–H bands obtained at 2973 cm−1 and 2870 cm−1 were found to be deeper than ethyl cellulose peaks and close to the peak intensity of shea butter. This may indicate successful encapsulation.

3.5 Evaluation of Treated Fabrics

After characterisation using SEM, particle size and mass yield of microcapsules, the S3 coded capsules were determined as the optimum formulation. The capsules were transferred to denim and non-denim fabrics by exhaustion and spraying methods and compared.

SEM images of denim and non-denim fabrics are indicated in Figure 8. These images show that capsule application succeeded for both exhaustion and spraying methods. It was observed that capsules were covered with the binder and fixed onto the textile surface for denim and non-denim fabrics. Also, the effect of repeated washings on capsules was evaluated. Capsules on the textile surface and embedded in the binder were observed even after five washes and rubbing test for both methods and fabrics.

Fig. 8

SEM micrographs of denim and non-denim fabrics treated with shea butter oil capsules with no wash, after five washes and after rubbing

SEM micrographs of denim and non-denim fabrics treated with shea butter oil capsules with no wash, after five washes and after rubbing

As a result of the SEM analysis, it was observed that the transfers made by the spraying method have similar results to the transfers made by the exhaustion method. It was concluded that capsules can also be transferred by the spraying method which can be used as an alternative to the conventional exhaustion method. Therefore, in order to determine the efficiency of the spraying method, analyses were carried out on the fabrics with capsules transferred by the spraying method.

3.6 Differential Scanning Calorimeter Analysis

The DSC diagrams of ethyl cellulose are given in Figure 9. When the DSC spectrum of shea butter is examined, based on data from Sigma Aldrich, the glass transition temperature (Tg) of ethyl cellulose is about 155°C. The melting temperature of shea butter is about 35–37°C in accordance with the literature (41). The endothermic movement observed at 169.64°C in the DSC analysis of ethyl cellulose is thought to be related to the glass transition temperature. When the microcapsules obtained with shea butter were examined, peaks corresponding to the melting point of the active substance are seen. It was concluded that these small peaks were due to the non-encapsulated active substance. When the DSC spectrum of microcapsules developed with shea butter and ethyl cellulose were examined, low intensity exothermic peaks were observed at 37°C. The reason for the low intensity of these peaks due to shea butter was attributed to being confined by ethyl cellulose.

Fig. 9

DSC diagrams of ethyl cellulose

DSC diagrams of ethyl cellulose

DSC diagrams of shea butter capsule transferred denim and non-denim fabrics are shown in Figure 10. When the DSC graphs of shea butter transferred fabrics were examined, similar graphs were seen in both denim and non-denim fabrics. This is thought to be due to the use of the same material (containing cellulose) as the raw material. As a result of SEM and DSC analysis, no difference could be detected between denim and non-denim fabrics (42, 43).

Fig. 10

DSC diagrams of shea butter, S3 coded capsules, shea butter capsule transferred denim and non-denim fabrics

DSC diagrams of shea butter, S3 coded capsules, shea butter capsule transferred denim and non-denim fabrics

The GC analysis results of fabrics transferred to microcapsules containing shea butter and the same samples after five washes are shown in Figure 11. As a result of GC analysis, shea butter peaks can be clearly seen in the GC diagrams. It was found that some of these peaks decreased after five washes, but significant peaks remained for shea butter. Oils transferred to the fabric in capsule form were protected.

Fig. 11

GC diagrams of shea butter capsule transferred fabrics and after five washes

GC diagrams of shea butter capsule transferred fabrics and after five washes

When the physical analysis results in Table VI are examined, it can be concluded that microcapsule application on both denim and non-denim products did not significantly affect the tear strength, elasticity and elastic recovery of the fabrics. The breaks in the warp direction were an expected result in denim products. If there is a break in the warp direction in denim fabrics, it means that the strength of the weft direction is above the standards and this situation is within acceptable limits for fabrics. The test results were evaluated by IBM® SPSS® software to examine the difference between the denim and non-denim fabrics. Results showed that the effect of fabric type is statistically significant for all microcapsule procedures and p value is 0.000 (p < 0.05).

Table VI

Physical Properties of Denim and Non-Denim Fabrics

Fabric Tear strength Elasticity, % Elastic recovery, %
Weft, N Warp, N
Raw fabric Denim 10.97 ± 0.81 21.51 ± 0.98 33.27 ± 1.25 10.00 ± 0.50
Capsule transferred trousers Denim 9.16 ± 0.76 Break 32.50 ± 1.12 8.00 ± 0.50
After five washes Denim 12.16 ± 0.91 21.98 ± 1.01 32.65 ± 1.14 7.50 ± 0.50
Raw fabric Non-denim 26.00 ± 1.21 Break 28.94 ± 1.09 6.5 ± 0.50
Capsule transferred trousers Non-denim 25.72 ± 1.17 35.62 ± 1.61 39.34 ± 1.55 6.5 ± 0.50
After five washes Non-denim 24.71 ± 1.07 31.34 ± 1.32 35.90 ± 1.42 7.5 ± 0.50

In order to examine the effect of microcapsule application on the comfort properties of the products, air permeability analysis was performed on both denim and non-denim fabrics according to the TS 391 EN ISO 9237:1995 (ASTM D737‐18) (35) standard and the results are stated in Table VII. When the air permeability results are examined, it can be observed that microcapsule application on both denim and non-denim products did not significantly affect air permeability.

Table VII

Air Permeability Results of Denim and Non-Denim Fabrics

Raw fabric Capsule transferred
Denim Non-denim Denim Non-denim
Air permeability values, mm s−1 18.14 18.74 19.50 20.60
Standard deviation 0.45 1.10 0.27 0.89
Coefficient of change, % 2.41 6.04 1.41 4.31

Within the scope of this study, shea capsules were produced successfully with the spray dryer method. In this method, materials can be directly dried into powder to produce shea microcapsules. It is easy to change the drying conditions and adjust product quality standards. The method has high production efficiency and large production capacity. These advantages will enable this method to be used in capsule production in future studies. Denim and non-denim products were developed by encapsulating shea butter with ethyl cellulose which were then successfully applied on denim and non-denim fabrics. The capsules remained on the fabric at a certain rate after five washes. When physical properties such as air permeability, tear strength and elasticity of the fabrics were examined, it was seen that the capsules did not create any negative effects on the fabrics. Denim and non-denim fabrics were compared with each other. As a result of SEM and DSC analysis, no difference could be detected between denim and non-denim fabrics as they consist of similar (cellulosic) materials.

Transferring microcapsules to denim and non-denim fabrics by spraying method is an innovation for the denim sector. Transfer of microcapsules that give functional properties to textile materials is mostly done by impregnation and exhaustion methods. In this study, the efficiency of the spraying method was compared with the conventional transfer method. As a result of the comparisons, the main objectives of the study have been achieved in both methods. The spraying method provided a more sustainable process as it uses less water, has lower chemical consumption and produces less waste compared to the exhaustion method, which works at higher liquor rates. When transferring with the spray method, the temperature and processing time used during the exhaustion method are eliminated. With this study, we demonstrate that adoption of the spraying technique for microcapsule application could be an efficient way to produce textiles while minimising energy and resource consumption.

By |2022-01-05T10:59:43+00:00January 5th, 2022|Weld Engineering Services|Comments Off on Using Spraying as an Alternative Method for Transferring Capsules Containing Shea Butter to Denim and Non-Denim Fabrics

Screening for Bioactive Compound Rich Pomegranate Peel Extracts and Their Antimicrobial Activities

Johnson Matthey Technol. Rev., 2022, 66, (1), 81

In this work, seven different extracts from pomegranate (Punica granatum L., cv. Hicaz nar) peel were prepared by using different solvents (ethanol, methanol, either alone or in combination with acid, acetone and water). The phenolics (punicalagins and ellagic acid), organic acids (citric acid and malic acid) and sugars of pomegranate peel extracts (PPEs) were determined. The highest amounts of punicalagins and ellagic acid were detected by ethanol-acid extract as 13.86% and 17.19% w/v respectively, whereas the lowest levels were obtained with acetone and water extracts. Moreover, the methanol-acid (3.19% malic acid) and ethanol-acid (1.13% citric acid) extracts contained the highest levels of organic acids. The antimicrobial activities of extracts were investigated by agar well diffusion method. Methanol-acid and ethanol-acid extracts exhibited the highest antimicrobial effects on all tested microorganisms, giving inhibition zones ranging in size from 17 mm to 36 mm. Although similar antimicrobial activities were observed by ethanol, methanol and acetone extracts (up to 24 mm), the lowest antimicrobial activities were attained by water extract (0–15 mm). All extracts were generally more effective against Gram-positive bacteria: Enterococcus faecalis, Bacillus subtilis, Bacillus cereus than Gram-negative ones: Escherichia coli and Enterobacter aerogenes (Klebsiella aerogenes). It was shown that extracts from pomegranate peels represent a good source of bioactive compounds.

1. Introduction

Punica granatum L. is a tree belonging to the Punicaceae family grown in Iran, Afghanistan, Turkey, the USA and Far East countries. The world pomegranate production is estimated as 1.5 million tonnes annually (1). Pomegranate juice is popular and is claimed to include antibacterial, anticancer, antioxidant, antiallergic and anti-inflammatory compounds (2, 3). Recent reports also showed its potential use in the treatments of cardiovascular diseases and diabetes (4).

The pomegranate peel amounts to more than half of the weight of the pomegranate. It is a fruit processing-waste but it could be used as a source of antioxidants, phenols, flavonoids and organic acids. Extracts of pomegranate peels including rind, husk, pericarp and membranes are rich in polyphenols (ellagitannin and punicalagins), gallic acid, flavones, flavanones and anthocyanidins (57). These phenolic compounds and organic acids can be extracted by using different solvents. The efficiency of extraction is mostly dependant on the type of solvent, time and temperature. Therefore, it is important to determine the best solvent and extraction method to obtain the best bioactive compound rich extracts. Many extraction methods are reported for extraction of phenolic compounds from pomegranate by using ethanol, methanol, acetone, ethyl acetate and water (8, 9).

The presence of punicalagins, punicalin, ellagic acid and gallic acid in PPEs could determine their antimicrobial activities on microorganisms (10, 11). PPEs prepared by using ethanol, methanol or their mixtures with water were shown to be effective on Staphylococcus aureus, Enterobacter aerogenes, Klebsiella pneumoniae and Salmonella typhi strains (10). Abdollahzadeh et al. (12) reported that the methanolic extract of pomegranate peel exhibited antimicrobial activities against oral pathogens including S. aureus and Staphylococcus epidermidis strains. Moreover, PPEs containing polyphenols, tannins and other secondary metabolites showed effective antibacterial activity against shiga toxin producing E. coli (STEC) (13). Extracts from other parts of pomegranate (such as rinds, membranes and seeds) also had antimicrobial effects on S. aureus and Bacillus megaterium (14). To the best of our knowledge there is no report for evaluation of antimicrobial activities of different PPEs for Turkish Hicaz variety. Therefore, in the present study the most efficient extraction methods were investigated to obtain potential natural antimicrobial compounds from Turkish Hicaz pomegranate peel that can be used as a source of safe preservatives in the food industry. For this, different solvents (ethanol, methanol, either alone or in combination with acid, acetone and water) were used for extraction of phenolics and organic acids from pomegranate fruit peels obtained as a waste from fruit juice processing industry. Extracts were then screened for their antimicrobial activities against some important microorganisms.

2. Materials and Methods

2.1 Preparation of Pomegranate Waste

Pomegranate (Punica granatum L., cv. Hicaz nar) peels were obtained from fruit processing industry in Turkey and stored at 4°C. The peels were lyophilised in a freeze dryer (VirTis Ultra Pilot Lyophilizer with a Wizard 2.0 control system, SP Industries, USA) by freezing at –30°C for 5 h and drying under 10 Pa pressure at 20°C for 24 h. The freeze-dried peels were ground to powder (No. 48 sieve) using a grinder and stored at 4°C until use.

2.2 Chemicals

Ellagic acid, punicalagins (A and B forms) and gallic acid standards were purchased from FlukaTM (USA). Malic acid and citric acid standards were obtained from Merck KGaA (Darmstadt, Germany). Ethanol (99% v/v), methanol (99% v/v), acetone (99% v/v), and hydrochloric acid (HCl; 37% v/v) were used as solvents (Merck).

2.3 Preparation of Pomegranate Peel Extracts

5 g of pomegranate peel powder was mixed with 100 ml of different solvents and incubated at 50°C for 30 min or 2 h in an ultrasonic water bath (150 W, 40 KHz) (E1: ethanol for 30 min, E2: ethanol for 120 min, EA: ethanol with HCl, M: methanol, MA: methanol with HCl, A: acetone and W: distilled water, for 30 min, Table I). The mixtures were centrifuged at 4°C at 4000 rpm for 15 min as described by Zhang et al. (15) and Türkyýlmaz et al. (14) with slight modifications (Scheme I). The supernatants were filtered with Whatman® Grade 1 paper and then evaporated in a rotary evaporator (Heidolph Instruments, Germany) at 50°C under a vacuum of 400 mbar. The extracts were stored at 4°C until used for further studies.

Table I

Extraction Methods for Different Pomegranate Peel Extracts Used in This Study

Extract Solvents Solvent ratio, % v/v Extraction time, min
E1 EtOH:Dwa 60:40 30
E2 EtOH:Dw 60:40 120
EA EtOH:HCl:Dw 60:5:35 30
M MeOH:Dw 80:20 30
MA MeOH:HCl:Dw 80:5:15 30
A Acetone:Dw 70:30 30
W Dw 100 30

Scheme I.

Schematic representation for preparation of PPEs and determination of their antimicrobial activities

Schematic representation for preparation of PPEs and determination of their antimicrobial activities

2.4 Qualitative Analysis of Phenolics and Sugars

Sugar and phenolic contents of PPEs were screened by thin layer chromatography (TLC). About 1 μl of each extract and standards were applied on TLC plate. For screening of phenolics, the plate was run into ethyl acetate:glacial acetic acid:formic acid:distilled water (100:11:11:5, v/v; adapted from Kumar et al. (16)). The plates were then sprayed with 5% w/v ferric chloride reagent (13). For sugars, the plate was run into acetonitrile:water (85:15, v/v) solvent system and then stained with α-naphthol (0.5% w/v) dissolved in ethanol solution acidified with H2SO4 (5% v/v), followed by heating at 110°C for 10 min (17). The colours of the spots were identified. An individual retention factor (Rf) value for each spot was measured and compared with standard reference sugars and phenolic compounds run in the same respective solvent systems.

2.5 Quantitative Analysis of Phenolics, Sugars and Organic Acids

Detection and quantification of phenolics, organic acids and sugars were carried out by high-performance liquid chromatography (HPLC) system. Each sample was centrifuged and then filtered through 0.22 μm membrane filter before HPLC analysis.

Ellagic acid and punicalagin separations were achieved at 30°C on a C18 column (150 mm × 4.6 mm, 5 μm, GL Sciences Inc, Japan). HPLC analysis was performed using Class VP, 20 AD series (Shimadzu Corporation, Japan) equipped with photodiode-array detector (PDA) and an autosampler. The mobile phase consisted of formic acid (1%) and acetonitrile with gradient mode elution (0–18 min, 15% v/v acetonitrile, 20 min 65% v/v acetonitrile, 25 min 5% v/v acetonitrile and 30 min 5%, v/v acetonitrile) at a flow rate of 1 ml min–1. The injection volume was 10 μl. The quantitation wavelength was set at 255 nm (18). 1000 μg ml–1 of ellagic acid, gallic acid and punicalagins were prepared by dissolving in 5 ml of HPLC grade methanol for standards. The solutions were stored at –20°C. The calibration curves were established from the standards of punicalagins and ellagic acid at concentrations between 0.005–0.02% and 0.25–1%, respectively.

Sugars (glucose and sucrose) were determined by using NH2 column (250 mm × 4.6 mm, 5 μm, GL Sciences Inc). The column temperature was 25°C. The eluted samples were detected by refractive index detector (RID). The mobile phase consisted of acetonitrile (60%) and ultra-pure water (40%). Flow rate was 1 ml min–1 and injection volume was 20 μl (19). The standards of glucose and sucrose (5 mg ml–1, 10 mg ml–1, 20 mg ml–1, 40 mg ml–1 and 50 mg ml–1) were used for calibration curves.

Organic acids (citric and malic acids) were determined with an ultraviolet-visible (UV-vis) detector (Shimadzu SPD-10A VP, Shimadzu Corporation). All organic acid analyses were carried out with a Kromasil® C18 HPLC column (5 μm, 4.6 mm × 156 mm). The mobile phase was prepared by using 0.005 N sulfuric acid. Injection volume was 50 μl and the column temperature was 25°C. Flow rate was 0.3 ml min–1. The data were recorded at 210 nm (20). Citric and malic acid standards (0.1–2% w/v) were used to prepare calibration curves.

2.6 Antimicrobial Analysis

The antimicrobial efficacies of PPEs were evaluated against E. coli (ATCC® 25922), E. faecalis (ATCC® 29212), B. subtilis (ATCC® 6633), B. cereus (ATCC® 11778), Pseudomonas aeruginosa (ATCC® 27853), Streptococcus uberis (ATCC® 700407), E. aerogenes (ATCC® 13048) and Candida albicans (ATCC® 10231) by using agar well diffusion method (Scheme I). Each microbial culture was incubated in Mueller Hinton Broth (MHB, Merck) overnight. The OD600 values of cultures were adjusted to 0.1 and then 100 μl of each microbial culture was spread on petri dishes containing 17 ml of Mueller Hinton Agar (MHA, Merck). The media were punched with 7 mm diameter wells and these wells were filled with 40 μl of each extract. The plates were then incubated for 24 h at 37°C. After incubation, inhibition zones for microorganisms for each extract were measured in millimetres. Each extract was tested three times.

2.7 pH Measurements

The pH levels of extracts were measured by a pH meter (HI-2211 Bench Top pH & mV Meter, Hanna Instruments Ltd, UK).

2.8 Statistical Analysis

Values are expressed as mean ± standard deviation. Data were analysed by student t-test. The level of statistical significance was accepted as p<0.05.

3. Results and Discussion

3.1 Phenolics

Punicalagins (punicalagin A and B) and ellagic acid were identified in all extracts by TLC. However, gallic acid was not determined in all extracts according to both TLC and HPLC analyses.

The highest levels of punicalagins and ellagic acid were detected in the EA extract as 13.86% and 17.19% respectively, whereas the lowest levels were obtained with W extract (p<0.05) (Figure 1) by HPLC analyses. This is consistent with previous results which reported that the solvents could affect the phenolic contents of plant extracts (21, 22). The difference in phenolic contents of extracts depends on the solvent polarity that affects solubility of selected groups found in antimicrobial bioactive compounds (8). Water, ethanol and methanol are polar solvents while acetone is an intermediate polar solvent that can dissolve both polar compounds including phenolics and nonpolar compounds. In addition, the extracts obtained by mixture of solvents (combination of acid and ethanol or methanol) could contain more radical scavenger than the pure solvents (23) by changing polarity that affects antimicrobial activities. It was also observed that ethanol alone or ethanol-acid combination could be more effective than other solvents to obtain high levels of phenolic compounds. The antimicrobial activities of phenolics (ellagic acid and punicalagins) were shown previously (24, 25). These polyphenols found in PPEs can work as antimicrobial agents by forming a complex with the bacterial cell to cause death or by inhibiting protein activities. The position and the number of hydroxyl groups on the phenolic components may also increase this inhibitory effect on the microorganisms (26, 27).

Fig. 1.

The phenolic contents (punicalagins and ellagic acid, %) of PPEs (E1: ethanol for 30 min, E2: ethanol for 2 h, M: methanol, EA: ethanol-acid and MA: methanol-acid, A: acetone and W: water). Values are the averages of three determinations; error bars represent standard deviations

The phenolic contents (punicalagins and ellagic acid, %) of PPEs (E1: ethanol for 30 min, E2: ethanol for 2 h, M: methanol, EA: ethanol-acid and MA: methanol-acid, A: acetone and W: water). Values are the averages of three determinations; error bars represent standard deviations

3.2 Sugars

The highest total sugar contents (glucose and sucrose) were obtained with MA (5.95%), E2 (4.98%) and EA (4.93%) extracts (p<0.05) (Table II). MA and EA extracts exhibited the highest antimicrobial activities (Figure 2). Sugars might help the antimicrobial efficacies of these extracts due to the osmotic effects of carbohydrates on microorganisms. However, there was no clear consistency for the sugar contents and antimicrobial activities of other extracts.

Fig. 2.

Inhibition zones (mm) exhibited by different PPEs: (a) E1: ethanol for 30 min, E2: ethanol for 2 h, EA: ethanol-acid; (b) M: methanol and MA: methanol-acid; (c) A: acetone and W: water) against several microorganisms. Values are the averages of three determinations; error bars represent standard deviations

Inhibition zones (mm) exhibited by different PPEs: (a) E1: ethanol for 30 min, E2: ethanol for 2 h, EA: ethanol-acid; (b) M: methanol and MA: methanol-acid; (c) A: acetone and W: water) against several microorganisms. Values are the averages of three determinations; error bars represent standard deviations

3.3 Organic Acids

The organic acid contents of PPEs determined by HPLC are presented in Table II. MA extract had the highest malic acid (3.19%) content whereas the highest citric acid level (1.13%) was detected with EA extract (p<0.05) (Table II). Organic acids could affect integrity of the cell membrane, activities of enzymes or biosynthesis of macromolecules and cellular homeostasis (28, 29).

Table II

The Organic Acids, Total Sugar Contents and pH Levels of Pomegranate Peel Extracts. Data are given as mean values ± standard deviations (n=3)

Extracts pH Malic acid, % Citric acid, % Total sugar, %
E1 3.10 ± 0.05 0.01 ± 0.00 0.44 ± 0.03 3.72 ± 0.24
E2 3.10 ± 0.04 0.03 ± 0.01 0.62 ± 0.07 4.98 ± 0.21
EA 0.30 ± 0.02 1.59 ± 0.12 1.13 ± 0.14 4.93 ± 0.14
M 3.40 ± 0.04 0.00 ± 0.00 0.69 ± 0.03 4.76 ± 0.29
MA 0.26 ± 0.02 3.19 ± 0.14 0.97 ± 0.04 5.95 ± 0.07
A 3.50 ± 0.05 0.37 ± 0.04 0.65 ± 0.13 4.00 ± 0.13
W 3.55 ± 0.07 0.04 ± 0.01 0.10 ± 0.01 1.69 ± 0.25

3.4 pH Values

The lowest pH level (0.26) was measured with MA extract while the highest pH (3.55) value was determined with W extract as expected (Table II). The highest inhibition zones for all tested microorganisms were determined with MA and EA extracts with the low level of pH (almost zero) that might also affect microbial growth.

3.5 Antimicrobial Activities of Pomegranate Peel Extracts

The antimicrobial effects of different extracts obtained by using different solvents were evaluated against food associated microorganisms. The antimicrobial activities were assessed by the presence or absence of inhibition zones and zone diameters. The results are given in Figure 2. The data of the study showed that MA and EA extracts of pomegranate peels had the highest antibacterial activities against all tested microorganisms (p<0.05) (Figure 2(b)). The inhibition zone diameters were found to be 17–36 mm with MA extract (including the diameter of the wells). EA extract, the second most efficient extract, resulted in 17–32 mm inhibition zones (Figure 2(a)). The extracts E1, E2, M and A showed similar antimicrobial effects (Figure 2). Increasing extraction time from 30 min to 120 min for E2 extract did not enhance (p>0.05) antimicrobial efficacies almost in most cases. The lowest inhibitions for all microorganisms were detected with W extract in the range of 0–15 mm (p<0.05) (Figure 2(a)).

In general, the antimicrobial effects of extracts could be attributed to their phenolics (30) and organic acid contents (31, 32). Therefore, according to results obtained in this work, the highest levels of organic acids (MA and EA) and phenolics (EA) could contribute antimicrobial activities of these extracts.

In previous works, Gram positive bacteria were more sensitive to plant extracts than Gram negative ones (33, 34) consistent with the results obtained from this study. It was found that B. subtilis, B. cereus, E. faecalis and S. uberis (Gram positive) strains were more sensitive than E. coli and E. aerogenes (Gram negative) strains (Figure 2). The cell walls of Gram positive bacteria were shown as more sensitive to antimicrobial compounds compared with Gram negative bacteria (35, 36) due to the lipopolysaccharide layer and periplasmic space present in Gram negative bacterial cell walls. However, Hama et al. (37) found that pomegranate juice had antibacterial activity on both Gram positive (S. aureus) and Gram negative bacteria including E. coli and P. aeruginosa. The multi-layered peptidoglycan was shown as the main factor for antimicrobial resistance (37). According to results obtained in this work, the antibacterial activities of extracts were similar for P. aeruginosa (Gram negative) and S. uberis (Gram positive) strains. The reason for this is not known, but might be related with some specific properties of these microorganisms or extraction methods. Therefore, no clear correlation was found between the cell wall structures and the antibacterial activities of the extracts. Previously, methanol extracts of peel showed the greatest activities on different bacteria depending on the pomegranate variety tested (38, 39). It was indicated that ethanol extracts of pomegranate had hydrolysable tannins including punicalagins, ellagic acid and gallic acid (30). In this work, punicalagins and ellagic acids were found in all extracts but gallic acid was not determined. That may be linked to the variety of the pomegranate or extraction techniques.

In the present study, the inhibition zones for C. albicans were between 8–25 mm in diameter. The highest inhibition zone was obtained with MA extract (25 mm). It was reported that the methanolic PPEs inhibited C. albicans with the inhibition zones of 6–6.5 mm (12) which were much lower than found in this study. Punicalagins were shown as antifungal components of ethanol extract of pomegranate peels. C. albicans treated with punicalagins extracted from pomegranate peels exhibited morphological alterations in cell structure and abnormal budding (40). The aqueous extract of pomegranate peels also showed inhibitory activity on C. albicans (41) which was consistent with the results obtained with this study.

4. Conclusion

In the present work, PPEs were prepared from Turkish Hicaz pomegranate variety by using ethanol, methanol or their combinations with acid, acetone and water. All extracts were found to have antimicrobial effects on different bacteria and a fungus. Amongst the evaluated extracts, MA and EA exhibited the largest inhibition zones for all tested microorganisms. It was shown that high amounts of organic acids (for MA and EA) and phenolics (for EA) could be responsible for the antibacterial activities. Further studies are required to isolate other potential bioactive compounds of the PPEs and to identify their molecular mechanisms of action. In addition, potential PPEs from different varieties of pomegranate should also be investigated to obtain the most valuable bioactive compounds that could be used as safe food preservatives in the food industry.

Acknowledgements

We would like to thank Gebze Technical University, Turkey (2018-A101-04). The authors would like to thank Aise Unlu for technical support during extraction processes. Both authors Merve Balaban and Cansel Koç contributed equally to this manuscript.

Conflict of Interest

On behalf of all authors, the corresponding author states that there is no conflict of interest.

The Authors


Merve Balaban received her MSc from the Department of Molecular Biology and Genetics at Gebze Technical University, Turkey, under the supervision of Professor Meltem Yesilcimen Akbas. During her master thesis she worked on extraction strategies to recover bioactive compounds from fruit processing wastes and identify their antimicrobial and antibiofilm effects on microorganisms.


Cansel Koç received her MSc from the Department of Molecular Biology and Genetics at Gebze Technical University under the supervision of Professor Meltem Yesilcimen Akbas. During her Master’s thesis she worked on bioactive compounds and antimicrobial and antibiofilm potential for polyphenol-rich fruit processing waste extracts on food related pathogenic bacteria.


Taner Sar is a Postdoctoral Researcher at Högskolan i Borås, Sweden. He received his PhD at Gebze Technical University in the group of Professor Akbas. His current research interests are recovery of nutrients from food processing wastes, production of protein-rich microbial biomass and bioactive compounds as antimicrobial and antibiofilm agents. His research also focuses on enhancement of bioethanol production from industrial wastes by using Vitreoscilla haemoglobin gene.


Meltem Yesilcimen Akbas is currently working as a Professor of Molecular Biology and Genetics at Gebze Technical University. Her research interests span many aspects of industrial microbiology and microbial biotechnology including engineering of bacteria using bacterial haemoglobin to improve growth and productivity and using food processing waste extracts for antimicrobial and antibiofilm agents.

By |2021-12-23T15:20:20+00:00December 23rd, 2021|Weld Engineering Services|Comments Off on Screening for Bioactive Compound Rich Pomegranate Peel Extracts and Their Antimicrobial Activities

Photoelectrochemical Hydrogen Evolution Using Dye-Sensitised Nickel Oxide

Johnson Matthey Technol. Rev., 2022, 66, (1), 21

1. Introduction

The global effort to produce solar fuels by means of molecular photocatalysis continues to intensify following the establishment of basic design principles in the 1970s and 1980s (15). Many of the challenges encountered at the time remain relevant today, namely molecular systems for photocatalytic water oxidation or reduction often rely on a sacrificial electron source to drive the thermodynamically demanding multielectron reaction, most of which are not environmentally benign or renewable (6). However, a direct photocatalytic system would avoid the fabrication and systems costs required with photovoltaics coupled to electrolysis. Tremendous effort has been expended in an attempt to understand photocatalytic processes in solution either as a bimolecular process for homogeneous catalysis or on a semiconductor surface in a heterogeneous system (711). Over the years a vast catalogue of new molecular catalysts and sensitisers has been generated, a prototypic example being the well-known ruthenium water oxidation catalyst reported by Meyer et al., the “blue dimer” (12). Recent efforts have produced catalysts based on earth abundant metals such as iron and cobalt which typically underperform compared to prior systems, leaving the economic and environmental considerations for moving away from precious metal systems (platinum, palladium, rhodium or ruthenium) under some debate (1315).

Sensitisers based on the thoroughly understood ruthenium(II) trisbipyridyl complex remain popular as a starting point for new avenues of research (1619). More recent efforts have focused on covalently linking the catalyst and sensitiser to optimise charge separation (20). The fundamental principle of photocatalyst design where donor and acceptor are joined by a suitable covalent bridge is elegant and inspired by the photosynthetic reaction centre of green plants, but challenging to optimise in a working photochemical reactor, even where the molecular systems are relatively simple (21, 22). To date, practical implementations of molecular photocatalytic systems are scarce, despite the variety of systems proposed. Surface and solvent parameters introduce a large set of variables for optimising a photocatalytic reactor. At this point there are now an abundance of molecules and materials but developing a mechanistic understanding of such systems to aid design is still an ongoing process (23).

Over the past decade, research into dye-sensitised solar cells (DSSCs) has converged with heterogeneous photocatalysis (1, 2427). The potential advantages include high atom efficiency for the catalyst, low cost assembly through solution-based processing, and devices that operate under ambient conditions. Dye-sensitised photocathodes have been constructed in photoelectrochemical devices to reduce protons to hydrogen, usually under a small applied bias for a half-cell in a photocatalytic system (2831). These can be coupled to photoanodes which provide the electrons for proton reduction as a byproduct of water oxidation in a tandem device (31). The tandem system, where both anode and cathode are decorated with photocatalysts, removes the need for sacrificial reagents and enables a sustainable system (32). These dye-sensitised photoelectrochemical cells overcome many of the disadvantages of molecular systems in solution, while taking advantage of the catalogue of sensitisers and catalysts already available. Light absorption, charge transport and catalysis are separated between three tuneable components (3335). Attention then turns to the interfaces between these components, for example, how photocatalysts attach and behave on the semiconductor surface, which requires considerable optimisation.

In this contribution we focus on optimising the proton reduction half reaction, generating hydrogen by means of new integrated photocatalysts adsorbed onto the surface of a transparent p-type semiconductor, nickel(II) oxide. A proof-of-concept for this approach was reported by us recently for two supramolecular photocatalysts based on a bipyridyl ruthenium photosensitiser coupled to either a platinum or palladium catalytic centre via a terpyridine or triazole bridging ligand (36). In this follow up paper, we explore a series of new photocatalysts with structural modifications made to the bridge and the catalytic centre, and evaluate the impact these have on the photoelectrocatalytic reduction of protons (Figure 1). Consideration is given as to how the photocatalysts bind to the electrode surface and interact with the surrounding environment. Device testing in a photoelectrochemical cell is used to determine photocurrent and hydrogen produced as a result, and stability is evaluated over prolonged periods of illumination. The photophysical and electrochemical properties of the photocatalysts are examined to develop a mechanistic understanding of the system.

Fig. 1.

The integrated photocatalysts PC1–PC5 used in the present study

The integrated photocatalysts PC1–PC5 used in the present study

2. Results

2.1 Optical Properties

The preparation and characterisation of mesoporous nickel oxide cathodes has been described previously (37). Adsorption of the photocatalysts onto the mesoporous nickel oxide films on NSG TECTM 15 conductive glass from acetonitrile solutions was recorded by ultraviolet-visible (UV-vis) spectroscopy. Normally in titania-based systems the ester group is hydrolysed prior to adsorption or the titania is treated with base to promote binding (38), but for nickel oxide we have found that these ester-functionalised systems bind as well as the carboxylic acid derivatives. To calculate the dye loading, we assumed that the molar absorption of the dyes did not change significantly on the nickel oxide surface compared to the dye in solution. In dry acetonitrile, all five dyes produce steady-state absorption spectra with characteristic metal to ligand charge transfer (MLCT) bands from ruthenium to the diethyl ester bipyridyl ligands (39). When immobilised on nickel oxide films, the overall trend is towards a broader, red-shifted spectrum. While we do not have a model regarding what causes this spectral shift, it indicates that the dye interacts with the nickel oxide surface through the ester anchoring groups. This spectral broadening is typical for dyes adsorbed on metal oxide surfaces, and is usually observed when carboxylic acid anchoring groups are used and it is possibly caused by deprotonation of the acid on binding (40, 41). In this case, where ester anchoring groups have been used it could be due to hydrolysis or, possibly, the result of overlap from several different orientations of the catalyst on the nickel oxide surface, including some aggregates (42). The steady state absorption spectra are shown in Figure 2 and the data are summarised in Table I.

Fig. 2.

UV-vis absorption spectra of PC1–PC5: (a) in acetonitrile solution; (b) adsorbed on nickel oxide. Solution spectra contained micromolar concentration of dye

UV-vis absorption spectra of PC1–PC5: (a) in acetonitrile solution; (b) adsorbed on nickel oxide. Solution spectra contained micromolar concentration of dye

Table I

Steady-State UV-Visible Absorption Data for the Photocatalysts

Catalyst (solution), nm (film), nm ɛ, M–1 cm–1 at (MeCN) Dye loading, nmol cm–2
PC1 480 510 28,800 5.9
PC2 498 520 27,600 7.0
PC3 480 520 42,500 2.9
PC4 527 530 42,000 6.2
PC5 467 470 30,500 6.2

2.2 Transient Absorption Spectroscopy

Transient absorption spectroscopy was used to probe the mechanism of electron transfer following excitation with visible light. In dye-sensitised photoelectrocatalytic devices, unlike many homogeneous photocatalytic systems which rely on long-lived excited states, the dye injects charge to the semiconductor rapidly upon excitation and subsequently returns to the ground state by transferring charge to the catalyst. Providing that these processes are more rapid, dye degradation is avoided, and the device is both efficient, as recombination is reduced, and leads to stability within the system.

The transient absorption spectra obtained following pulsed photolysis (λexc = 470 nm) of PC5 in acetonitrile solution and PC5 adsorbed on nickel oxide are shown in Figure 3. A ground state bleach occurs within the pulse following excitation together with a broad, weak absorption extending from 500 nm to 700 nm, and a strong absorption together with a sharp transient absorption band at ca. 395 nm. These features do not decrease in intensity during the 3 ns window of the experiment, which is consistent with the 3MLCT states formed on excitation of a ruthenium diimine chromophore. When the dye was adsorbed on nickel oxide, transient absorption bands were also formed within the time resolution of the experiment, however, the spectral features were broadened, and the signal was more intense in the red region of the spectrum compared to the blue. Based on our previous work, the spectral shape is consistent with the formation of a charge-separated state (36). The transient absorption bands, with peak maxima at ca. 395 nm and 580 nm, and the ground state bleach, decayed on a similar timescale (τ = ca. 250 ps) and the ground state was recovered in ca. 1 ns. The results of the transient absorption spectroscopy are consistent with the rapid transfer of an electron from the valence band of nickel oxide to the photocatalyst, rather than stepwise excitation followed by charge-transfer. Possibly, the MLCT states on the diethyl [2,2’-bipyridine]‐4,4’‐dicarboxylate are destabilised on binding, promoting charge-transfer towards the bridging ligand and the catalytic centre. Recombination between the reduced photocatalysts and the hole remaining in nickel oxide occurs rapidly.

Fig. 3.

(a) Transient absorption spectra of PC5 in acetonitrile solution (black) and adsorbed on nickel oxide (red) 5 ps after excitation at 470 nm; (b) decay of the transient absorption and ground state bleach after excitation at 470 nm

(a) Transient absorption spectra of PC5 in acetonitrile solution (black) and adsorbed on nickel oxide (red) 5 ps after excitation at 470 nm; (b) decay of the transient absorption and ground state bleach after excitation at 470 nm

This fast recombination is likely to be the major limitation to the performance of the photoelectrocatalytic devices (28). However, previous studies on nickel oxide from the groups of Hammarström and Papanikolas have highlighted how the bias applied to the film affects the recombination kinetics (43, 44). Under the range of potentials studied here, we would expect recombination to be slowed down by several orders of magnitude compared to the lifetime determined from the spectroscopic measurements performed on dry films.

2.3 Photoelectrocatalysis

The photocathodes were tested in a three-electrode setup with a platinised fluorine doped tin oxide (FTO) counter electrode and a silver/silver chloride reference electrode. The pH of the aqueous electrolyte and composition of the buffer was varied, and different applied potentials (Eappl) were tested to find the optimum reaction condition for each photocatalyst. The electrolyte solutions used were: pH 3 potassium hydrogen phthalate buffer (0.1 M), pH 5 acetate buffer (0.2 M) or (2-morpholino)ethanesulfonic acid buffer (0.1 M), pH 7 potassium phosphate buffer (0.1 M). The range of Eappl was chosen to be less than the conduction band edge of titania (VCB in V vs. SCE = –0.40 – 0.06 × pH) (45) to mimic the conditions in a tandem device. Within this range, applied potentials were chosen where the photocurrents were maximised and were most stable, whilst avoiding significant changes to the background current.

Photocurrent was generated under 1 sun, AM 1.5 illumination, initially with chopped light (30 s intervals) followed by uninterrupted illumination. Photocurrent values were evaluated against dark current obtained after a period of equilibration in a sealed dark box. Control experiments confirmed that a system comprising two platinum-FTO electrodes acted as a simple electrolyser under an applied voltage of –0.3 V vs. Ag/AgCl in pH 3 phthalate buffer solution. A second control experiment comprised a system of a nickel oxide working electrode lacking a sensitiser with a platinum-FTO counter electrode. Both systems generated stable current but were not sensitive to incident light, thus we can exclude the possibility of direct (> band gap) excitation of nickel oxide leading to photocurrent or hydrogen evolution.

Figure 4 displays the photocurrents generated under equivalent conditions (pH 3–7, Eappl = –0.2 V vs. Ag/AgCl) for the full series of photocatalysts, a representative example of the many datasets. Longer experiments demonstrating the stability of the current over 3600 s are provided in Figure S2 in the Supplementary Information accompanying the online version of this article. All photocatalysts produced current under chopped light, as expected. A characteristic of all the chronoamperometry experiments was an initial spike of current due to either an accumulation of charge on the electrode surface or the consumption of oxygen within the pores. This emphasises the need for an equilibration period at the beginning of each experiment to obtain a true baseline value for light and dark currents. It also indicates that there may be a mass transport limitation within the system. Typical photocurrent densities for these small-scale devices (active nickel oxide area 0.79 cm–2) are in the μA cm–2 region. Notably, all samples were stable under chopped light illumination over the initial testing period of approximately 10 min. After chopped light illumination the experiment was continued under steady illumination for 60 min.

Fig. 4.

Chronoamperometry measurements of all sensitised nickel oxide photocathodes at: (a) pH 3; (b) pH 5; and (c) pH 7 at Eappl = –0.2 V vs. Ag/AgCl. The first 700 s are shown with ten 30 s on/off cycles of illumination recorded. The full experiment was 60 min

Chronoamperometry measurements of all sensitised nickel oxide photocathodes at: (a) pH 3; (b) pH 5; and (c) pH 7 at Eappl = –0.2 V vs. Ag/AgCl. The first 700 s are shown with ten 30 s on/off cycles of illumination recorded. The full experiment was 60 min

In some cases, characteristic spikes in the photocurrent transients were observed. For example, PC4 at pH 3 shows charging and discharging at the electrode-electrolyte interface under light on-off cycles. This may indicate that electrons are not being transferred to the catalyst or protons efficiently. For PC1, spikes are present when the light is switched on, followed by stabilisation of the photocurrent. In this case, charge accumulation at the electrode-electrolyte interface may arise from trapped holes, slow kinetics of proton reduction, slow charge-extraction (high transport resistance), fast charge recombination between the electrons in the catalyst, and holes in the nickel oxide or poor diffusion in the pores of the semiconductor. The smooth shape of the photocurrent vs. time trace for PC5 at pH 3, however, is consistent with catalysis and the evolution of hydrogen. As the applied bias was increased to –0.4 V vs. Ag/AgCl, the spikes decreased (except for PC4) and smoother transients were observed (Figure S4 in the Supplementary Information). This is consistent with filling of trap states at the nickel oxide surface.

The choice of buffer had a surprising impact on the photocurrent density and stability. At pH 3 and pH 7 (phthalate and phosphate buffers respectively) all samples produced stable photocurrent during the prolonged period of illumination. At pH 5, where an acetate buffer was employed, there was a steady decay of photocurrent consistent with degradation or desorption of the photocatalyst. This is in contrast to studies by Massin et al. who found the opposite trend for their dye-sensitised photoelectrocatalytic system with an organic dye, which was found to be stable in acetate buffer but unstable with phosphate buffer (46). In order to address the problems with photocatalyst instability in pH 5 acetate buffer an alternative non coordinating buffer was employed, 2-(N-morpholino)ethanesulfonic acid (MES). Use of this buffer has been previously shown to improve stability of similar photocatalytic systems (47). An example of the comparison between electrolytes for PC5 is summarized in Figure S5 in the Supplementary Information. For each of the photocatalysts, we observed that employing the MES buffer improved photocurrent stability compared to acetate buffer. PC1 and PC5 gave consistent photocurrent density regardless of the pH. PC2 consistently gave relatively low photocurrent density compared to the others. PC3 gave the highest photocurrent density at pH 7 but a lower photocurrent density was recorded at pH 3. For PC4 very little photocurrent was observed at pH 3 and pH 5, but relatively high photocurrent density was recorded at pH 7. It is encouraging that the photocurrent density did not drop at higher pH, because this would be compatible with a tandem device.

For each photocatalyst, hydrogen was detected by sampling the headspace and analysing it by gas chromatography. Table S1 in Supplementary Information summarises the results. Despite the differences in photocurrent density with buffer and Eappl described above, the most hydrogen was detected with pH 7 buffer and these results are shown in Table II.

Table II

Results for the Photocatalysts at Eappl 0 V, –0.2 V vs. Ag/AgCl, with pH 7 Buffera

Catalyst Eappl, V Jphoto, μA cm–2 Jtotal, μA cm–2 [H2]exp, μmol [H2]the, μmol ηFar, % TON
PC1 0 0.03 0.65 0.14 0.00 7
–0.2 2.09 4.39 0.11 0.31 36 5
PC2 0 0.38 0.77 0.13 0.06 33
–0.2 2.00 4.11 0.13 0.29 43 32
PC3 0 2.71 3.03 0.13 0.40 32 12
–0.2 8.84 11.79 0.11 1.30 9 11
PC4 0 2.71 2.12 0.08 0.40 21 15
–0.2 6.00 6.4 0.13 0.88 14 23
PC5 0 3.03 3.41 0.13 0.45 29 24
–0.2 3.03 4.13 0.13 0.45 28 23

While attempts were made to keep the sampling consistent, there was considerable error in the measurements due to bubbles forming on the electrode surface and quantifying hydrogen by syringe (>7% deviation from the mean average). The amount of hydrogen detected may also vary due to differences in hydrogen solubility in different electrolytes (48, 49), or as a side product from the photocatalyst degrading.

2.4 X-Ray Photoelectron Spectroscopy

X-ray photoelectron spectroscopy (XPS) data was recorded for the photocatalyst films before application in a photoelectrocatalysis cell under illumination with pH 3 in phthalate buffer and an applied bias of –0.2 V vs. Ag/AgCl. The nickel 2p peak remained unchanged so this was used to normalise the spectra to give a rough comparison of dye-loading. Figures 5 and 6 show the palladium and platinum regions, where relevant, for PC1 to PC5. There was no shift in binding energy observed for platinum or palladium on the electrode surface under our conditions, suggesting that the photocatalyst remains intact. A slight change in relative intensity for some of the photocatalysts (PC1 and PC4) suggests that there may be some desorption of the photocatalyst. Figure S8 in Supplementary Information shows that additional bands are present in the binding energy region 275–300 eV. These are assigned to C 1s and K 2p, which probably arises from the buffer. Their presence on the electrode surface makes the analysis of the ruthenium 3d band difficult.

Fig. 5.

XPS data for the palladium 3d region. Red = pre-catalysis, blue = post catalysis. A = PC1, B = PC2, C = PC4

XPS data for the palladium 3d region. Red = pre-catalysis, blue = post catalysis. A = PC1, B = PC2, C = PC4

Fig. 6.

XPS data for the platinum 4f region. Red = pre-catalysis, blue = post catalysis. A = PC3, B = PC5

XPS data for the platinum 4f region. Red = pre-catalysis, blue = post catalysis. A = PC3, B = PC5

3. Discussion

As with our previous studies with integrated photocatalysts based on a similar architecture, ester groups on the bipyridyl ligands serve as an anchoring site to nickel oxide (36). Our previous findings clearly suggested that there was sufficient interaction between the ester groups and the nickel oxide surface to provide a system resistant to dye desorption during photocatalysis (under suitable conditions). XPS results largely corroborate these claims. The XPS results show that the buffer salts can assemble on the electrode surface, and it is possible that there is competition between organic salts and the photocatalyst, leading to some desorption. We continue to favour ester substituted photocatalysts due to the simplified synthesis and purification of the dye. However, the diethoxy ester bipyridyl ligand serves two functions, both as the anchoring group to the nickel oxide surface and as an electron withdrawing ligand which stabilises the MLCT excited states. Locating the electron density close to the nickel oxide surface could increase the rate of charge-recombination, so the best photocatalysts should promote charge-transfer to the catalyst centre via the bridging ligand (20).

All the photocatalysts in this study produced photocurrent and hydrogen under each varied condition. Some photocatalysts perform better at pH 3, whereas others performed better at pH 7. The performance with pH 5 acetate buffer was the most consistent between different catalysts, but was generally lower than the other two buffers. Changing to MES buffer improved the performance at pH 5. Different authors report contrasting results when changing the pH of the electrolyte for analogous. The type of buffer affects the performance in two ways. Lower pH should increase the rate of hydrogen formation from the catalyst (50), however, the effect of pH on the valence band edge of the nickel oxide is a shift to more positive potentials as the H+ concentration increases (51). Further transient absorption spectroscopy studies are necessary to probe the effect of pH on the dynamics. It is expected that charge transfer from the nickel oxide to the photocatalyst would be slower at higher pH due to the lower valence band edge and, therefore, smaller driving force (52). Charge-recombination should occur in the Marcus inverted region and would be expected to be slower at higher pH, and increase the charge-collection efficiency of the device. However, in most kinetic studies, charge-recombination at the photosensitiser/nickel oxide interface appears to follow Marcus normal behaviour, accelerating with increasing driving force, probably due to recombination with more energetic intra-bandgap defect states (53, 54).

While this study shows that there are a variety of ways to improve the performance of dye-sensitised photoelectrochemical devices, including tuning the structure of the catalyst or the environment, the performance of dye-sensitised photocathodes based on nickel oxide still lags behind equivalent photoanode devices based on titania. Further improvements are necessary, for example, improving the porosity of the electrodes to facilitate mass transport. Additionally, bubble formation on the electrode surface leads to a drop in the photocurrent and good diffusion is necessary to prevent a build-up of OH in the pores. At the same time, high surface area must be maintained to adsorb enough photocatalyst to absorb all the incident light. A limitation of the ruthenium bipyridyl chromophores is the low absorption coefficient (ɛ = 27,600–42,500 M–1 cm–1 for PC1–PC5). Organic photosensitisers have two to three times larger absorption coefficients, enabling thinner or more porous films to be used (33, 55, 56). Future considerations for dye-sensitised photoelectrochemical assemblies should also consider the prospect of engineering the thermodynamic driving force for charge recombination towards the Marcus inverted region (similar to titania-based systems). Ongoing work within our laboratory looks to find an alternative semiconductor to nickel oxide with a more typical band structure to address this (32, 57).

4. Conclusion

The present study describes a series of novel sensitiser-catalyst dyads that were tested in a photoelectrocatalytic half-cell set-up to determine the optimum conditions for water splitting. At a range of pH levels the dyads remained intact with a stable photocurrent, demonstrating their robustness. However, when using a non-coordinating buffer we saw an increase in photocurrent. All our systems produced hydrogen under a small applied bias. Under optimal conditions, Faradaic efficiencies up to 90% with turnover numbers of up to 33 in an hour were achieved, which are comparative to our previously reported systems. Transient absorption measurements confirmed that charge separation on the surface of a p-type semiconductor, nickel oxide, is very efficient when compared to the same system in dilute solution. While rapid charge injection facilitates reduction of the catalyst, thus aiding photocatalysis, recombination of the oxidised sensitiser with nickel oxide remains equally efficient. The insight from transient absorption data in particular highlights a major challenge for integrated molecular photocatalysts on a semiconductor interface and further work will seek to address this.

Acknowledgements

We thank the Leverhulme Trust for a project grant RGS108374, The North East Centre for Energy Materials EP/R021503/1; Science and Technology Facilities Council (STFC) for access to the Central Laser Facility (CLF) ULTRA facility for transient spectroscopy; NEXUS XPS facility for conducting the XPS measurements. Laura O’Reilly thanks the Irish Research Council for financial support and Martin Kaufmann gratefully acknowledges support by the Project “HYLANTIC” – EAPA_204/2016 which is co‐financed by the European Regional Development Fund in the framework of the Interreg Atlantic programme. Data supporting this publication is openly available under an ‘Open Data Commons Open Database License’. Additional metadata are available (58).

Supplementary Information

Download the Supplementary Information (PDF, 2.1 MB)

The Authors


Abigail Seddon is currently a PhD student in the Energy Materials Group at School of Natural and Environmental Sciences, Newcastle University, UK, working on applications of polyoxometalates. Previously, she graduated from Newcastle University with an MChem in Chemistry with an Industrial Placement year at AstraZeneca. Her research interests include artificial photosynthesis, photovoltaics and inorganic synthesis.


Joshua Karlsson graduated from the University of York, UK, with a BSc in Chemistry and Imperial College London, UK, with an MRes in Green Chemistry in 2013 and 2014 respectively, before undertaking a PhD at Newcastle University in 2015. His doctoral studies covered a wide range of topics on the molecular photophysics of organic dyes pertinent to solar cells and medical imaging. His expertise lies in photocatalysis and detailed interrogation of excited state properties for organic and inorganic chromophores using UV-vis absorption, fluorescence and time-resolved optical spectroscopy.


Libby Gibson joined Newcastle University as a Lecturer in Physical Chemistry in 2014 and was promoted to Reader in Energy Materials in 2018. Prior to her current role, she held a University of Nottingham Anne McLaren Research Fellowship and a Royal Society Dorothy Hodgkin Research Fellowship. She obtained her PhD in 2007 from the University of York, supervised by Robin Perutz FRS and Anne-Kathrin Duhme-Klair. Research in her group focuses on solar cell and solar fuel devices that function at a molecular level and challenge the conventional solid-state photovoltaic technologies. Her current European Research Council (ERC)-funded project focuses on developing transparent p-type semiconductors for tandem solar cells and artificial photosynthesis.


Laura O’Reilly graduated from Dublin City University, with a BSc in Chemistry and Pharmaceutical Science in 2014, and subsequently undertook a PhD at Dublin City University. Her doctoral research focused on the design and synthesis of novel photocatalysts for hydrogen generation. During her PhD programme she used a range of spectroscopic techniques including UV-vis absorption, time-resolved UV-vis and time resolved infrared spectroscopy to probe the photophysical properties of the photocatalysts.

Martin Kaufmann is currently a MaREI postdoctoral researcher within the School of Chemical Sciences at Dublin City University. Prior to joining Mary Pryce’s research group in Dublin, Martin did his PhD in organic chemistry at the Friedrich Schiller University Jena in Germany. His research interests are the syntheses of heterocyclic functional dyes, transition metal complexes and their application in the photocatalytic hydrogen generation.

Han Vos is Emeritus Professor of Inorganic Chemistry at Dublin City University. His research interests are in the design of supramolecular systems containing transition metal complexes. Of particular interest are the synthesis, photophysical and electrochemical properties of dinuclear and polymeric ruthenium and osmium polypyridyl complexes both in solution and when immobilised on solid substrates, and their application in energy sources.


Mary Pryce joined Dublin City University, Ireland, in 1997 as a Lecturer in Inorganic Chemistry. Prior to joining the School of Chemical Sciences, she was employed as a postdoctoral Fellow at the University of Milan, Italy. In 1995, she obtained her PhD from Dublin City University in the area of organometallic photochemistry. Current research projects within the group focus on designing new materials (polymers, organometallic compounds or organic dyes) for energy applications such as hydrogen generation, or CO2 conversion. Another aspect of research focuses on antimicrobial materials. Central to both of these research areas is understanding the photophysical properties using time resolved techniques.

By |2021-12-23T09:53:02+00:00December 23rd, 2021|Weld Engineering Services|Comments Off on Photoelectrochemical Hydrogen Evolution Using Dye-Sensitised Nickel Oxide
Go to Top