Kevin J. Hughes
Current Organizations / Institutes
The organizations/institutes from the scholar's latest article
Kevin J. Hughes has a total of 75 co-authors. Here are the top co-authors by number of shared publications:
Mohamed Pourkashanian
22 shared publications- Mohammed S. Ismail
School of Engineering, University of Hull, Hull HU6 7RX, UK
13 shared publications Derek B. Ingham
11 shared publicationsLin Ma
11 shared publications- Derek B. Ingham
University of Leeds
10 shared publications - Lin Ma
Energy Institute, The University of Sheffield, Sheffield S3 7RD, UK
8 shared publications
Latest Publications
- 23 September 2026
- Published by Elsevier in Energy Conversion and Management
- Vol. 370
Enhancing the efficiency of an amine-based CO2 capture plant using an interheated stripper modification
- 23 September 2026
- Published by Elsevier in Energy Conversion and Management
- Vol. 370
Enhancing the efficiency of an amine-based CO2 capture plant using an interheated stripper modification
- Open Access
- 10 July 2026
- Published by Elsevier in Carbon Capture Science & Technology
- Vol. 20
Performance Campaign of a Chemical Absorption Pilot Plant Treating High CO2 Content Industrial Process Emissions
- 10 July 2026
- Published by Elsevier in Carbon Capture Science & Technology
- Vol. 20
Open AccessPerformance Campaign of a Chemical Absorption Pilot Plant Treating High CO2 Content Industrial Process Emissions
- Open Access
- 4 June 2026
- Published by Elsevier in SSRN Electronic Journal
Performance Campaign of a Chemical Absorption Pilot Plant Treating High CO2 Content Industrial Process Emissions
Decarbonisation of critical hard-to-abate industrial sectors such as the iron and steel industry is crucial for meeting climate targets, with chemical absorption carbon capture identified as a key transitional technology. However, its application is hindered by a significant knowledge gap: the absence of publicly available and transparent performance benchmarks using conventional capture systems under elevated CO2 conditions that are representative of industrial process emissions. An experimental performance campaign was conducted on the chemical absorption pilot plant at the Energy Innovation Centre (EIC) in Sheffield, UK. The study established a novel performance baseline across a wide operating envelope for flue gas concentrations ranging from 10 to 25 mol.% CO2, achieving 90% capture efficiency using a 35 wt.% monoethanolamine (MEA) solvent. In addition, a methodology was developed to quantify solvent regeneration energy and its constituent components, complementing a system energy balance for each capture condition. The results provided experimentally validated insight into the relationship between operating conditions, capture performance, and energy demand at elevated CO2 concentrations. The dataset established a robust baseline for conventional packed-bed systems and improved understanding of regeneration energy contributions under industrially relevant conditions. These findings are scalable for application to the design, operation and optimisation of chemical absorption systems in heavy industries and provide a reliable benchmark for future work on advanced solvents, process intensification and scale-up to commercial deployment.
- 4 June 2026
- Published by Elsevier in SSRN Electronic Journal
Open AccessPerformance Campaign of a Chemical Absorption Pilot Plant Treating High CO2 Content Industrial Process Emissions
Decarbonisation of critical hard-to-abate industrial sectors such as the iron and steel industry is crucial for meeting climate targets, with chemical absorption carbon capture identified as a key transitional technology. However, its application is hindered by a significant knowledge gap: the absence of publicly available and transparent performance benchmarks using conventional capture systems under elevated CO2 conditions that are representative of industrial process emissions. An experimental performance campaign was conducted on the chemical absorption pilot plant at the Energy Innovation Centre (EIC) in Sheffield, UK. The study established a novel performance baseline across a wide operating envelope for flue gas concentrations ranging from 10 to 25 mol.% CO2, achieving 90% capture efficiency using a 35 wt.% monoethanolamine (MEA) solvent. In addition, a methodology was developed to quantify solvent regeneration energy and its constituent components, complementing a system energy balance for each capture condition. The results provided experimentally validated insight into the relationship between operating conditions, capture performance, and energy demand at elevated CO2 concentrations. The dataset established a robust baseline for conventional packed-bed systems and improved understanding of regeneration energy contributions under industrially relevant conditions. These findings are scalable for application to the design, operation and optimisation of chemical absorption systems in heavy industries and provide a reliable benchmark for future work on advanced solvents, process intensification and scale-up to commercial deployment.
- 27 March 2026
- Published by Elsevier in Chemical Engineering Research and Design
- Vol. 228, 714-726
Performance analysis of absorber intercooling for a CO2 capture plant integrated with the natural gas combined cycle
- 27 March 2026
- Published by Elsevier in Chemical Engineering Research and Design
- Vol. 228, 714-726
Performance analysis of absorber intercooling for a CO2 capture plant integrated with the natural gas combined cycle
- Open Access
- 17 December 2024
- Published by Elsevier in Energy Conversion and Management: X
- Vol. 25
A techno-economic and life cycle assessment of a new power and biomass to liquids (PBtL) configuration with negative emissions for producing sustainable aviation fuel (SAF)
- 17 December 2024
- Published by Elsevier in Energy Conversion and Management: X
- Vol. 25
Open AccessA techno-economic and life cycle assessment of a new power and biomass to liquids (PBtL) configuration with negative emissions for producing sustainable aviation fuel (SAF)
- Open Access
- 11 December 2024
- Published by Elsevier in International Journal of Hydrogen Energy
- Vol. 98, 576-589
Characterisation of double-sided graphene microporous layers for improved polymer electrolyte membrane fuel cell performance
- 11 December 2024
- Published by Elsevier in International Journal of Hydrogen Energy
- Vol. 98, 576-589
Open AccessCharacterisation of double-sided graphene microporous layers for improved polymer electrolyte membrane fuel cell performance
- Open Access
- 18 November 2024
- Published by Frontiers Media SA in Frontiers in Fuels
- Vol. 2, 1401691
A quantitative study of OH and NO concentration of a premixed laminar kerosene flame using a flat-flame burner at atmospheric pressure
In the context of global warming and the increasing demands for the application of sustainable fuels, measurements of a variety of experimental targets under a wide range of conditions are crucial to improving the fundamental understanding of real jet fuels and developing quality kinetic mechanisms for large hydrocarbons. Planar laser-induced fluorescence (PLIF) is an effective approach to investigate concentrations of important species of a given flame while quantifying the fluorescence image remains a great challenge with significant uncertainties. This investigation aims to improve the fundamental understanding of the oxidation of kerosene-based mixtures at two equivalence ratio conditions. Two gas fuels are utilized as the reference for the quantitative studies. For each flame condition, relative OH and NO quantities and temperature profiles were measured by applying the PLIF and coated fine wire type R Pt/Pt-Rh thermocouples, respectively. The converted OH and NO results were subsequently compared with the simulation by using ANSYS Chemkin Pro, and the results indicate that reliable temperature profiles are the key to accurately quantify the species concentration of a given flame.
- 18 November 2024
- Published by Frontiers Media SA in Frontiers in Fuels
- Vol. 2, 1401691
Open AccessA quantitative study of OH and NO concentration of a premixed laminar kerosene flame using a flat-flame burner at atmospheric pressure
In the context of global warming and the increasing demands for the application of sustainable fuels, measurements of a variety of experimental targets under a wide range of conditions are crucial to improving the fundamental understanding of real jet fuels and developing quality kinetic mechanisms for large hydrocarbons. Planar laser-induced fluorescence (PLIF) is an effective approach to investigate concentrations of important species of a given flame while quantifying the fluorescence image remains a great challenge with significant uncertainties. This investigation aims to improve the fundamental understanding of the oxidation of kerosene-based mixtures at two equivalence ratio conditions. Two gas fuels are utilized as the reference for the quantitative studies. For each flame condition, relative OH and NO quantities and temperature profiles were measured by applying the PLIF and coated fine wire type R Pt/Pt-Rh thermocouples, respectively. The converted OH and NO results were subsequently compared with the simulation by using ANSYS Chemkin Pro, and the results indicate that reliable temperature profiles are the key to accurately quantify the species concentration of a given flame.