A5017145341- Process Optimization and Integration
- Advanced Control Systems Optimization
- Carbon Dioxide Capture Technologies
- Membrane Separation Technologies
- Thermodynamic and Exergetic Analyses of Power and Cooling Systems
- Catalysis and Oxidation Reactions
- Chemistry and Chemical Engineering
- Water-Energy-Food Nexus Studies
- Advanced Thermodynamics and Statistical Mechanics
- Catalysts for Methane Reforming
- Sustainable Industrial Ecology
- Phase Equilibria and Thermodynamics
- Hybrid Renewable Energy Systems
- Environmental Impact and Sustainability
- Zeolite Catalysis and Synthesis
- Catalytic Processes in Materials Science
- Advanced Multi-Objective Optimization Algorithms
- Integrated Energy Systems Optimization
- Climate Change Policy and Economics
- Reservoir Engineering and Simulation Methods
- Global Energy and Sustainability Research
- Membrane-based Ion Separation Techniques
- Membrane Separation and Gas Transport
- Solar Thermal and Photovoltaic Systems
- Methane Hydrates and Related Phenomena
Texas A&M University at Qatar
2015-2024
Texas A&M University
2011-2024
Mitchell Institute
2011-2024
University of British Columbia
2024
K.N.Toosi University of Technology
2024
American Society For Engineering Education
2024
Indian Institute of Technology Delhi
2017
Qatar Foundation
2016
Qatar Airways (Qatar)
2014
Centre for Research and Technology Hellas
2012
Global hydrogen production is dominated by the Steam-Methane Reforming (SMR) route, which associated with significant CO2 emissions and excess process heat. Two paths to lower specific in SMR are investigated: (1) integration of capture compression for subsequent sequestration or utilization, (2) electrolysis increased production. In both cases, heat utilized drive reduction options. Four different design regimes carbon identified. Techno-economic analyses performed study effect mitigation...
Efficient power generation from low to medium grade heat is an important challenge be addressed ensure a sustainable energy future. Organic Rankine Cycles (ORCs) constitute enabling technology and their research development has emerged as very active field over the past decade. Particular focus areas include working fluid selection cycle design achieve efficient conversions for diverse hot streams associated with geothermal, solar or waste sources. Recently, number of approaches have been...
This work presents a Computer-Aided Molecular Design (CAMD) method for the synthesis and selection of binary working fluid mixtures used in Organic Rankine Cycles (ORC). The consists two stages, initially seeking optimum mixture performance targets by designing molecules acting as first component binaries. identified are subsequently approached required matching selecting concentration. A multiobjective formulation CAMD-optimization problem enables identification numerous candidates,...
The water–energy nexus continues to gain traction around the world, because of inherent merits in simultaneously considering both resources. In this paper, a systematic procedure is developed for maximizing benefits interdependent relationship, when coupled with industrial processes exhibiting net surplus heat energy. presented methodology utilizes total site analysis first screen process power and water generation potential. addition streams, seawater desalination considered as an...
Abstract The limitations are addressed that emerge from the computer aided molecular design (CAMD) applications in optimal synthesis of solvents through a novel approach designing built upon multiple objective optimization technology. This technology has certain advantages over single approaches have been used for solvent molecules past. different drives, described by various functions, treated independently without being submitted to unnecessary fixed assumptions bias designs. As result,...
In the present paper, a semi-empirical kinetic model for catalytic reforming has been developed. developed model, component "lumping" strategy is based on paraffins, olefins, naphthalenes, and aromatics (PONA) analysis. "Activation energy lumps" are introduced to take into account different values of activation energies within specific reaction classes. The parameters have estimated by bench marking with industrial data. Simulation results found be in very close agreement plant One...