Gunther Kolb

ORCID: 0000-0003-2392-1278
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About
Contact & Profiles
Research Areas
  • Catalytic Processes in Materials Science
  • Catalysts for Methane Reforming
  • Catalysis and Oxidation Reactions
  • Catalysis and Hydrodesulfurization Studies
  • Electrocatalysts for Energy Conversion
  • Innovative Microfluidic and Catalytic Techniques Innovation
  • Fuel Cells and Related Materials
  • Hybrid Renewable Energy Systems
  • Biodiesel Production and Applications
  • Advancements in Solid Oxide Fuel Cells
  • Ammonia Synthesis and Nitrogen Reduction
  • Industrial Gas Emission Control
  • Heat Transfer and Optimization
  • Iron and Steelmaking Processes
  • Heat Transfer and Boiling Studies
  • Zeolite Catalysis and Synthesis
  • Injection Molding Process and Properties
  • Additive Manufacturing and 3D Printing Technologies
  • Process Optimization and Integration
  • Electric Vehicles and Infrastructure
  • Carbon dioxide utilization in catalysis
  • Thermochemical Biomass Conversion Processes
  • Microfluidic and Capillary Electrophoresis Applications
  • Heat and Mass Transfer in Porous Media
  • Electrohydrodynamics and Fluid Dynamics

Fraunhofer Institute for Microengineering and Microsystems
2016-2025

Carl Zeiss (Germany)
2016-2025

Fraunhofer Institute for Chemical Technology
2014-2023

Eindhoven University of Technology
2010-2020

Synthetic Biologics (United States)
2014-2016

Boreskov Institute of Catalysis
2016

University of Warwick
2016

John Wiley & Sons (Germany)
2015

Netzsch (Germany)
2009

Voestalpine (Austria)
2002

10.1016/j.cej.2003.10.005 article EN Chemical Engineering Journal 2004-01-22

A simulation model of biomass gasification for syngas production with steam as gasifying agent and subsequent adjustment has been developed using Aspen Plus. The is based on Gibbs free energy minimization applying the restricted equilibrium method. objective to study effect important parameters such temperature, ratio shift reaction temperature hydrogen concentration, CO conversion, CO2 conversion H2/CO in syngas. Simulations were performed different feedstocks predict their composition....

10.1016/j.renene.2016.08.069 article EN cc-by Renewable Energy 2016-11-10

10.1016/j.cep.2012.10.015 article EN Chemical Engineering and Processing - Process Intensification 2012-12-05

The MAPSYN project of the European Union (standing for Microwave, Acoustic and Plasma SYNtheses) aims at utilization plasma technology nitrogen fixation reactions on an industrial scale with reactor technology, developed utilised commercially [1]. Key motif is enhanced energy efficiency to make process viable chemical industry. corresponding enabling technologies – catalysis, smart reactors (microreactors) more go beyond prior approaches. Continuing a first project-based literature...

10.1016/j.cattod.2013.04.005 article EN cc-by-nc-nd Catalysis Today 2013-06-03

In this work, several kinetic models have been studied for the methanol dehydration to dimethyl ether (DME), applying a commercial ZSM-5 catalyst rather than state-of-the-art alumina. The tests were carried out in fixed-bed external-recycle reactor, absence of temperature and concentration gradients. Kinetic parameters different calculated evaluated against physicochemical constraints guidelines on entropy values. After discrimination, it was concluded that modification model previously...

10.1016/j.cej.2018.04.160 article EN cc-by-nc-nd Chemical Engineering Journal 2018-04-25

Ammonia has attracted much interest as a potential green and renewable hydrogen carrier or energy vector. Compared to hydrogen, ammonia offers several advantages. For example, significantly higher density can be liquefied at room temperature moderate pressure of 8 bars. While cracked supply it is also possible convert directly into high-temperature solid oxide fuel cells (SOFCs) generate electricity. The Ship-FC project aims install an ammonia-fed 2MW SOFC system on board the vessel Viking...

10.3390/catal15030196 article EN Catalysts 2025-02-20
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