<abstract xml:lang="en" xmlns="http://www.w3.org/1999/xhtml">The dependence of carbon formation, hydrogen yield and efficiency of the ethanol autothermal reforming process on critical process factors is studied in the work by using chemical equilibrium calculations with a process simulation model made in the ChemCAD environment. The studied process factors are carbon-to-steam ratio S/C, air-to-fuel ratio λ and temperature in the reactor TATR. Since the goal of the reforming process is to achieve possibly higher values of H2 concentration in the reforming gas, by operating reformer at the maximum efficiency at the same time, the optimization of the reforming process was done by using objective functions which include hydrogen yield and the amount of heat supplied to the process. As a result it was found that the maximum process efficiency, which is defined as the ratio of obtained hydrogen energy to the energy supplied to the process in the studied range of process factors is 0,61, and this value can be achieved at λ value of 0,1, S/C values of 2,5-3 and temperatures in the reactor TATR 680 - 695°C. Hydrogen yield under these conditions is 4,41-4,55 mol/molC2H5OH.</abstract>

The dependence of carbon formation, hydrogen yield and efficiency of the ethanol autothermal reforming process on critical process factors is studied in the work by using chemical equilibrium calculations with a process simulation model made in the ChemCAD environment. The studied process factors are carbon-to-steam ratio S/C, air-to-fuel ratio λ and temperature in the reactor TATR. Since the goal of the reforming process is to achieve possibly higher values of H2 concentration in the reforming gas, by operating reformer at the maximum efficiency at the same time, the optimization of the reforming process was done by using objective functions which include hydrogen yield and the amount of heat supplied to the process. As a result it was found that the maximum process efficiency, which is defined as the ratio of obtained hydrogen energy to the energy supplied to the process in the studied range of process factors is 0,61, and this value can be achieved at λ value of 0,1, S/C values of 2,5-3 and temperatures in the reactor TATR 680 - 695°C. Hydrogen yield under these conditions is 4,41-4,55 mol/molC2H5OH.

Optimization of Ethanol Autothermal Reforming Process with Chemical Equilibrium Calculations

Institute of Energy Systems and Enviroment, Riga Technical University, Kronvalda boulv. 1, LV-1010, Riga, Latvia

Environmental and Climate Technologies

The dependence of carbon formation, hydrogen yield and efficiency of the ethanol autothermal reforming process on critical process factors is studied in the...

Optimization of Ethanol Autothermal Reforming Process with Chemical Equilibrium Calculations

Data publikacji: 26 mar 2010

Zakres stron: 79 - 85

DOI: https://doi.org/10.2478/v10145-009-0011-x

Słowa kluczowe
autothermal reforming, chemical, ethanol, equilibrium, fuel cells, optimization

This content is open access.

Optimization of Ethanol Autothermal Reforming Process with Chemical Equilibrium Calculations

Data publikacji: 26 mar 2010

Zakres stron: 79 - 85

DOI: https://doi.org/10.2478/v10145-009-0011-x

Słowa kluczoweautothermal reforming, chemical, ethanol, equilibrium, fuel cells, optimization

This content is open access.

Słowa kluczowe
autothermal reforming, chemical, ethanol, equilibrium, fuel cells, optimization