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π SIMILAR VOLUMES
The simulation of a steam/CO 2 reformer is based upon detailed intrinsic kinetics of reforming, including those of carbon deposition and -gasification. The internal diffusion limitations are accounted fot through the modeling. The influence of the steam/methane and the CO 2 /methane ratio on the syn
Partial oxidation of methane to syngas with or ;;ft;,rr simultaneous CO2 and steam reformlng reactions over
03 Gaseous fuels (derived gaseous fuels) two superimposed tiers. In almost 8000 h of plant operation up to September 1995, the filter operated well. A permanent clean gas dust content of <3 mg/m"(STP) was obtained, compared with the design value of 5 mg/m'(STP). Using dry gas cleaning at increased t
Thermodynamics was applied to investigate propane dry reforming (DR) and steam reforming (SR). Equilibrium calculations employing the Gibbs free energy minimization were performed upon a wide range of pressure (1e5 atm), temperature (700e1100 K), carbon dioxide to propane ratio (CPR, 1e12) and water