id	author	title	date	pages	extension	mime	words	sentence	flesch	summary	cache	txt
cet-13132		cet-13132		6	.pdf	application/pdf	3659	121	46	Considering the thermodynamic analysis results, using an off-gas stream from a biomethane 20 30 40 50 60 70 80 90 100 50 250 450 650 850 1050 C O 2 C o n v e rs io n ( % ) T (˚C) 0% CH4 1% CH4 5% CH4 10% CH4 20% CH4a) 1.E-06 1.E-05 1.E-04 1.E-03 1.E-02 1.E-01 1.E+00 1.E+01 50 250 450 650 850 1050 C H 4 ,o u t (k m o l/ h ) T (˚C) 0% CH4 1% CH4 5% CH4 10% CH4 20% CH4c) 1.5 2 2.5 3 3.5 4 4.5 5 5.5 650 750 850 950 1050 C O ,o u t (k m o l/ h ) T (˚C) 0% CH4 1% CH4 5% CH4 10% CH4 20% CH4 d) 0.6 0.7 0.8 0.9 1 1.1 1.2 1.3 1.4 1.5 700 800 900 1000 1100 H 2 /C O T (˚C) 0% CH4 1% CH4 5% CH4 10% CH4 20% CH4 b) 0 10 20 30 40 50 60 70 80 90 100 550 650 750 850 950 1050 C H 4 C o n v e rs io n ( % ) T (˚C) 1% CH4 5% CH4 10% CH4 20% CH4a) 0 1 2 3 4 5 6 7 50 250 450 650 850 1050 H 2 ,o u t (k m o l/ h ) T (˚C) 0% CH4 1% CH4 5% CH4 10% CH4 20% CH4 b) 323 plant (or a CO2 stream doped with CH4) could be a potential alternative for syngas production, once the possible simultaneous occurrence of the RWGS and the methane bi-reforming reactions allows higher CO2 conversions and the production of higher amounts of CO and H2, while consuming H2O, an unwanted RWGS by product, reducing the need of water condensation before syngas conversion. Alternatively, if a certain process is destined for methane production from CO2, the reaction must be carried out at lower temperatures and higher H2/CO2 ratios (e.g. 3) allowing higher CO2 conversions.	cache/cet-13132.pdf	txt/cet-13132.txt