id	author	title	date	pages	extension	mime	words	sentence	flesch	summary	cache	txt
cet-14450		cet-14450		6	.pdf	application/pdf	3568	123	50	The operation of the gasifier was rather unstable in the last setpoint, which was observed as very large variation in bed temperatures and bed pressure drops. 1/3S+2/3D 0.25 1.67 0 0 3.0 3.5 882 895 2.6 2.9 46.7 S 0.25 0.91 0 0.6 4.2 2.0 740 825 1.3 2.3 41.6 S 0.5 0.61 0 0.89 4.2 1.7 704 826 1.0 2.2 38.1 S 0.5 0.41 0 1.29 4.2 1.7 706 863 0.93 2.2 37.2 - 0 0.29 0 1.34 4.2 1.7 661 859 0.86 2.2 37.2 Dry gas composition, vol% CO CO2 H2 N2 (as difference) CH4 C2Hy C3-C5Hy H2O in wet gas, vol% 16.3 22.6 27.5 28.4 4.19 1.01 0 32.2 12.2 20.3 18.3 42.2 4.46 1.53 0.02 27.9 13.0 20.0 16.8 44.3 4.46 1.45 0.02 29.3 14.0 19.1 18.6 43.3 3.90 1.02 0 31.9 13.7 18.8 18.7 44.0 3.78 0.98 0 31.6 Tars + benzene, g/m3 STP 10.5 14.9 14.3 9.3 9.3 Filter temperature, °C Dust content in filter inlet, g/m3 STP Filter pressure drop, mbar Filter face velocity, cm/s 550 25 27 1.8 548 38 35 1.6 548 64 39 1.4 522 90 36 1.4 516 65 36 1.4 C-conversion to gas and tars, % 93.5 85.7 75.5 67.5 66.6 * S + P3: The mixture of sand and Myanit limestone, ** STP: at 273.15 K and 101,325 kPa Figure 4: Carbon conversions in BCFB gasification tests.	cache/cet-14450.pdf	txt/cet-14450.txt