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10
12
t/ / /
CO
C H O N S Cl 100 t/d 4.8 %W.B. 95.0 %W.B. 0.2 W.B. 49.0 %D.B. 6.7 %D.B. 44.1 %D.B. 0.0 %D.B. 0.0 %D.B. 0.0 %D.B. HHV 17.6 MJ/kg (W.B.) 4195 kcal/kg LHV 16.1 MJ/kg (W.B.) 3834 kcal/kg 973 K 1173 K ICFG H 2 CO CH 4 CO 2 N 2 HHV (W.B.) LHV (W.B.) CO 2 O 2 N 2 5637 m 3 N /h W.B. 4833 m 3 N /h D.B. 57.0 %D.B. 26.4 %D.B. 1.7 %D.B. 12.3 %D.B. 2.7 %D.B. 11.3 MJ/m 3 N 2691 kcal/m 3 N 10.1 MJ/m 3 N 2412 kcal/m 3 N 74.4 % (HHV basis) 73.0 % (LHV basis) 10040 m 3 N /h W.B. 9482 m 3 N /h D.B. 17.1 %D.B. 3.5 %D.B. 2.7 %D.B.
(a) Syn-Gas Scrubber Waste Heat Boiler Syn-gas Compresser CO Shift Reactor H 2 -PSA Unit [1] (c) Wood Biomass 100 t/d ICFG (b) Combustion Gas Waste Heat Boiler Steam Air Heater No.2 FDF No.1 FDF Economizer M. P. Steam Stack H 2 Compresser (a)(b)(c) CHG ( 20MPa ) 2740m 3 N/h Steam Turbine Steam [1] Off-gas Burner Bag Filter IDF G
L (mm) W (mm) H (mm) TA80 2700* 1150 2650
MAP
100t/ /40 /50 52 8/kg 202/ /40 /60 40 45/kg 151.5/ 90/kg 95/kg
kw
PFI RPS
IPP Proprietary Information of EBARA Corporation August 27, 2001
: 100t/d 36.7t/d : 42 10 : 2,400 / t- : 1.6 / 10 / / 16 : 3.0% : 3.0% : 1.0% 23 4# $& '(# )$& *+ )$& 5!6 # ))&,-./0./ # 1&!"# $%&
[ / t ]
kg