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- えりか ひがき
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60 RHF (..14 ()
61 % 39% 2 CO 2 (RHF:Rotary Hearth Furnace) 1
62 1,2001,400 FASTMET 12 6 (-3) 1-1 T.Fe Fe2O3 FeO M.Fe ZnO PbO SiO2 Al2O3 CaO MgO Cl S C T.FeFe2O3, FeO, M.FeFe 5 (2005) I
63 1-1. 3
64
65 Zn,Pb
66 (95%) 0.1ng-TEQ/Nm 3 1ng-TEQ/Nm 3 95% 6
67 [] = (A)[]/(B)[] 100 (A)= (t) (%) (B)= (t) (%) (t) (%) RHF(t) RHF (%) (t) (t) (%) [] 7
68 (%) (%) [] = (C)[]/(D)[ ] 100 (C)= (t) (%) (D)= (t) (%) - (t) (%) - RHF(t) RHF (%) [] = [ ] (21 [(%)]) / (21-15) RHF 15% 8
69 9 2-2 a) 210 b) ()
70 % 0.1ng-TEQ/Nm 3 95% 1ng-TEQ/Nm 3 RHF+ 10
71 VM /
72 (1) RHF RHF (2) (2) RHF 1819 VM 18 95% Zn 0.1ng-TEQ/Nm3 19 RHF t (2) t /RHF
73 (3) (3) (71 ) (3)-2. DRI RHF 3.9% 95%
74 (1) RHF 3rd 37275t DRIDRI DRI DRI 14
75 3-4 (2) 95% 0.1ng-TEQ/Nm3 95% (3) CBQCold Briquette CBQ RHF RHF CBQ RHF DRI DRI N2 RHF DRI DRI DRI RHF CBQ RHF
76
77 (4) (4) CBQ % 3-7. wt% C H 4.07 N 2.09 S 0.28 O 0.95 (4)-2 RHF CBQ RHF % 95% RHF 3-9 RHF SOx 17
78 3-8 wt% E F G 3-9 t/h ,3301,360 E,F,G (4)-3 1) AG263t OZnO A G 18
79 100 DRI 2) // 3-4 = [ 1 { (DRI Zn%)/(DRI T.Fe%) } / { (CBQ Zn%)/(CBQ T.Fe%)} ] x 100 = [ 1 { (DRI Pb%)/(DRI T.Fe%) } / { (CBQ Pb%)/(CBQ T.Fe%)} ] x 100 = (DRI M.Fe%)/(DRI T.Fe%) x 100 (5) RHF 0.3% DRI DRI 3-4. / 19
80 3-4. EFG 95% Fe 7090% CBQ CBQ RHF CBQ 95% % 3) 3-10 RHF Fe (CaO, MgO, SiO2, Al2O3) 1% 3-6 ZnO, PbO, T.Fe 20
81 3-10 % ZnO, PbO, T.Fe 4) DRI DRI 3-11 (2) // Zn, Pb, Fe CaO, MgO, SiO2, Al2O DRI (%) * DRI DRI ZnO, PbO T.Zn, T.Pb ZnO,PbO 21
82 5) RHF (1)DRI DRI 24.8%, 0.3%RHF 100 x 24.8/100 = x 0.3/100 = /24.8 x 100 = 0.4% DRI Fe Fe 95% Fe Fe
83 6) ng-TEQ/Nm nd 3rd 3rd 4 th O D g/nm <0.001 <0.001 SOx V/Vppm 2 < NOx V/Vppm ng-teq/nm
84 7) 7)-1 1/10 RHF CBQ 3-13 CBQ ZnO CBQ T.Fe ZnO C CaO SiO2 Cl <1 3-8 DRI 50%90% 3-8 RHF DRI 24
85 7)-2 VM VM VM T.Fe 67% 37%, 9% () % CBQ DRI RHF RHF 8) 3rd RHF mm
86 (5) 95% Zn 95% Zn Pb Fe 1% Fe 0.4% 0.1ng-TEQ/Nm3 VM RHF RHF 26
87 () (1) 18 () ([C]) 19 [S] () (71 )
88 3-15 1) 1st3rd.() () () () 2) 4th.5th.() 2 (DRI) 3) 6th.7th.()
89 / 3-9 (DRI) 1st.3rd. 1 (a) 4th. 2 (b)7th. DRI (c) 3-10 DRI 3-11 DRI DRI
90 25,000 20,885 20,000 DRIkg 15,000 10,000 5, ,622 2, CP1 CP2 CP3 CP4 CP5 CP6 CP DRI 4,000 3,500 5th'07/5/96/7 6th'07/7/38/2 7th'07/9/2410/ ,000 DRIkg/ch) 2,500 2,000 1,500 7th 60 1,000 6th th ,200 1,600 2,000 kg/h 3-11 DRI 30
91 (2) () () 35 () () (/) /DRI ([C] (DRI) DRI (/) DRI () 31
92 (3) (3) DRI
93 3-13 () DRI RHF()DRIRHF
94 (3) () C O2 CO DRI 500 () CO DRI DRI DRI DRI
95 m 2.1m 900Nm3/h 60Nm3/h 3/hr 60 NaOH 11,000Nm3/hr, 1000 (4) (4)-1 35
96 [C] COCO 2 O 2 [C] 400mm (4)-2 DRI
97 (4)-3 1) C O2 CO O2 COCO 2 O2 DRI ( 3-15 ) :25:00 14:26:30 14:28:00 14:29:30 14:31:00 14:32:30 14:34:00 14:35:30 14:37:00 14:38:30 14:40:00 14:41:30 14:43: :44:30 14:46:00 14:47:30 14:49:00 14:50:30 14:52:00 14:53:30 14:55:00 14:56:30 14:58:00 14:59:30 15:01:00 15:02:30 15:04:00 15:05:30 15:07:00 15:08:30 15:10:00 15:11:30 15:13:00 15:14:30 2) (DRI)3rd. DRI DRI CO ( 3-16 ) 3-16 (DRI)(3rd.) 37
98 3) [C] DRI DRI [C]( 3-17 ) 1, ,500 1,400 C 1,498 1,488 1, ,463 1,384 1,364 1,355 1,347 1,342 1, ,503 1, , , ,459 1,444 1,444 1, ,458 1,452 1,449 1, ,516 1,506 1, ,428 1, C 1, , :43 12:57 13:12 13:26 13:40 13:55 14:09 14:24 14:38 14:52 15:07 15:21 15:36 15:50 16: [C] 4) COCO 2 2 DRI CO Nm 3/h Nm 3/h DRI 1600 CO/CO2/O :00:00 13:04:50 13:09:40 13:14:30 13:19:20 13:24:10 13:29:00 13:33:50 13:38:40 13:43:30 13:48:20 13:53:10 13:58:00 14:02:50 14:07:40 14:12:30 14:17:20 14:22:10 14:27:00 14:31:50 14:36:40 14:41:30 14:46:20 14:51:10 14:56:00 15:00:50 15:05:40 15:10:30 15:15:20 15:20:10 15:25:00 15:29:50 15:34:40 15:39: :44:20 15:49:10 15:54:00 15:58:50 38
99 5) th. DRI = % % 15% 10.0 /min 5.0 No ,000 1,500 2,000 2,500 3,000 (5.0) (10.0) DRIkg/h ) th.DRI 1,724kg 1.7t-DRI/h () 3540 DRI Input Output Input Output Si COCO2 1, Fe DRI ,523 1, Mcal Mcal % %
100 7) 3-21 Input DRI Output CO/CO2 dust dust Input Output 95.4 =( DRI Input 20% Input C 3% Output C dust 1% 5% 25% DRI 7% 73% COCO2 66%
101 8) DRI (3,750kg)H.No.71B1( ) DRI Output Fe Input Fe slag 0.4% dust 1.0% 2.4% DRI 34.1% 30.3% 65.9% 65.9% DRI ) S S 3-23 DRI S Output S dust dust S dust S S H2SCOS dust S Input Output DRI Input S DRI S Output S dust S S S 41
102 19.1% Input S 2.8% S 1.5% Output S 7.6% 31.2% DRI 24.1% 56.8% slag 11.4% dust 45.5% 3-23 S 10) P P 3-24 [P] DRI P Output P Input Output P Output DRI Input P DRI P Output P P Input P P 9.3% DRIP 6.1% 0.5% slag 7.2% Output P 0.4% 91.9% 84.7% 3-24 P 42
103 11) DRI DRI 3-25 DRI DRI 800 DRI 1.4 DRI DRI800 DRIton/h DRI 800 DRIton/h DRI 25 ton/ ton/ 3-25 DRI 12) DRI (3,750kg) H.No.71B1( )( 3-26[C] 3-27 DRI ) 1 2 DRI 2,025kg1,725kg= 3,750kg [C] DRI Max.2t/h 43
104 1, ,500 1,505 1,481 1,467 1,521,523 1,500 1,482 1,473 1,563 1,548 1,548 1,484 1,565 1,554 1,541 1,538 1,541 1,530 1,520 1,527 1,516 1,515 1,500 1, ,421 1,430 1, ,400 1,300 1, , C , C 1, :31 11:45 12:00 12:14 12:28 12:43 12:57 13:12 13:26 13:40 13:55 14:09 14:24 14:38 14:52 15:07 15:21 15:36 15:50 16:04 16:19 16:33 16: [C] :30:00 11:38:10 11:46:20 11:54:30 12:02:40 12:10:50 12:19:00 12:27:10 12:35:20 12:43:30 12:51:40 12:59:50 13:08:00 13:16:10 13:24:20 13:32:30 13:40:40 13:48:50 13:57:00 14:05:10 14:13:20 14:21:30 14:29:40 14:37:50 14:46:00 14:54:10 15:02:20 15:10:30 15:18:40 15:26:50 15:35:00 15:43:10 15:51:20 15:59:30 16:07:40 16:15:50 16:24: DRI 44
105 13) SUS SUS 3-28 SUS NiCr DRI NiCr DRI Ni 76 Cr SUS 45
106 14) (7th ) 3-29 (T.Fe) 1.2 T.Fe 3-29 (T.Fe) 46
107 (5) (5)-1 RHF ( 3-30 ) (DRI) DRI
108 (5) ) COREXFINEX (Midrex ) (FINMET) 6 (*1) () (*1); COREX;FINEX; 2) (RHF) (FASTMELT) DRI FASTMELT 20-30%
109 (5)-3 (5)-4 RHF RHF RHF VM / (5)-5 / DIOS, HIsmelt), COREX ( 5t )( 10t
110 (6) [] [C]>4% t 2.0t/h DRI DRI 90-70% DRI 2 50
111 (7) (7)-1 DRIDRI S S S DRI Fe S S S (7)-2 CaO S S (7) RHF CaO RHF
112 (7) t (7)-5 S S S S t S 0.03% FASTMELT 0.2%0.4% Si
113 CaO-Al 2 O 3 1t rpm t 4.5%C0.3%Si S0.03%0.2%0.4% 1450 CaOAl 2 O 3 Al2kg S=0.2,0.4% 500mm rpm (7)-6 1) S [S] 0.03%300ppm S kg/t 210rpm [S] 5ppm 3-35 S kg/t 53
114 2) S [S] 0.2% 0.4% S kg/t 215rpm [S]0.19%[S]0.031% 3-36 S (7)-7 FASTMELT S S 54
115 3-22 (a) (b) (a)+(b) () () 55
116 ( ) () 3-23 H H20.5 DEVELOPMENT OF EAF DUST RECYCLING AND MELTING TECHNOLOGY USING THE COAL-BASED FASTMELT PROCESS AIST Scrap Substitues and Alternative Ironmaking V (:) H20.11 ( 154 1) H19.9 2)(RHF 3) ( 155 H20.3 1)-2 2) ( R&D Vo.158, No.1 H20.4 FASTMELT 2 nd International Symposium on Sustainable Ironmaking() H20.9 ( 156 H20.9 1)-3 3 () H20.10 No H18.2 No H18.3 No H18.3 No H19.4 No H19.5 No H19.7 No H19.7 No H19.7 No H19.8 No H19.8 No H19.9 No H19.9 No H19.9 No NOx H20.2 No H20.3 No H20.3 No H
117 3-24 (95%) 0.1ng-TEQ/Nm 3 95% 95% 0.1ng-TEQ/Nm 3 95% % 0.1ng-TEQ/Nm 3 95% 0.1ng-TEQ/Nm 3 95% 57 95% SUS Ni,Cr
118 21 DRI FS
119 ,000 /t 60,000 /t 30,000 /t / 59
120 , CrNi Cr Ni LME 184,000 /t ,000 /t
121 (DRI) DRI 61
122 COREX&FINEX 2002 VM / CO
123 : 10,500 kl) CO2 29,000 t-co (179) ( );2007 2, (1) 1ton + 11,800MJ 1,700MJ 1,780MJ 10,720MJ 2,630MJ ,500MJ 15,100MJ 1,600MJ TJ 38.2MJ/l 10,500 kl 400(TJ/) x 1,148 /GJ2,100 /GJ= / ( ) 2007 CO2 400(TJ/) x 20(t-C/TJ) x 0.99 x 44/12(CO2/C) = 29,000 t-co2 NEDO 19 63
124 (2) 1) % % (6 ) % (6 )11.25 (45.0 ) ( ) ) % 95% 60% %95%60% (17.81 ) %95%60% (59.37 ) ( ) ) (75 ) (31.3 ) ( )
125 15 19 (1) (2) (3) (SUS ) (4) FASTMET
126
127 67
128
129 1/ 1/ 1/ 69
130 , , ( )
131
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