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Optimum temperatures for carbon deposition duringintegrated coal pyrolysis –tar decomposition (CVIironmaking)
Rochim B. Cahyono , Naoto Yasuda, Takahiro Nomura,Tomohiro Akiyama
Center for Advanced Research of Energy & Materials,Hokkaido University, JAPAN
Kuala Lumpur, Dec 12-14, 2013
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Ironmaking industry
[1] World Steel Association, 2011. Steel statistical yearbook 2011.; [2] The Japan Iron and Steel federation. ; [3] http://1ms.net/chevrolet-camaro-indianapolis-500-pace-car-221845.html; [4] http://atlazcrew-world.blogspot.jp/2012/04/my-dream-jalur-lintas-nusantara.html; [5] http://www.ipact.com/solutions/blast-furnace-applications/
Raw materials : Coal (HG) = 690 kg/ton-pig ironIron ore (HG) = 1390 kg/ton-pig iron
Consumes around 5% of the total world energy[=24 EJ]Energy recovery : 25.3 % of input energyCO2 emission: 1519 kg-CO 2/ton-pig iron
Years
P i g i r o n p r o d u c
t i o n ,
1 0 3 M t
World pig iron production
Pig iron
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Dehydration process
(a)
Micropore
Macropore
Mesopore
Removing H2O during dehydration processcreated porous ore with layer by layer structureThe micropore/mesopore was predominat in thedehydrated ore
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A higher temperature resulted in a
large reduction degree because ofindirect reduction of CO and fastreduction rate.FeO was found at hightemperature; this is consistent withthe phase diagram.
30 40 50 60 70 802θ [degree]
I n t e n s i t y [ a . u ]
400 oC
500 oC
600 oC
700 oC
800 oC
Dehydrated ore
Fe2O3 Fe3O4 FeOH ore; pyro lysis temp : 800 oC
(b)
0
0.2
0.4
0.6
0.8
1
400 500 600 700 800 900 1000Tar decomposition temp [ oC]
Fe
Fe3O4
FeO P C
O
P C O
+ P C
O 2 [ - ]
Fe2O3
H ore; pyrolysis temp : 800 oC
(a)
2
243
24332
COFeCOFeO
CO3FeOCOOFe
;COO2FeCOO3Fe
Tar decomposition
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0
20
40
60
0 5 10 15
P o r e s i z e
d i s t r i b u t i o n
[ 1 0 - 6 m
3 / n m / k g ]
Pore size [nm]
DH
400600
800
: Dehydrated ore (DH)
: Tar decomposition at 400o
C: Tar decomposition at 600 oC
: Tar decomposition at 800 oC
H ore;
Pyrolysis temp: 800 oC
86.7
21.9 20.32.8
DH 400 600 800
BET surfacearea [m 2/g]
Tar decomposition temp [ oC]
3.15
3.89
1.94
400 600 800
Carbon deposition [%mass]
Tar decomposition temp [ oC]
Tar decomposition
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Smallest carbon depositionbut largest deceasing ofsurface are and poredistribution, why??
The amount of carbon deposition should beproportional with the decreasing of surfacearea and pore size distribution.The melting point of the iron ore (Fe 2O 3) was1733 K(=1460 oC)
Sintering process
[14] HSC chemistry 7.0; [15] Canovaa, IC. et.al. Materials Research Vol. 2, No. 3, (1999) 211-217
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-0.16
-0.14
-0.12-0.10
-0.08
-0.06
-0.04
-0.02
0.00
0.02
100 300 500 700 900 1100 1300
W e i g h t c
h a n g e r a t i o =
[ - ]
Temperature [ oC]
.Carbonized ore - Lignite
∆ W W o
Heating rate = 50 oC/minAtmosphere = Argon (500
NmL/min )
Reagent Fe 3O4 + coke
COFeCFeO;COFeO3COFe 43
Reactivity of CVI ore
~nm
The nano-scale contact between iron ore and carbon enhances thecontacting area and results in the increasing of reaction rate
Iron ore
Carbon
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Iron oreCoke (carbon)
~cm
[16] http://webs.purduecal.edu/civs/research/educationtraining/virtual-blast-furnace/
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Reactivity of CVI ore
The carbonized ore was also useful and effective in the reduction reaction whichwas indicated by decreasing of carbon content during reduction reactionThe XRD result confirmed that the reduction reaction was started at 750 - 900 oC
Reduction of Fe 3O 4 to FeO was started
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Reactivity of CVI oreTransforming of iron compound in each experiment steps
The final product of CVI ore can be sent directly to blast furnace and
sintering machine
30 40 50 60 70 80
I n
t e n s
i t y [
a . u
]
2θ [degree]
Fe2O3 FeOFeOOH FeFe3O4
Original ore
Dehydrated oreat 450 oC
Carbonizationat 600 oC
Reduction a t900 oC
OHOFeOH2FeO 232
24332
243232
COOFe2COO3Fe
OHO2FeHO3Fe
COFeCFeO
CO3FeOCOFe 43
Tar decomposition
Direct reduction at
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Conclusions
The highest deposited carbon was obtained at tar decomposition
temperature of 600o
C. At elevated temperature, the amount of deposited carbon decreased dueto carbon gasification.
At tar decomposition temperature of 800 oC, the FeO was found but thesintering phenomena was startedThe deposited carbon within iron ore showed promising candidate as goodreducing agent due to higher reactivity and lower reduction temperature.The reactivity of carbon-deposited ore increased because carbondeposited within iron pores and caused nanoscale contact between theiron ore and carbon.
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