Status and Future of FINEX Process for Reducing CO2 Emissions and Steel... · POSLAB 20 Innovate...

21
Innovate Steel, Design Future 1 POSLAB 1 5 November 2013 Status and Future of FINEX ® Process for Reducing CO 2 Emissions

Transcript of Status and Future of FINEX Process for Reducing CO2 Emissions and Steel... · POSLAB 20 Innovate...

Page 1: Status and Future of FINEX Process for Reducing CO2 Emissions and Steel... · POSLAB 20 Innovate Steel, Design Future ®After starting R&D activities of FINEX in 1992, it is being

Innovate Steel, Design Future 1 POSLAB 1

5 November 2013

Status and Future of FINEX® Process

for Reducing CO2 Emissions

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Contents

1. Introduction of FINEX® Process

2. Direct Reduction of CO2 Emissions

3. Indirect Reduction of CO2 Emissions

4. Future of FINEX® Process

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Contents

1. Introduction of FINEX® Process

2. Direct Reduction of CO2 Emissions

3. Indirect Reduction of CO2 Emissions

4. Future of FINEX® Process

- Scale up History

- FINEX® Process Flow

- Characteristics of FINEX® Process

Page 4: Status and Future of FINEX Process for Reducing CO2 Emissions and Steel... · POSLAB 20 Innovate Steel, Design Future ®After starting R&D activities of FINEX in 1992, it is being

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1996 1999 2003 2007

Pilot Plant

(150t/d)

No.1 FINEX®

(0.6 MTPA)

Model Plant

(15t/d)

1992

Annual

Production

(MTPA)

2014

No.3 FINEX® (2.0 MTPA)

(Construction Site)

No.2 FINEX®

(1.5 MTPA)

2.0

1.5

1.0

0.5

0.0

Jun. 2003 0.6 MTPA FINEX® (Demo.)

Apr. 2007 1.5 MTPA FINEX®

Dec. 2013 2.0 MTPA FINEX®

FINEX® R&D

Kick-off

Scale-up History

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No.1 FINEX®

(0.6 MTPA)

No.2 FINEX®

(1.5 MTPA)

Panoramic Views

No.3 FINEX®

(2.0 MTPA) Melter-gasifier

Fluidized bed Reactor

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CO2

Removal

(PSA)

Power Plant

Oxygen Plant

Ore Fine Non-Coking

Coal

Melter Gasifier

Fluidized Bed Reactors

PCI

Oxygen

Coal Briquetter

Hot DRI Compactor

R2

R1

FINEX® Process Flow

R2

R1

R3

R4

Scrubber

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No pretreatment plants

Flexibility of raw materials in use

Environmentally-friendly process

Flexibility of hot metal production

Characteristics of FINEX® Process

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Contents

1. Introduction of FINEX® Process

2. Direct Reduction of CO2 Emissions

3. Indirect Reduction of CO2 Emissions

4. Future of FINEX® Process

- Coal Briquette

- CO2 Removal Process - Pulverized Coal Injection

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Briquettes

Binder

Coal Fine

Mixing

46

35

100

Lump

Coal

Coal

Briquette Coke

95 78

100

Lump

Coal

Coal

Briquette Coke

Cold Strength

Hot Strength

Coal Briquette

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CO2 Removal Process

Production (t/d)

Co

al C

on

sum

ptio

n R

ate

(k

g/t

HM

)

After CO2 Removal

Before CO2 Removal

1000

1100

1200

1300

1500 1800 2100 2400 2700

700

800

900

Coal

Heat

Gas

DRI

Off Gas Recycling

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Pulverized Coal Injection

Continuous Operation (days)

Reduction Degree (%)

37

83

200

300

Pulverized

Coal

Gas + Dust

Coal Pyrolysis

Hot Metal

Coal Briquettes

Coal Bq. Coal PC

Pyrolysis,

Dust loss

Dome,

Char Bed -

56% Raceway 100%

Gas

Carbon solution loss

Combustion

Fluidized Bed Reactor Availability

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FINEX COREX

Pro

du

ctio

n (

T/D

)

CO2 Rmv.

PCI

500

1000

2000 1,800 T/D (0.6MT)

1500

Co

al R

ate

(k

g/t

)

750

850

1050

950

2500 1150

1250 3000 Coal Briq.

2003 2004 2005 2006 2007

7 9 11 1 3 5 7 9 11 1 3 5 7 9 11 1 3 5 7 9 11 12 1 2 3 4

FINEX® Demo Plant Operational Performance

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Operating Parameters of No. 2 FINEX®

Indices Target

(designed)

Operation

(2008)

Production Mt/y 1.5 1.5

t/d ≥ 4,200 4,300

Coal Rate

kg/t-HM

≤ 730 720

Coke ≤ 70 60

PCR ≥ 140 150

Hot

Metal

[S] % ≤ 0.030 0.027

[Si] % ≤ 0.80 0.81

11

FINEX® Comm. Plant Operational Performance

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Contents

1. Introduction of FINEX® Process

2. Direct Reduction of CO2 Emissions

3. Indirect Reduction of CO2 Emissions

4. Future of FINEX® Process

- Heat Recovery System

- Dry Dust Collectors

- Recycling of By-products

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Heat Recovery System

Demineralized water

Steam 40 t/hr

260 ºC

13.5 bar

Off gas 300 kNm3/h,

380 ºC

230 ºC

Scrubber

Heat Recovery System

Reducing Gas Water Treatment System Heat Recovery System

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Dry Dust Collectors

Ceramic Filter

(Commercial Stage)

Multi-Cyclone

(Commercial Stage)

Bag Filter

(Pilot Stage)

Bag Filter

(Commercial Stage)

DRI Feed Bin

Fluidized Bed Reactors

700 ºC

380 ºC 230 ºC

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Recycling of By-products

Sludge

Hot Briquetter

DRI Feed Bin Dust

Fluidized Bed Reactors

DRI

Dryer

Melter-Gasifier

Composition(%) Total Fe RD C SiO2 CaO Al2O3 MgO

By-products 50~55 15~20 5~10 4~6 3~4 3~4 ~ 1

Agglomeration

Agglomerates

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Contents

1. Introduction of FINEX® Process

2. Direct Reduction of CO2 Emissions

3. Indirect Reduction of CO2 Emissions

4. Future of FINEX® Process

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CO2 Removal

Power Plant

Oxygen Plant

Ore Coal

Melter Gasifier

Fluidized Bed Reactors

PCI

Oxygen

Coal Briquetter

R2

FINEX® Process Flow

R1

R2

R3

TRT

Prep.

Tail Gas

CO2 Purification (CO2 > 95 %)

CO2 Sequestration

Product Gas

Heat Ex. Filter Scrubber

Chemical Plant

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After starting R&D activities of FINEX® in 1992, it is being scaled up to 2.0 Mt/y

CO2 emissions from FINEX® drastically fell down because POSCO has

developed coal briquetting process and has optimized the FINEX process

by adopting CO2 removal system and pulverized coal injection

A series of technical developments such as heat recovery system, dry dust

collectors and recycling by-products could reduce CO2 emissions furthermore

FINEX® has lots of potential for lowering coal consumption rate and saving energy

as a developing process

Summary

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