examples of fuel switching

20
Examples of Fuel switching IGU WOC5 SG5.1 meeting Tokyo, Japan April 19th, 2007

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Page 1: Examples of Fuel switching

Examples of Fuel switching

IGU WOC5 SG5.1 meeting

Tokyo, Japan

April 19th, 2007

Page 2: Examples of Fuel switching

2

Index

Y steel Co.,Ltd(Ladle pre-heater)

Efficiency improvement with re-generative burner.

Senboku heat treatment Co.,Ltd

Quality and efficiency improvement with combustion and internal pressure control.

Nagahashi dyeing Co.,Ltd(Boiler)

Space saving with compact one-through boiler. Flash steam recovery system

Page 3: Examples of Fuel switching

3

1.Y steel Co.,Ltd

Ladle size:φ4,090×3,590LLadle capacity:130t(melted metal)temperature:1,000~1,100℃burner:785-P(200ℓ/h)

×1・・・heavy oil↓

Twin re-generative burnerTREG-1700K(150m3/h)×1

・・・Natural gas

Temperature Control:manual・・・heavy oil

↓proportional control

specifications

Ladle pre-heater

Page 4: Examples of Fuel switching

4

1-1. ladle pre-heater

electrode

Fuel-oxygen burner

Car transfer machine

Re-generative burner 1700K

Melted metal

Cutter

billet④ continuous casting

burner

move

scrap

① Arc furnace

③ Tundish

ladle(130t/ch)

② ladle pre-heater

1000~1100℃

1000~1100℃

130t/ch

ladle(130t/ch)

tundish

Page 5: Examples of Fuel switching

5

1-2. Ladle pre-heater appearance

Heat exchanger Ladle stand and burner

burner

ladle

Page 6: Examples of Fuel switching

6

1-3.Comparison with the previous one

previous present

burner capacity 2,070kW 1,700kW

Processing time 3.5h 2.45h

Exhaust gas temp 1,136℃ 263℃

Energy saving base line 57%

Installation cost base line 100,000euros

Annual profit base line 25,000euros

Page 7: Examples of Fuel switching

7

2.Senboku heat treatment Co.Ltd

type : car transfer annealing furnace

capacity : 120t/chdimension:4,000W×13,000L×3,500Hburner : PLB-3EL×18 ・・・・kerosene

temperature: 600~950℃

LC-400K-S×9・・・natural gas(3-zone impulse combustion)

specifications

The appearance of the furnace

Page 8: Examples of Fuel switching

8

2-1.Impulse combustion system

Ⓓ50%50%

50%50%

Ⓐ Ⓑ

Ⓒ Ⓓ

100%

0%

0%

100%

Ⓐ Ⓑ

Ⓒ Ⓓcyclecycle

ON ON

ON

ON

ON

ON

ON ON

ON ON

Typical one Impulse combustion Time table(50%)

①Two position control : stirring furnace atmosphere

②Unique time table : minimizing temperature distribution

Page 9: Examples of Fuel switching

9

2-2.furnace and burner

Car transfer unit Burner and peripheral devices

Page 10: Examples of Fuel switching

10

2-3.Energy saving and high quality

burner

burner

Previous one Present one

steel

Car

piers

steel

Car

Brick walls

Invasion air Invasion air

Pressure control damper

Invasion air Invasion air

X X

①Pressure control damper : preventing invasion air

②removing brisk walls : stirring furnace atmosphere

Page 11: Examples of Fuel switching

11

2-4.Furnace atmosphere

Previous one

Temperature distribution:50℃

Present one

Temperature distribution:10℃

Page 12: Examples of Fuel switching

12

2-5.Comparison with the previous one

previous present

burner capacity 5,400kW 3,600kW

Temp distribution 50℃ 10℃

Energy saving base line 20%

Installation cost base line 170,000euros

Annual profit base line 21,250euros

Page 13: Examples of Fuel switching

13

3.Nagahashi dyeing Co.,Ltd

specifications

Factory appearance

・boiler : replaceheavy oil・furnace pipe fire-tube boiler:8t/h・One through boiler : 4t/h

Natural gas・One through boiler : 12.5t/h・Flash steam recovery system

・Gas fired dyeing machineSwitching LPG to Natural gas

Page 14: Examples of Fuel switching

14

3-1.space saving (by 40%)

One-through boiler 2t/h

Oil tank

Fire-tube boiler4t/h

One-through boiler 2.5t/h×5

10

10

13.8 m 13.8 m

Fire-tube boiler4t/h

One-through boiler 2t/h

Previous one Present one

9.2m

9m

Page 15: Examples of Fuel switching

15

3-2.boiler appearance

Previous one Present one

Page 16: Examples of Fuel switching

16

3-3.previous system

boilerSteam header

Ste

am

eq

uip

men

t

Ste

am

equip

ment

Ste

am

equip

ment

condensate

pressure regulator

Flash steam

2㎏/㎠G

Steam trap

Steam trap

Steam trapcondensate

8㎏/㎠G

Page 17: Examples of Fuel switching

17

3-4.flash steam recovery system

boilerSteam header

Ste

am

eq

uip

men

t

Ste

am

equip

ment

Ste

am

equip

ment

condensate

pressure regulator

Flash steam

2㎏/㎠G

Steam trap

Steam trap

Steam trapcondensate

Fla

sh

tan

k

8㎏/㎠G

ejector

Page 18: Examples of Fuel switching

18

3-5.appearance of recovery system

Pressure pump

Flash tank

Flash steam pipe

Page 19: Examples of Fuel switching

19

3-6.factory appearance

Under construction Present factory

Page 20: Examples of Fuel switching

20

3-7.Comparison with the previous one

previous present

Space saving base line 40%

Energy saving base line 18%

Installation cost base line 500,000euros

Annual profit base line 71,500euros

CO2 reduction base line 602t/year