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920kW급 이동식 소형 발전설비 개발

09.15.2006

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엔진기계사업본부(본부장 : 최원길 전무)는 힘센엔진 S타입(8H17/28)을 탑재한 소형 이동식 발전설비(PPS)를 개발, 최근 성공적으로 제작을 마쳤습니다.

이번에 개발한 PPS는 기존의 PPS와 달리, 컨테이너 외부에 있던 연료공급장치를 엔진 크기를 줄여 컨테이너 내부로 통합 탑재하였고, 엔진 기동방식을 압축공기방식에서 전기방식으로 간편화시킨 것이 특징입니다.

이번 제품은 출력이 920kW로 기존 설비(1천700kW)보다 작지만 이동과 설치가 쉽고 작동이 쉬워서 시장성이 클 것으로 기대하고 있습니다.

LIST

Fuel	Pros	Cons	CO2 (Tank to propeller, Oil is 1.0)	TRL1) (Technology Readiness Level)	Fuel Cost (ton)	Eng. Cost (Main Engine, oil is 1.0)
LNG	High energy density Big gas reserves Sulphur free	Higher CO2 emission than others	0.8	9	$310	1.4
LPG	Less CO2 than MGO Sulphur free	Heavier than air Easy phase change	0.9	9	$340	1.5
Methanol	Sulphur free Low CO2 emission Easy transport & Store	Toxic Low energy density	0.9	6	$410	1.5
Ammonia	Sulphur free Low CO2 emission Easy transport & Store	Toxic & Corrosive Low energy density No bunkering Infra. No IGF code	0.1	2	$500	1.7
Hydrogen	Sulphur free Low CO2 emission	High OPEX Low energy density No bunkering Infra.	0.0	-	Over $10,000	N/A

Fuel

Pros

Cons

CO2
(Tank to propeller,
Oil is 1.0)

TRL1)
(Technology
Readiness Level)

Fuel Cost
(ton)

Eng. Cost
(Main Engine, oil is 1.0)

LNG

High energy density
Big gas reserves
Sulphur free

Higher CO2 emission than others

0.8

$310

1.4

LPG

Less CO2 than MGO
Sulphur free

Heavier than air
Easy phase change

0.9

$340

1.5

Methanol

Sulphur free
Low CO2 emission
Easy transport & Store

Toxic
Low energy density

0.9

$410

1.5

Ammonia

Sulphur free
Low CO2 emission
Easy transport & Store

Toxic & Corrosive
Low energy density
No bunkering Infra.
No IGF code

0.1

$500

1.7

Hydrogen

Sulphur free
Low CO2 emission

High OPEX
Low energy density
No bunkering Infra.

0.0

Over $10,000

N/A

Fuel	Pros	Cons	CO2 (Tank to propeller, Oil is 1.0)	TRL1) (Technology Readiness Level)	Fuel Cost (ton)	Eng. Cost (Main Engine, oil is 1.0)
LNG	High energy density Big gas reserves Sulphur free	Higher CO2 emission than others	0.8	9	$310	1.4
LPG	Less CO2 than MGO Sulphur free	Heavier than air Easy phase change	0.9	9	$340	1.5
Methanol	Sulphur free Low CO2 emission Easy transport & Store	Toxic Low energy density	0.9	6	$410	1.5
Ammonia	Sulphur free Low CO2 emission Easy transport & Store	Toxic & Corrosive Low energy density No bunkering Infra. No IGF code	0.1	2	$500	1.7
Hydrogen	Sulphur free Low CO2 emission	High OPEX Low energy density No bunkering Infra.	0.0	-	Over $10,000	N/A

Fuel

Pros

Cons

CO2
(Tank to propeller,
Oil is 1.0)

TRL1)
(Technology
Readiness Level)

Fuel Cost
(ton)

Eng. Cost
(Main Engine, oil is 1.0)

LNG

High energy density
Big gas reserves
Sulphur free

Higher CO2 emission than others

0.8

$310

1.4

LPG

Less CO2 than MGO
Sulphur free

Heavier than air
Easy phase change

0.9

$340

1.5

Methanol

Sulphur free
Low CO2 emission
Easy transport & Store

Toxic
Low energy density

0.9

$410

1.5

Ammonia

Sulphur free
Low CO2 emission
Easy transport & Store

Toxic & Corrosive
Low energy density
No bunkering Infra.
No IGF code

0.1

$500

1.7

Hydrogen

Sulphur free
Low CO2 emission

High OPEX
Low energy density
No bunkering Infra.

0.0

Over $10,000

N/A

Property	MGO	LNG	LPG	Methanol	L_NH3	L_H2
Flash point [℃]	52	-188	-105	11	132	-150
Auto ignition temperature [℃]	250	595	459	464	651	535
Boiling point at 1 bar [℃]	20	-162	-42	20	-34	-253
Low Heating Value [MJ/kg]	42.7	50.0	46.0	19.9	18.6	120
Density at 1 bar [kg/m3]	870	470	580	792	682	71
Energy density [MJ/L]	36.6	21.2	26.7	14.9	12.7	8.5
Fuel tank size	1.0	1.7	1.4	2.5	2.9	4.3
Ignition energy [MJ]	0.23	0.28	0.25	0.14	8	0.011
Flammable concentration range in the air [%]	0.6 - 7.5	5 - 15	2.2 - 9.5	5.5 - 44	15 - 28	4 -75

Property

MGO

LNG

LPG

Methanol

L_NH3

L_H2

Flash point [℃]

-188

-105

132

-150

Auto ignition temperature [℃]

250

595

459

464

651

535

Boiling point at 1 bar [℃]

-162

-42

-34

-253

Low Heating Value [MJ/kg]

42.7

50.0

46.0

19.9

18.6

120

Density at 1 bar [kg/m3]

870

470

580

792

682

Energy density [MJ/L]

36.6

21.2

26.7

14.9

12.7

8.5

Fuel tank size

1.0

1.7

1.4

2.5

2.9

4.3

Ignition energy [MJ]

0.23

0.28

0.25

0.14

0.011

Flammable concentration range in the air [%]

0.6 - 7.5

5 - 15

2.2 - 9.5

5.5 - 44

15 - 28

4 -75

Property	MGO	LNG	LPG	Methanol	L_NH3	L_H2
Flash point [℃]	52	-188	-105	11	132	-150
Auto ignition temperature [℃]	250	595	459	464	651	535
Boiling point at 1 bar [℃]	20	-162	-42	20	-34	-253
Low Heating Value [MJ/kg]	42.7	50.0	46.0	19.9	18.6	120
Density at 1 bar [kg/m3]	870	470	580	792	682	71
Energy density [MJ/L]	36.6	21.2	26.7	14.9	12.7	8.5
Fuel tank size	1.0	1.7	1.4	2.5	2.9	4.3
Ignition energy [MJ]	0.23	0.28	0.25	0.14	8	0.011
Flammable concentration range in the air [%]	0.6 - 7.5	5 - 15	2.2 - 9.5	5.5 - 44	15 - 28	4 -75

Property

MGO

LNG

LPG

Methanol

L_NH3

L_H2

Flash point [℃]

-188

-105

132

-150

Auto ignition temperature [℃]

250

595

459

464

651

535

Boiling point at 1 bar [℃]

-162

-42

-34

-253

Low Heating Value [MJ/kg]

42.7

50.0

46.0

19.9

18.6

120

Density at 1 bar [kg/m3]

870

470

580

792

682

Energy density [MJ/L]

36.6

21.2

26.7

14.9

12.7

8.5

Fuel tank size

1.0

1.7

1.4

2.5

2.9

4.3

Ignition energy [MJ]

0.23

0.28

0.25

0.14

0.011

Flammable concentration range in the air [%]

0.6 - 7.5

5 - 15

2.2 - 9.5

5.5 - 44

15 - 28

4 -75

920kW급 이동식 소형 발전설비 개발

파워플랜트 셀렉터

Step 1. 발전소 규모

Step 2. 연료선택

Step 3. 운전모드

Step 4. 건물타입

개인정보처리방침

Feature of Eco-friendly Fuels

Physical Properties of Eco-friendly Fuels