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*Главный двигатель Модель 5S70MC – C производитель HSD – MAN B&W .doc
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Расчет паропотребления судна

1. General

Steam consumption is calculated under the following operational conditions

  1. Sea going

  2. Cargo oil tank heating

  3. Maneuvering

  4. Cargo unloading

  5. In-port

  6. Cargo oil tank cleaning

2. Design criteria

1) Environmental data

Environmental condition

Winter (°C)

I.S.O. ((°C)

Atmosphere

-10

25

Sea water

0

25

Ballast water

0

25

Pump room

10

25

Engine room

15

25

2) Temperature in tank

F.O. tank

45

HFO settling tank

60

HFO service tank

85

Cargo oil tank

66

Slop tank

66


3) Heating-up temperature and time

Tank

Winter

Heating-up time

F.O. tank Cargo oil tank Slop tank

From5°C to 45°C From 44 °C to 66°C From 44 °C to 66°C

96 Hours 96 Hours 24 Hours

4) Available enthalpy

Heating method

Application

7 kg/cm2g (kcal/kg)

9 kg/cm2g (kcal/kg)

Heater Tank

490 540

*573 **543

* For the tank cleaning heater

** For the cargo and slop tank heating

5) Specific gravity and specific heat

Fluid

Specific gravity

Specific heat

(kcal/kg °C)

Sea water

1.025

0.94

Fresh water

1.000

1.00

H.F.O.

0.980

0.45

L.O.

0.900

0.45

Cargo oil

0.850

0.45

For the calculation of cargo oil tank heating

3. Main components

1) Steam generating plant

Oil fired boiler

Exhaust gas economizer

Type

Vertical water tube

Forced circulation

No. of sets

2

1

Evaporation x Pressure (kg/h x kg/cm2g)

25,000x16/7

1,500x7

Design Condition

-

NCR load of M/E and I.S.O. reference conditions

2) Main engine and Gen. engine

Main engine

Gen. engine

Type

B&W 5S70MC-C

4-Stroke

No. of sets

1

3

MCR (ВНР x rpm)

21,100x91.0

1,090x720

NCR (ВНР x rpm)

18,990x87.9

-

3) Heater

Description

Set

Flow rate (m3/h)

In/out temperature (°C)

M/E F.O. heater

2

6.9

100.0/150.0

G/E F.O. heater

2

1.5

100.0/150.0

A/B F.O. heater

2

4.3

55.0/145.0

H.F.O. purifier heater

2

. 3.6

60.0/98.0

L.O. purifier heater

2

2.4

45.0/98.0

Tank cleaning water heater

1

180.0

20.0/80.0

Calorifier

1

1.0

10.0/70.0

4) Steam driven pump

Description

Set

Capacity (m3/h x mTH)

Type

Steam consumption (kg/h)

Cargo oil pump

3

3,000x125

Vertical centrifugal with 1-stage steam turbine

13,268

Cargo stripping pump

1

200x125

Reciprocating

2,910

Proj. No. : H.5230

STEAM

CONSUMPTION

CALCULATION

Date: Feb.27, 2003

WINTER

CONDITION

DESCRIPTION

DESIGN

SEAGOING

TANK HEATING

MANEUVERING

UNLOADING

IN-PORT

TANK CLEANING

NO

EACH CAPACITY

P

AMOUNT

NO

%

STM

NO

%

STM

NO

%

STM

NO

%

STM

NO

%

STM

NO

%

STM

M/E F.O. Heater

2

6.9m3/h (100/150 °C)

7

311

1

56

173

1

56

173

1

36

110

0

0

0

0

0

0

1

56

173

G/E F.O. Heater

2

1.5m3/h (100/150 °C)

7

68

1

22

15

1

35

23

1

35

23

1

35

23

1

22

15

1

35

23

HFO Purifier Heater

2

3.6 m3/h ( 60/ 98 °C)

7

123

1

100

123

1

100

123

1

100

123

1

100

123

1

100

123

1

100

123

A/B FO Heater

2

4.3m3/h ( 55/145 °C)

7

348

1

7

25

1

63

221

1

25

87

1

72

251

1

8

28

1

60

209

LO Purifier Heater

2

2.4 m3/h ( 45/ 98 °C)

7

105

1

87

91

1

87

91

1

89

94

0

0

0

0

0

0

1

87

91

Boiler warm-up

2

For Stand-By Boiler

7

50

1

100

50

0

0

0

1

100

50

0

0

0

1

100

50

0

0

0

A/B Burner Atomizing

2

Steam Atomizing

7

94

1

11

10

2

74

140

1

53

50

2

85

160

1

11

10

2

64

120

HFO Sett. Tank

1

72.6 m3 60 °C Keeping

7

120

1

54

65

1

94

113

1

37

45

1

27

32

1

0

0

1

92

111

HFO Serv. Tank

1

72.6 m3 85 °C Keeping

7

48

1

39

19

1

39

19

1

39

19

1

39

19

1

39

19

1

39

19

Others

1

Misc. equipment/tanks

7

100

1

100

100

1

100

100

1

100

100

1

100

100

1

100

100

1

100

100

COP Turbine

3

3000 m3/h x125m

16

13,268

0

0

0

0

0

0

0

0

0

3

100

39,804

0

0

0

1

100

13,268

CO Stripping Pump

1

200m3/h x125m

16

2,910

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

Air Ejector

1

For Vacuum Condenser

16

320

0

0

0

0

0

0

0

0

0

1

100

320

0

0

0

1

100

320

Cargo Oil Tank

1

127315 m3 (44/66°C/96H)

9

28,088

0

0

1

100

28,088

0

0

0

0

0

0

0

0

0

0

0

0

127315 m3 66°C Keeping

9

10,040

0

0

0

■o

0

1

100

10,040

0

0

0

0

0

0

0

0

0

Slop Tank

2

1350.3 m3 ( 44/66 °C/24H)

9

1,583

0

0

0

2

100

3,166

0

0

0

0

0

0

0

0

0

0

0

0

2

1350.3 m3 66 °C Keeping

9

158

0

0

0

0

0

0

2

100

316

0

0

0

0

0

0

2

100

316

T.C. Heater

1

180m3/h (20/80 °C)

9

18,160

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

1

100

18,160

Ballast & FW Tanks

1

0 °CKeeping

9

4,568

0

0

0

0

0

0

0

0

0

0

0

0

1

100

4,568

1

100

4,568

No.1 H.F.O. Tank(S)

1

825.3 m3 (5/45°C/96H)

7

370

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

1

825.3 m3 45 °C Keeping

7

165

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

No.2H.F.O. Tank(S)

1

996.9 m3 (5/45°C/96H)

7

478

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

1

996.9 m3 45 °C Keeping

7

248

1

100

248

1

100

248

1

100

248

1

100

248

1

100

248

1

100

248

No.1 H.F.O. Tank(P)

1

733.3 m3 (5/45°C/96H)

7

330

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

1

733.3 m3 45 °C Keeping

7

152

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

No.2 H.F.O. Tank(P)

1

909.0 m3 (5/45°C/96H)

7

414

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

1

909.0 m3 45 °C Keeping

7

221

1

100

221

1

100

221

1

100

221

1

100

221

1

100

221

1

100

221

Accomm. Heating

1

100%Capa. (-30/20°C)

7

650

1

79

514

1

79

514

1

79

514

1

79

514

1

79

514

1

79

514

Calorifier

1.0m3/h ( 10/70°C)

7

122

1

36

44

1

36

44

1

36

44

1

36

44

1

36

44

1

36

44

Sub Total

1,696

33,283

12,084

41,859

5,939

38,627

Pipe loss & margin( 5%

85

1,664

604

2,093

297

1,931