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26th World Gas Conference - IGU

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1 5 June 2015, Paris, France 26 th World Gas Conference World Scale Boil-off Gas Reliquefaction (BOGR) Heinz Bauer Linde Engineering / Germany
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Page 1: 26th World Gas Conference - IGU

1 – 5 June 2015, Paris, France

26th World Gas Conference

World Scale Boil-off Gas Reliquefaction (BOGR)

Heinz Bauer

Linde Engineering / Germany

Page 2: 26th World Gas Conference - IGU

World Scale Boil-off

Gas Reliquefaction Sources of Boil-Off Gas (BOG)

• Large LNG export terminals include a LNG tank farm with large LNG tanks

providing storage capacity of several hundred thousand meters cubed.

Low pressure gases at tank pressure (about 100 to 200 mbarg) originate

from several sources like

– Boil-off gas caused by heat ingress through the tank walls and LNG

pumps

– Flash gas generated in the run-down line between liquefaction and

storage as well as during cool-down of warm send-out systems

– Ship return gas / displacement gas during ship loading

• Total BOG flow rate for a 10 mtpa facility ~1,000 t/d

2

Page 3: 26th World Gas Conference - IGU

World Scale Boil-off

Gas Reliquefaction Concept Selection

• A BOG reliquefaction (BOGR) unit with 0.3 - 1.0 mtpa LNG is similar to a

mid-scale LNG plant

• Most land based plants of this size use SMR technology with ~350 kWh/tLNG

or 15 MW for 1000 t/d

• Feed gas compression to >50 bar requires about the same power as the

refrigeration cycle

• The preferred cryogenic heat exchanger is a coil wound heat exchanger

(CWHE)

• The cost adder for a CWHE is more than offset by its superior availability

• Mechanical drive with gas turbines is the preferred choice

• Electric motors should be considered only, if power supply is reliable and

economically attractive

3

Page 4: 26th World Gas Conference - IGU

World Scale Boil-off

Gas Reliquefaction Process Optimization

4

Base Case

—N2 stripper T

—LNG subcooler E3

— two casing EFG compressor

C3

—unbalanced power

between C1 and C2

Page 5: 26th World Gas Conference - IGU

World Scale Boil-off

Gas Reliquefaction Process Optimization

5

Optimized Case

—N2 flash drums D1 & D2

—no LNG sub-cooler required

—one casing EFG compressor

C3

—balanced power

between C1 and C2

Page 6: 26th World Gas Conference - IGU

World Scale Boil-off

Gas Reliquefaction Fuel Gas Composition

6

0

10

20

30

40

50

25 30 35 40 45

N2 i

n F

uel

Ga

s (

mo

l%)

Gas Turbine Efficiency (%)

8 mol%

6 mol%

4 mol%

2 mol%

N2 contentin BOG

Material Balance for N2

— limited amount of N2 in LNG

—GT's with high efficiency will

see high N2 content in fuel

—max. 8 mol% N2 in BOG are

acceptable for state-of-the-

art gas turbines

Page 7: 26th World Gas Conference - IGU

World Scale Boil-off

Gas Reliquefaction N2 Tolerant Gas Turbine

7

Annular combustor design

—premixed air and fuel as

main gas

—pilot flame burns around

main flame for stabilization

—18 3rd generation nozzles

(burners)

main fuel gas

18 burners

pilot gas

film air holes

Siemens SGT-700/800

courtesy Siemens

Page 8: 26th World Gas Conference - IGU

World Scale Boil-off

Gas Reliquefaction N2 Tolerant Gas Turbine

8

Operational flexibility

—DLE system can operate on

fuel gas with high inert gas

— stable combustion without

pulsations up to 40 vol% N2

—emission performance

independent of N2 content

Wobbe Index

increase by 80% in 2

minutes

qu

ick dro

p

LFP: low frequency pulsation courtesy Siemens

Page 9: 26th World Gas Conference - IGU

World Scale Boil-off

Gas Reliquefaction Boil-Off Gas Compressor

9

Adjustable inlet guide

vanes

—direct online start-up possible

— compact design

— large turn-down

— low maintenance

—plenty of references

courtesy Siemens

Page 10: 26th World Gas Conference - IGU

World Scale Boil-off

Gas Reliquefaction Boil-Off Gas Compressor

10

(yellow) Oil heated Seal Carrier

(green) Dry Gas Seal

(red) 3D Impeller

(blue) Inlet Guide Vane Unit (IGV)

Heated dry gas seal carrier

—avoids thermal shocks (e.g.

during start-up)

—protects from low and high

temperatures and from rapid

temperature fluctuations

—avoids condensate build-up

courtesy Siemens

Page 11: 26th World Gas Conference - IGU

World Scale Boil-off

Gas Reliquefaction Conclusions

• World-scale BOG reliquefaction has become reality

• Linde Engineering has successfully developed a new product

for the LNG industry

• Siemens contributed with innovative compressor and gas

turbine designs, which are proven in service and are highly

respected worldwide

• The first plant, which is based on this novel concept, is under

execution for Malaysia LNG in Bintulu and is scheduled

for start-up in mid 2015

11

Page 12: 26th World Gas Conference - IGU

World Scale Boil-off

Gas Reliquefaction Marlin Project in Bintulu/Malaysia

12 courtesy Petronas


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