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3rd Trondheim Gas Technology Conference COIL WOUND HEAT EXCHANGERS FOR LNG - INVESTIGATION OF TRANSPORT PHENOMENA WITHIN THE BUNDLE Thomas Walter, Christiane Kerber, Konrad Braun, Carsten Richardt, Manfred Steinbauer Trondheim, 05.06.2014

3rd Trondheim Gas Technology Conference · 3rd Trondheim Gas Technology Conference COIL WOUND HEAT EXCHANGERS FOR LNG - INVESTIGATION OF TRANSPORT PHENOMENA WITHIN THE BUNDLE Thomas

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Page 1: 3rd Trondheim Gas Technology Conference · 3rd Trondheim Gas Technology Conference COIL WOUND HEAT EXCHANGERS FOR LNG - INVESTIGATION OF TRANSPORT PHENOMENA WITHIN THE BUNDLE Thomas

3rd Trondheim Gas Technology ConferenceCOIL WOUND HEAT EXCHANGERS FOR LNG - INVESTIGATION OFTRANSPORT PHENOMENA WITHIN THE BUNDLE

Thomas Walter, Christiane Kerber, Konrad Braun, Carsten Richardt, Manfred SteinbauerTrondheim, 05.06.2014

Page 2: 3rd Trondheim Gas Technology Conference · 3rd Trondheim Gas Technology Conference COIL WOUND HEAT EXCHANGERS FOR LNG - INVESTIGATION OF TRANSPORT PHENOMENA WITHIN THE BUNDLE Thomas

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IntroductionBackground

05.06.2014 TGTC-3 - Coil wound heat exchangers for LNG – Investigation of transport phenomena within the bundle

— Coil wound heat exchangers (CWHEs) in LNG industry as Precoolers / Liquefiers / Subcoolers

— Dimensions up to 10,000 tubes 30,000 m² heating surface area 20 m in height 5 m in diameter

— Natural Gas is on tube side

— Refrigerant streams are on tube side and shell side

— Refrigerant is flashed over Joule-Thomson valve and flows downwards on shell side, evaporating as falling film

Shell side mal-distribution will lead to radial temperature differencesresulting in a reduced performance of the CWHE

Liquid mal-distribution can be triggered by uneven distribution from liquid distributor or by liquid migration effects within bundle

Page 3: 3rd Trondheim Gas Technology Conference · 3rd Trondheim Gas Technology Conference COIL WOUND HEAT EXCHANGERS FOR LNG - INVESTIGATION OF TRANSPORT PHENOMENA WITHIN THE BUNDLE Thomas

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IntroductionAim

— Improve understanding of physics within bundle Optimize CWHE's with respect to size and performance

— Investigate influence of transport phenomena on shell side distribution and heat exchanger performance at various conditions with regard to:

— vapour fraction

— heat input

— liquid distribution

— gas and liquid load

— By use of

— adjustable liquid distribution system

— liquid collecting system

— glass fibre full 3D-temperature measurements

05.06.2014 TGTC-3 - Coil wound heat exchangers for LNG – Investigation of transport phenomena within the bundle

Page 4: 3rd Trondheim Gas Technology Conference · 3rd Trondheim Gas Technology Conference COIL WOUND HEAT EXCHANGERS FOR LNG - INVESTIGATION OF TRANSPORT PHENOMENA WITHIN THE BUNDLE Thomas

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Pilot plantOverview

05.06.2014 TGTC-3 - Coil wound heat exchangers for LNG – Investigation of transport phenomena within the bundle

Refrigerant: 80% n-Pentane, 20% Iso-Octane up to 14,000 kg/h 1.3 bar(a)

Process (principle)

LNG (warm water) Up to 80,000 kg/h

73.9 °C(x=1.00)

1260kW50.5 °C

(x=0.02)

53.4 °C

78.3 °C

Duty

Tem

pera

ture

LNG (warm water)

Refrigerant

Page 5: 3rd Trondheim Gas Technology Conference · 3rd Trondheim Gas Technology Conference COIL WOUND HEAT EXCHANGERS FOR LNG - INVESTIGATION OF TRANSPORT PHENOMENA WITHIN THE BUNDLE Thomas

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Pilot plantCWHE

05.06.2014 TGTC-3 - Coil wound heat exchangers for LNG – Investigation of transport phenomena within the bundle

Pilot plant CWHE:

— Bundle height of 2 m, 9 layers

— 171 tubes, 2200 m length

Total heat exchanger area of 84 m²

Pre-distributor

Adjustable liquid distributors, control valves and flow indicators

Approx. 150 m fiber optic, 24 temperature and nine pressure sensors within bundle

Liquid collection and flow metering

Page 6: 3rd Trondheim Gas Technology Conference · 3rd Trondheim Gas Technology Conference COIL WOUND HEAT EXCHANGERS FOR LNG - INVESTIGATION OF TRANSPORT PHENOMENA WITHIN THE BUNDLE Thomas

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Pilot plantVideo CWHE

05.06.2014 TGTC-3 - Coil wound heat exchangers for LNG – Investigation of transport phenomena within the bundle

Page 7: 3rd Trondheim Gas Technology Conference · 3rd Trondheim Gas Technology Conference COIL WOUND HEAT EXCHANGERS FOR LNG - INVESTIGATION OF TRANSPORT PHENOMENA WITHIN THE BUNDLE Thomas

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InnerMiddleOuter

Exemplary resultsDescription

05.06.2014 TGTC-3 - Coil wound heat exchangers for LNG – Investigation of transport phenomena within the bundle

Adjustable liquid distribution above bundle at three sections:

— Inner (layer 1-3, 27 % of total area)

— Middle (layer 4-6, 33 % of total area)

— Outer (layer 7-9, 40 % of total area)

Liquid collectors, at two positions, arranged in same way. Additional collectors at:

— Mandrel

— Shroud

OuterMiddle

Inner

Shroud

Mandrel

Page 8: 3rd Trondheim Gas Technology Conference · 3rd Trondheim Gas Technology Conference COIL WOUND HEAT EXCHANGERS FOR LNG - INVESTIGATION OF TRANSPORT PHENOMENA WITHIN THE BUNDLE Thomas

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Significant change of transport phenomena within bundle

— Increased flow at shroud

— Decreased flow in outer and middle section

— Almost constant flow in inner section and at mandrel

Exemplary resultsLiquid outlet distribution vs. average gas flow

05.06.2014 TGTC-3 - Coil wound heat exchangers for LNG – Investigation of transport phenomena within the bundle

Page 9: 3rd Trondheim Gas Technology Conference · 3rd Trondheim Gas Technology Conference COIL WOUND HEAT EXCHANGERS FOR LNG - INVESTIGATION OF TRANSPORT PHENOMENA WITHIN THE BUNDLE Thomas

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Exemplary results3D-temperature measurements

Increasing transport to outer layer can also be seen by 3D-temperature measurements

05.06.2014 TGTC-3 - Coil wound heat exchangers for LNG – Investigation of transport phenomena within the bundle

Page 10: 3rd Trondheim Gas Technology Conference · 3rd Trondheim Gas Technology Conference COIL WOUND HEAT EXCHANGERS FOR LNG - INVESTIGATION OF TRANSPORT PHENOMENA WITHIN THE BUNDLE Thomas

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Exemplary resultsCell model

05.06.2014 TGTC-3 - Coil wound heat exchangers for LNG – Investigation of transport phenomena within the bundle

A cell model is set-up and adapted to the measured liquid distribution

Determination of the transport coefficient at various conditions.

0,00

0,05

0,10

0,15

0,20

Tran

spor

t Fac

tor [

-]

p hydraulic q hydraulic p thermal q thermal

Gas Flow [t/h]

Page 11: 3rd Trondheim Gas Technology Conference · 3rd Trondheim Gas Technology Conference COIL WOUND HEAT EXCHANGERS FOR LNG - INVESTIGATION OF TRANSPORT PHENOMENA WITHIN THE BUNDLE Thomas

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Outlook

05.06.2014 TGTC-3 - Coil wound heat exchangers for LNG – Investigation of transport phenomena within the bundle

Pilot plant was operated for more than 10 months, over 150 measurements were performed

Results are compared to world-scale plant measurements

Development of empirical correlations not fruitful:

— no homogeneous geometry of bundle

— very complex transport and heat transfer phenomena

Development of heterogeneous 2D CFD model based on OpenFOAM

Verification of 2D CFD model with pilot plant results

Page 12: 3rd Trondheim Gas Technology Conference · 3rd Trondheim Gas Technology Conference COIL WOUND HEAT EXCHANGERS FOR LNG - INVESTIGATION OF TRANSPORT PHENOMENA WITHIN THE BUNDLE Thomas

1205.06.2014 TGTC-3 - Coil wound heat exchangers for LNG – Investigation of transport phenomena within the bundle

Thomas Walter, Christiane Kerber, Konrad Braun, Carsten Richardt, Manfred SteinbauerTrondheim, 05. June 2014

Thank you for your attention!!!