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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
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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
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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
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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
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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
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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
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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
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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
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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
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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]
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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
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!!!