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Lng Liquefaction Cycle
Citation preview
James BronfenbrennerDr. Yu-Nan Liu
Dr.Tamara Daugherty
James BronfenbrennerDr. Yu-Nan Liu
Dr.Tamara Daugherty
LNG Liquefaction CycleEfficiency Analysis
Air Products and Chemicals, Inc.
LNG Liquefaction CycleEfficiency Analysis
Air Products and Chemicals, Inc.
©1998 Air Products and Chemicals, Inc.
Carnot Work
Carnot Cycle Work
Wmin = To ΔS - ΔH
Carnot efficiency W = (To) - (Tr) Q o (To)
COPQr = (Tr) W (To) - (Tr)
Carnot Cycle
Wmin
Entropy
Temp
Temperature-Entropy Diagram
-
-
To
Tr
0
To
Tr δWr
δWr-1
δWr-2
δWr-3
δW1T1
Tr-3
Tr-2
Tr-1
Entropy
T-S DiagramIn
Out0
. . . . . . . . Tem
pera
ture
Minimum work: δW = To δS - δH
Carnot Work Over a Temperature Range
Minimum Work
A
BC
D
E-40
0
40
80
Tem
pera
ture
(C)
Temperature-Entropy Diagram Pure Component System
1
2
Entropy
A
B
CB2
E
C2
D
Temperature-Entropy Diagram Mixed Refrigerant Cycle
-160
-80
0
80
160
Tem
pera
ture
(C)
Entropy
Single MR Cascade Dual MR
Lost Work Components
0%
20%
40%
60%
Lost
Wor
k, %
Tot
al W
ork
Lost
Wor
k, %
Tot
al W
ork
(Incr
easi
ng P
ower
)
(Incr
easi
ng P
ower
)
dP, Mix, Sep
P Letdown
C3 EvapMCHE,C1/C2 Evap.Inter/AfterCoolers
Compress
C3/MR
Compressor Performance Curve
% Volumetric Flow
% H
ead
80
100
120
80 100 120
Surge
100%
105%
95%
Speed
83
Efficiency %8282
80
80
Interstage Cooling/Condensing Issues
Interstage Cooling - More Isothermal Compression
Cp/Cv Ratio N2-1.4; C1-1.3; MR-1.2; C3-1.1
Interstage Condensing - Converts Compression to Pump Power
Heat Exchange Area
Pow
erPower - Area Tradeoff
ΔTmean 0
DISTILLATION
MR TO COMPRESSOR
DRY FEED
MR FROMCOMPRESSOR
Heat Exchange Area
Pow
erMaldistribution
ΔTmean 0
20% Maldistribution
Perfect Mixing
Cycle Efficiency Comparison
Ideal Carnot
C3-MR Dual MR Cascade Single MR0
20
40
60
Effic
ienc
y, %
63
48 48 45 43
•Thermodynamic fundamentals•Sound engineering practices•Defined evaluation criteria
Will produce a meaningfulLNG Liquefaction Cycle
Efficiency Analysis
Air Products and Chemicals, Inc.
•Thermodynamic fundamentals•Sound engineering practices•Defined evaluation criteria
Will produce a meaningfulLNG Liquefaction Cycle
Efficiency Analysis
Air Products and Chemicals, Inc.©1998 Air Products and Chemicals, Inc.