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[object Object]
[object Object],[object Object],[object Object],INTRODUCTION
[object Object],[object Object],[object Object],INTRODUCTION
GAS COMPOSITION ,[object Object],[object Object]
[object Object],[object Object],GAS COMPOSITION
[object Object],[object Object],[object Object],LIQUID RECOVERY
[object Object],[object Object],[object Object],LIQUID RECOVERY
[object Object],[object Object],LIQUID RECOVERY
[object Object],[object Object],LIQUID RECOVERY
PROBLEM ,[object Object],[object Object],[object Object],[object Object]
Component Feed gas composition Mole % Gal / mole HHV Btu/scf N 2 CO 2 C 1 C 2 C 3 i-C 4 n-C 4 i-C 5 n-C 5 C 6+ 1.0 3.0 85 5.8 3.0 0.7 0.8 0.2 0.3 0.2 6.4532 4.1513 6.4172 10.126 10.433 12.386 11.937 13.860 13.713 15.566 0 0 1010 1769.6 2516.1 3262.3 3251.9 4008.9 4000.9 4755.9
GPM CALCULATIONS
HHV CALCULATIONS
Shrinkage Value  =  [(330 * 1115.01) – (295.862 * 971.24)]*2  = $161,201/day SHRINKAGE CALCULATIONS
[object Object],[object Object],DEW POINT CONTROL
DEW POINT CONTROL ,[object Object],[object Object],[object Object],[object Object]
 
REDUCTION  OF  HYDROCARBON   DEW POINT ,[object Object],[object Object],[object Object]
LOW TEMPERATURE SEPARATION ,[object Object],[object Object],[object Object]
[object Object],[object Object],[object Object],[object Object],LOW TEMPERATURE SEPARATION
[object Object],[object Object],LOW TEMPERATURE SEPARATION
LOW-TEMPERATURE SEPARATION SYSTEM WITH  GLYCOL INJECTION AND CONDENSATE STABILIZATION
STRAIGHT REFRIGERATION PROCESS ,[object Object],[object Object],[object Object]
STRAIGHT REFRIGERATION PROCESS
[object Object],[object Object],[object Object],[object Object],STRAIGHT REFRIGERATION PROCESS
[object Object],[object Object],[object Object],[object Object],STRAIGHT REFRIGERATION PROCESS
[object Object],[object Object],STRAIGHT REFRIGERATION PROCESS
 
 
 
PROCESS ALTERNATIVES ,[object Object],[object Object],[object Object],[object Object],[object Object]
Type “A”
[object Object],[object Object],[object Object],[object Object],TYPE “A”
[object Object],[object Object],[object Object],[object Object],TYPE “A”
Type “B”
[object Object],[object Object],[object Object],[object Object],[object Object],Type “B”
Type “C”
[object Object],[object Object],Type “C”
[object Object],[object Object],[object Object],[object Object],[object Object],Type  “B”  & “C”
Type “D”
[object Object],[object Object],[object Object],[object Object],Type “D”
STABILIZATION ,[object Object],[object Object],[object Object]
[object Object],[object Object],[object Object],STABILIZATION
[object Object],[object Object],[object Object],LEAN OIL ABSORPTION
[object Object],[object Object],[object Object],REFRIGERATED LEAN OIL ABSORPTION
REFRIGERATED LEAN OIL ABSORPTION
[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],REFRIGERATED LEAN OIL ABSORPTION
[object Object],[object Object],[object Object],[object Object],REFRIGERATED LEAN OIL ABSORPTION
[object Object],[object Object],REFRIGERATED LEAN OIL ABSORPTION
ETHANE RECOVERY ,[object Object],[object Object],[object Object],[object Object]
 
 
[object Object],[object Object],[object Object],[object Object],[object Object],METHODS OF ETHANE RECOVERY
J-T EXPANSION PROCESS ,[object Object],[object Object],[object Object]
[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],J-T EXPANSION PROCESS
J-T EXPANSION PROCESS
[object Object],[object Object],[object Object],[object Object],[object Object],J-T EXPANSION PROCESS
[object Object],[object Object],[object Object],REFRIGERATED J-T PROCESS
REFRIGERATED J-T PROCESS
[object Object],[object Object],[object Object],[object Object],REFRIGERATED J-T PROCESS
TURBOEXPANDER PROCESS ,[object Object],[object Object],[object Object]
TURBOEXPANDER PROCESS
[object Object],[object Object],[object Object],[object Object],TURBOEXPANDER PROCESS
[object Object],[object Object],[object Object],[object Object],TURBOEXPANDER PROCESS
[object Object],[object Object],[object Object],[object Object],[object Object],TURBOEXPANDER PROCESS
RESIDUE RECYCLE ,[object Object],[object Object]
RESIDUE RECYCLE
[object Object],[object Object],[object Object],[object Object],RESIDUE RECYCLE
[object Object],[object Object],[object Object],[object Object],RESIDUE RECYCLE
GAS SUBCOOLED PROCESS
[object Object],[object Object],[object Object],GAS SUBCOOLED PROCESS
[object Object],[object Object],[object Object],[object Object],GAS SUBCOOLED PROCESS
[object Object],[object Object],[object Object],GAS SUBCOOLED PROCESS
[object Object],[object Object],GAS SUBCOOLED PROCESS
[object Object],[object Object],[object Object],COLD RESIDUE RECYCLE (CRR) PROCESS
CRR PROCESS
[object Object],[object Object],[object Object],[object Object],CRR PROCESS
SIDE DRAW REFLUX (SDR) PROCESS ,[object Object],[object Object],[object Object],[object Object]
SIDE DRAW REFLUX (SDR) PROCESS
[object Object],SIDE DRAW REFLUX (SDR) PROCESS
[object Object],[object Object],[object Object],[object Object],MIXED  REFRIGERANT  PROCESS
MIXED REFRIGERANT PROCESS
[object Object],[object Object],[object Object],[object Object],MIXED REFRIGERANT PROCESS
[object Object],[object Object],[object Object],MIXED REFRIGERANT PROCESS
[object Object],[object Object],[object Object],[object Object],FRACTIONATION CONSIDERATIONS
[object Object],[object Object],[object Object],[object Object],FRACTIONATION CONSIDERATIONS
FRACTIONATION CONSIDERATIONS

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