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TG&T Plant Operator Training Class IV Refrigeration Update 11-09
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DRAWING 05A
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332 MMCFD 976 psig 120 F 8 gpm 110 F 10 gpm 956 psig 328 MMCFD -30 F 328.7 MMCFD 39 GPM HC 13 GPM EG/Water 1.2 MMCFD 980 psig 120 F 77% C1 9% C2 6% C3 2% C4+
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GAS/GAS EXCHANGERS DRAWING 05A EG Injection Exchange heat between Warm Treated Gas from sweetening and Cold Treated Gas from Cold Separator yields Dry Gas to Sales Ethylene Glycol injected into Wet Treated Gas upstream of exchangers and directly into the head at the tube sheet
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2 DRAWING 05B
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2 Wet Treated Gas in the tube side. Refrigerant Propane in the shell side EG injected into Wet Treated Gas upstream of Chiller inlet and directly into the head at the tube sheet
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3 DRAWING 05B LIC-4432 operates LV-4432 to maintain a sufficient level to keep the tubes covered LV-4432
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4 DRAWING 05B Refrigerant Reclaimer removes unwanted refrigerant components. Heavier contaminants drain off the bottom of the chiller into the Reclaimer where Hot Oil flashes the propane out and into the Compressor vapor return line. Contaminants drain to a sump.
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5 DRAWING 05B
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5 Three phase separator (SEE ILLUSTRATION)
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DRAWING 05B 5
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CONDENSATE STABILIZATION
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DRAWING 05B 5
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6 DRAWING 06
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8 DRAWING 07
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ETHYLENE GLYCOL REGENERATION
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9 DRAWING 05B
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9 ACID GAS COOLER
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9 DRAWING 15
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10 DRAWING 18B
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12 DRAWING 18A
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14 DRAWING 18B
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REFRIGERATION LOOP
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2 DRAWING 05B
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15 DRAWING 08
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16 DRAWINGS 09A & 09B
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16 DRAWINGS 09A & 09B 4-1250 HP 2 stage compressors capable of moving 4.4MMSCFD of propane each at 210 psig
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17 DRAWING 09B
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17 2-50 HP fans for each bay 3 bays total Duty; 16,300 MBTU each bay
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18 DRAWING 10
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18 Acts like a Refrigerant Surge Tank Level is maintained manually by adding Refrigerant Propane to the Chiller Refrigerant inlet line from the Refrigerant Storage Tank
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19 DRAWING 08
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