IP Library Granted Patent US 11,339,339
Granted Patent B1
US 11,339,339 · App. 17/024,456 · Granted May 24, 2022

Condensate stabilization process

Inventors: Mehdi Nouri (Houston, TX); Eberhard Lucke (Houston, TX)
C10L3/103B01D53/02B01D53/261C10L3/101C10L3/104F25J1/0022F25J3/0214F25J3/0295B01D2253/116B01D2256/24B01D2257/304B01D2257/306B01D2257/504B01D2257/602B01D2257/80
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Quick Facts
Patent No.
US 11,339,339
App. No.
17/024,456
Granted
May 24, 2022
Kind
B1
Abstract

A natural gas processing system is configured to process a two-phase flow in a natural gas transportation system. The natural gas processing system has an off-gas compression package with a compressor suction drum, joined to a stabilizer and to a first stage compressor. A first stage off-gas after cooler is joined to the compressor suction drum and a second stage off-gas suction drum. The second stage off-gas suction drum is operatively coupled to a two-phase separator. A second stage compressor is joined to the second stage off-gas suction drum and a second stage off-gas after cooler. The second stage off-gas after cooler is operatively coupled to an acid gas removal system. The off-gas compression package separates the liquid phase from an off-gas phase.

Claims (13)

1. A natural gas processing system configured to process a two-phase flow in a natural gas transportation system; the natural gas processing system comprising:

a slug catcher, operatively connected to the two-phase flow, an acid gas removal system and a feed preheater,

a two-phase separator, joined to the feed preheater, a cross exchanger, and an off-gas compression package;

a stabilizer, joined to the cross exchanger, a reboiler, and the off-gas compression package;

wherein the off-gas compression package further comprises:

a compressor suction drum, joined to the stabilizer and to a first stage compressor;

a first stage off-gas after cooler, joined to the compressor suction drum and a second stage off-gas suction drum; wherein the second stage off-gas suction drum is operatively coupled to the two-phase separator; and

a second stage compressor, joined to the second stage off-gas suction drum and a second stage off-gas after cooler; wherein the second stage off-gas after cooler is operatively coupled to an acid gas removal system;

wherein the off-gas compression separates the liquid phase from an off-gas phase.

2. The natural gas processing system of claim 1 , wherein the acid gas removal system further comprises: a mol sieve dehydration stage operatively coupled to an acid gas removal stage and a mercury removal stage; wherein the acid gas removal stage removes hydrogen sulfide, carbon dioxide and mercaptans from the off-gas phase; wherein the mol sieve dehydration stage removes water from the off-gas phase.

3. The natural gas processing system of claim 2 , wherein the acid gas removal system further comprises a mercury removal stage, operatively connected to the mol sieve dehydration stage and a C2+ recovery stage; wherein the mercury removal stage removes mercury from the off gas.

4. The natural gas processing system of claim 3 , wherein the acid gas removal system further comprises a C2/C3 separation stage, operatively coupled to the C2+ recovery stage and a C3/C4 separation stage; wherein the C2/C3 separation stage removes ethane from the off gas and the C3/C4 separation stage removes propane from the off gas.

5. The natural gas processing system of claim 4 , wherein the acid gas removal system further comprises a C4/C5 separation stage, operatively coupled to the C3/C4 separation stage and the storage tank; wherein the C4/C5 separation stage removes butane from the off-gas resulting in a condensate that is transferred to the storage tank.

Cited By (2)
US 12,521,729 US 12,703,831