Absorption process with solvent pre-saturation

• US 5,687,584 A
• Filed: 08/30/1996
• Issued: 11/18/1997
• Est. Priority Date: 10/27/1995
• Status: Expired due to Term

• Current Assignee: Aet Partners, LLC
• Original Assignee: Advanced Extraction Technologies, Inc.
• Inventors: Mehra, Yuv R.
• Primary Examiner(s): Capossela, Ronald C.
• Application Number:
  US08/697,829
• Time in Patent Office: 445 Days
• Field of Search: 62/625, 62/632, 62/635, 62/938
• US Class Current: 62/632
• CPC Class Codes: B01D 53/1487 Removing organic compounds
• CPC Class Codes: C10G 5/04 with liquid absorbents
• CPC Class Codes: F25J 2200/04 in a dual pressure main column system
• CPC Class Codes: F25J 2205/50 using absorption, i.e. with selective solvents or lean oil, heavier CnHm and including generally a regeneration step for the solvent or lean oil
• CPC Class Codes: F25J 2215/62 Ethane or ethylene
• CPC Class Codes: F25J 2215/64 Propane or propylene
• CPC Class Codes: F25J 2215/66 Butane or mixed butanes
• CPC Class Codes: F25J 2230/08 Cold compressor, i.e. suction of the gas at cryogenic temperature and generally without afterstage-cooler
• CPC Class Codes: F25J 2230/60 the fluid being hydrocarbons or a mixture of hydrocarbons
• CPC Class Codes: F25J 2245/02 Recycle of a stream in general, e.g. a by-pass stream
• CPC Class Codes: F25J 2290/80 Retrofitting, revamping or debottlenecking of existing plant
• CPC Class Codes: F25J 3/0209 Natural gas or substitute natural gas
• CPC Class Codes: F25J 3/0233 separation of CnHm with 1 carbon atom or more
• CPC Class Codes: F25J 3/0238 separation of CnHm with 2 carbon atoms or more
• CPC Class Codes: F25J 3/0242 separation of CnHm with 3 carbon atoms or more

Abstract

A retro fitted unit to an existing simple refrigerated natural gas plant that substantially increases the amounts of propane, butanes and natural gasoline, or ethane, propane, butanes and natural gasoline recovered from the natural gas in the existing gas treatment plant, wherein in one embodiment the existing natural gas treatment plant includes a refrigerated feed cooler, a separator and a stabilizer and the retrofitted unit comprises an NGL absorber, a refrigerated lean solvent cooler and a lean solvent regenerator; and wherein in a second embodiment the existing simple refrigerated gas treatment plant additionally includes an NGL fractionation train that separates the recovered NGL into saleable fractions and wherein the NGL fractionation train includes a debutanizer that produces all or part of the lean solvent utilized in the retrofitted unit which comprises an NGL absorber and a refrigerated solvent cooler; and wherein the natural gas treatment process utilizes a solvent that is pre-saturated with lighter undesirable components present in the overhead stream from the NGL absorber.

Claims

1. In an absorption process for recovery of a desired component and all components heavier than the desired component from a feed gas stream containing components of varying degrees of volatility'"'"'s wherein the feed gas stream is counter-currently contacted in an absorber column with a lean solvent stream comprised of the heaviest components present in the feed gas stream to produce an overhead stream having lighter undesired components, the improvement comprising pre-saturating the lean solvent with the lighter undesired components of the feed gas stream obtained from the overhead stream of the absorber column.

2. The process of claim 1 wherein the feed gas stream is a natural gas.

3. The process of claim 2 wherein the desired component is propane and the undesired component is ethane.

4. The process of claim 2 wherein the desired component is ethane and the undesired component is methane.

5. The process of claim 2 wherein the lean solvent is comprised of C₅ +components present in the feed gas stream.

6. The process of claim 1 wherein the absorber column is reboiled at the bottom.

7. The process of claim 6 wherein the absorber column is a dual pressure column consisting of a high pressure absorption section and a low pressure stripping section which is reboiled at the bottom.

8. The process of claim 1 wherein the desired component is propane and the undesired component is ethane.

9. The process of claim 1 wherein the desired component is ethane and the undesired component is methane.

10. The process of claim 1 wherein the lean solvent is comprised of C₅ +components present in the feed gas stream.