Cryogenic system for removing acid gases from a hydrocarbon gas stream, and method of removing acid gases

Patent metadata

Field	Value
Publication number	US-9423174-B2
Application number	US-201013255219-A
Country	US
Kind code	B2
Filing date	Jan 22, 2010
Priority date	Apr 20, 2009
Publication date	Aug 23, 2016
Grant date	Aug 23, 2016

Abstract

A system for removing acid gases from a raw gas stream the system includes a cryogenic distillation tower. The tower receives and separates the raw gas stream into an overhead methane stream and a bottom liquefied acid gas stream. Refrigeration equipment downstream of the cryogenic distillation tower cools the overhead methane stream and returns a portion of the overhead methane stream to the cryogenic distillation tower as liquid reflux. The system also may include a first molecular sieve bed upstream of the distillation tower and a second molecular sieve bed downstream of the distillation tower. The first molecular sieve bed adsorbs water while the second molecular sieve bed adsorbs additional acid gases from the cooled overhead methane stream.

First claim

What is claimed is:

1. A system for removing acid gases from a raw gas stream, comprising:
a distillation tower for receiving and then separating the raw gas stream into an overhead methane stream and a bottom liquefied acid gas stream;
a first solid adsorbent bed upstream of the distillation tower for at least partially removing a first contaminant from the raw gas stream; and
a second solid adsorbent bed downstream of the distillation tower for adsorbing a least some of a second contaminant from the cooled overhead methane stream,
wherein the second solid adsorbent bed downstream of the distillation tower is a regenerated solid adsorbent bed configured for service as the first solid absorbent bed upstream of the distillation tower when saturated with the second contaminant,

wherein the distillation tower is a cryogenic distillation tower, the system further comprising:
refrigeration equipment downstream of the cryogenic distillation tower for cooling the overhead methane stream and returning a portion of the overhead methane stream to the cryogenic distillation tower as liquid reflux;
wherein the refrigeration equipment generates liquid reflux in a sufficient quantity to remove acid gases from the raw gas stream within the cryogenic distillation tower down to a first selected composition, and delivers the overhead methane stream to the second solid adsorbent bed downstream of the cryogenic distillation tower to remove the remaining acid gases down to a second selected composition.

2. The system of claim 1 , wherein:
the second contaminant is carbon dioxide;
the quantity of the generated liquid reflux is sufficient to remove carbon dioxide from the raw gas stream down to the first composition of about 1 to 4 mol. percent; and
the second solid adsorbent bed downstream of the distillation tower removes additional carbon dioxide from the overhead methane stream down to the second composition of about 0.2 to 3.0 mol. percent.

3. The system of claim 2 , wherein the second contaminant is carbon dioxide, and wherein the second solid adsorbent bed downstream of the cryogenic distillation tower removes carbon dioxide from the overhead methane stream down to a composition less than about 100 ppm.

4. The system of claim 3 , wherein the second contaminant is carbon dioxide, and wherein the second solid adsorbent bed downstream of the cryogenic distillation tower removes carbon dioxide from the overhead methane stream down to a composition less than about 50 ppm.

5. The system of claim 2 , wherein the second solid adsorbent bed downstream of the cryogenic distillation tower is a molecular sieve bed.

6. The system of claim 5 , wherein:
the second contaminant is hydrogen sulfide; and
the molecular sieve bed of the second solid adsorbent bed downstream of the cryogenic distillation tower removes hydrogen sulfide from the overhead methane stream down to a composition less than about 10 ppm.

7. The system of claim 6 , wherein the second contaminant is hydrogen sulfide, and wherein the molecular sieve bed of the second solid adsorbent bed downstream of the cryogenic distillation tower removes hydrogen sulfide from the overhead methane stream down to a composition less than about 4 ppm.

8. The system of claim 5 , wherein:
the first solid adsorbent bed upstream of the cryogenic distillation tower is a molecular sieve bed; and
the system further comprises at least one additional solid adsorbent bed in reserve, wherein the at least one additional solid adsorbent bed in reserve is also a molecular sieve bed.

9. The system of claim 2 , further comprising:
one or more vessels downstream of the cryogenic distillation tower for further separating carbon dioxide from methane using either ionic liquids, physical solvents, or chemical solvents.

10. The system of claim 1 , further comprising a control system for controlling cycle times of the first solid adsorbent bed upstream of the distillation tower.

11. The system of claim 10 , wherein the first contaminant is water, and wherein the control system comprises:
a measurement device for measuring the composition of water in the raw gas stream upstream of the first solid adsorbent bed upstream of the distillation tower; and
a flow meter for measuring the rate of flow of the raw gas stream into the first solid adsorbent bed upstream of the distillation tower.

12. The system of claim 10 , wherein the first contaminant is water, and wherein the control system comprises:
a measurement device for measuring the composition of water of the effluent of the first solid adsorbent bed upstream of the distillation tower; and
the control system is configured to shut off the flow of fluids through the first solid adsorbent bed upstream of the distillation tower when the measurement device senses a predetermined level of water.

13. The system of claim 1 , wherein the second contaminant is carbon dioxide, and wherein:
a quantity of the generated liquid reflux is sufficient to remove carbon dioxide from the raw gas stream down to a first composition that meets a pipeline specification; and
the second solid adsorbent bed downstream of the cryogenic distillation tower removes carbon dioxide from the overhead methane stream down to the second selected acid gas composition that meets an LNG specification.

14. The system of claim 1 , wherein the refrigeration equipment comprises an open loop refrigeration system.

15. The system of claim 1 , wherein the refrigeration equipment comprises a closed loop refrigeration system.

16. The system of claim 1 , wherein:
the raw gas stream further comprises nitrogen; and
the system further comprises a third solid adsorbent bed downstream of the distillation tower for adsorbing at least some nitrogen from the cooled overhead methane stream.

17. A method for removing acid gases from a raw gas stream, comprising:
providing a cryogenic distillation tower, the tower having a lower distillation zone and an intermediate controlled freezing zone that receives a cold liquid spray comprised primarily of methane;
receiving the raw gas stream into the cryogenic distillation tower;
separating the raw gas stream in the cryogenic distillation tower into an overhead methane stream and a bottom acid gas stream;
passing the overhead methane stream through a refrigeration system downstream of the cryogenic distillation tower, the refrigeration system cooling the overhead methane stream;
returning a first portion of the cooled overhead methane stream to the cryogenic distillation tower as liquid reflux to serve as the cold liquid spray;
passing a second portion of the cooled overhead methane stream through a first solid adsorbent bed downstream of the cryogenic distillation tower so as to remove additional acid gases comprising a first contaminant and to generate a polished gas stream;
producing, with the refrigeration system, the liquid reflux at a sufficient quantity as to remove acid gases from the raw gas stream within the cryogenic distillation tower down to a first selected composition, and delivering the overhead methane stream to the first solid adsorbent bed downstream of the cryogenic distillation tower to remove additional acid gases down to a second selected composition;
at least partially dehydrating the raw gas stream by passing the raw gas stream through a second solid adsorbent bed upstream of the cryogenic distillation tower to remove a second contaminant, wherein the first solid adsorbent bed downstream of the cryogenic distillation tower and the second solid adsorbent bed upstream of the cryogenic distil

Assignees

• Northrop Paul Scott
• Kelley Bruce T
• Mart Charles J
• Exxonmobil Upstream Res Co

Inventors

• Northrop Paul Scott
• Kelley Bruce T
• Mart Charles J

Classifications

• F25J2205/64

  by pressure-swing adsorption [PSA] at the hot end · CPC title

• F25J2205/60

  using adsorption on solid adsorbents, e.g. by temperature-swing adsorption [TSA] at the hot or cold end · CPC title

• B01D53/0423

  Beds in columns · CPC title

• F25J2280/40

  Control of freezing of components · CPC title

• F25J2220/80

  Separating impurities from carbon dioxide, e.g. H2O or water-soluble contaminants · CPC title