Purification of gas with liquid ionic compounds

• US 6,579,343 B2
• Filed: 04/01/2002
• Issued: 06/17/2003
• Est. Priority Date: 03/30/2001
• Status: Expired due to Term

• Current Assignee: University of Notre DAME Du Lac
• Original Assignee: University of Notre DAME Du Lac
• Inventors: Brennecke, Joan F., Maginn, Edward J.
• Primary Examiner(s): Spitzer, Robert H.
• Application Number:
  US10/113,400
• Publication Number:
  US 20020189444A1
• Time in Patent Office: 442 Days
• Field of Search: 95/444.5, 95/50--52, 95/54, 952/30, 952/31, 952/36, 952/37, 96/45
• US Class Current: 95/51
• CPC Class Codes: B01D 53/1493 Selection of liquid materials for use as absorbents

Abstract

The present invention provides a method for purifying a gas by contacting the gas with a liquid ionic compound. Natural gas may be purified, removing water and carbon dioxide, by contacting the natural gas with a liquid ionic compound.

Claims

1. A method for separating a gas from a gaseous mixture, comprising the step of contacting the gaseous mixture with a liquid ionic compound, said liquid ionic compound comprising a nitrogen-containing heterocyclic cation.

2. The method of claim 1 wherein the liquid ionic compound comprises a compound selected from the group consisting of:

(a) a compound of the formula

 

where;

R¹ is hydrogen or C₁-C₁₈ alkyl;

A is —

O—

, —

S—

, or —

N(R⁴)—

;

B is —

N—

or —

C(R⁵)—

;

R², R³, R⁴, and R⁵ are independently hydrogen, C₁-C₆ alkyl, C₂-C₆ alkenyl, C₃-C₆ cycloalkyl, C₃-C₈ cycloalkenyl, aryl, substituted aryl, aryl(C₁-C₄ alkyl), or substituted aryl(C₁-C₄ alkyl); and

X is an anion selected from the group consisting of hydroxide, chloride, bromide, iodide, borate, tetrafluoroborate, cuprate, Cu(I)Cl₂ anion, phosphate, hexafluorophosphate, hexafluoroantimonate, perchlorate, nitrite, nitrate, sulfate, a carboxylate, a sulfonate, a sulfonimide, and a phosphonate; and

,

n is an integer from 1 to 4; and

(b) a compound of the formula

 

where;

R¹ is as defined above;

A is as defined above;

B is as defined above;

R² is as defined above;

R⁶ is hydrogen, C₁-C₆ alkyl, C₂-C₆ alkenyl, C₃-C₆ cycloalkyl, C₃-C₈ cycloalkenyl, aryl, substituted aryl, aryl(C₁-C₄ alkyl), or substituted aryl(C₁-C₄ alkyl);

X is as defined above; and

,

n is as defined above; and

(c) a compound of the formula

 

where;

R¹ is as defined above;

U, V, and W are independently —

N—

or —

C(R⁹)—

, provided that U and V are not simultaneously —

N—

;

R⁷, R⁸, and R⁹ are independently hydrogen, C₁-C₆ alkyl, C₂-C₆ alkenyl, C₃-C₆ cycloalkyl, C₃-C₈ cycloalkenyl, aryl, substituted aryl, aryl(C₁-C₄ alkyl), or substituted aryl(C₁-C₄ alkyl);

X is as defined above; and

,

n is as defined above.

3. The method of claim 1 wherein the liquid ionic compound is a compound selected from the group consisting of imidazolium salts, pyrazolium salts, oxazolium salts, thiazolium salts, triazolium salts, pyridinium salts, pyridazinium salts, pyrimidinium salts, and pyrazinium salts.

4. The method of claim 1 wherein the liquid ionic compound is selected from the group consisting of 1-ethyl-3-methylimidazolium chloride, 1-butyl-3-ethylimidazolium chloride, 1-butyl-3-methylimidazolium chloride, 1-butyl-3-methylimidazolium bromide, 1-methyl-3-propylimidazolium chloride, 1-methyl-3-hexylimidazolium chloride, 1-methyl-3-octylimidazolium chloride, 1-methyl-3-decylimidazolium chloride, 1-methyl-3-dodecylimidazolium chloride, 1-methyl-3-hexadecylimidazolium chloride, 1-methyl-3-octadecylimidazolium chloride, 1-ethylpyridinium bromide, 1-ethylpyridinium chloride, 1-butylpyridinium chloride, and 1-benzylpyridinium bromide, 1-butyl-3-methylimidazolium tetrafluoroborate, 1-butyl-3-methylimidazolium iodide, 1-butyl-3-methylimidazolium nitrate, 1-ethyl-3-methylimidazolium tetrafluoroborate, 1-ethyl-3-methylimidazolium bromide, 1-ethyl-3-methylimidazolium iodide, 1-ethyl-3-methylimidazolium nitrate, 1-butylpyridinium tetrafluoroborate, 1-butylpyridinium bromide, 1-butylpyridinium iodide, 1-butylpyridinium nitrate, 1-butyl-3-methylimidazolium hexafluorophosphate, 1-octyl-3-methylimidazolium hexafluorophosphate, 1-octyl-3-methylimidazolium tetrafluoroborate, 1-ethyl-3-methylimidazolium ethylsulfate, 1-butyl-3-methylimidazolium triflate, 1-butyl-3-methylimidazolium acetate, 1-butyl-3-methylimidazolium trifluoroacetate, and 1-butyl-3-methylimidazolium bis(trifluoromethanesulfonimide).

5. The method of claim 1 wherein the liquid ionic compound is selected from the group consisting of 1-butyl-3-methylimidazolium hexafluorophosphate, 1-octyl-3-methylimidazolium hexafluorophosphate, 1-butyl-3-methylimidazolium nitrate, 1-octyl-3-methylimidazolium tetrafluoroborate, 1-ethyl-3-methylimidazolium ethylsulfate, N-butylpyridinium tetrafluoroborate, 1-butyl-3-methylimidazolium triflate, 1-butyl-3-methylimidazolium acetate, 1-butyl-3-methylimidazolium trifluoroacetate, and 1-butyl-3-methylimidazolium bis(trifluoromethanesulfonimide).

6. The method of claim 1 wherein the liquid ionic compound is provided as a supported liquid membrane.

7. The method of claim 6 wherein the gaseous mixture comprises carbon dioxide and nitrogen, the gas is nitrogen, and wherein carbon dioxide selectively diffuses through the supported liquid membrane.

8. The method of claim 7 wherein the carbon dioxide that diffuses through the supported liquid membrane is substantially free of nitrogen.

9. The method of claim 6 wherein the supported liquid membrane comprises a first side and a second side, the contacting step comprises contacting the first side of the membrane with the gaseous mixture, and wherein impurities diffuse to the second side of the membrane.

10. The method of claim 6, wherein the supported liquid membrane comprises a first side and a second side, the contacting step comprises contacting the first side with the gaseous mixture such that the gas diffuses to the second side of the membrane, and further comprising the step of collecting the gas that diffuses to the second side of the membrane.

11. The method of claim 6 wherein the gas and an impurity in the gaseous mixture have a ratio of Henry'"'"'s law constants for the liquid ionic compound of at least 20.

12. The method of claim 11 further comprising the step of adjusting the temperature of the liquid ionic compound to increase the ratio and improve separation efficiency.

13. The method of claim 6 wherein the gaseous mixture comprises an alkane and an olefin, and the alkane and olefin have a ratio of Henry'"'"'s law constants for the liquid ionic compound of at least 2.0.

14. The method of claim 6 wherein the gaseous mixture comprises an alkane and an olefin, and the alkane and olefin have a ratio of Henry'"'"'s law constants for the ionic compound of at least 1.7.

15. The method of claim 1 wherein the liquid ionic compound is substantially free of water.

16. The method of claim 1 wherein the gaseous mixture is selected from the group consisting of natural gas and air.

17. The method of claim 1 wherein the gaseous mixture includes carbon dioxide as an impurity and carbon dioxide is removed from the gaseous mixture.

18. The method of claim 1 wherein the gaseous mixture includes water and water is removed from the gaseous mixture.

19. The method of claim 1 wherein the gaseous mixture includes both water and carbon dioxide and the method comprises decreasing the amount of carbon dioxide and water in the gaseous mixture.

20. The method of claim 1 wherein the liquid ionic compound is provided in a fixed bed and the contacting step comprises flowing the gaseous mixture into the fixed bed.

21. The method of claim 20 wherein the liquid ionic compound is coated on the surface of a solid particulate substrate within the fixed bed.

22. The method of claim 20 wherein the gaseous mixture is flowed continuously through the fixed bed.

23. The method of claim 20 wherein the gaseous mixture is held in contact with the fixed bed for a prescribed residence time.

24. The method of claim 20 wherein the gas is retained within the fixed bed and impurities are allowed to flow out of the fixed bed.

25. The method of claim 20 wherein impurities are retained within the fixed bed and the gas is collected as the gas flows out of the fixed bed.

26. The method of claim 20 wherein the gas and an impurity within the gaseous mixture have a ratio of Henry'"'"'s law constants for the liquid ionic compound of at least 17.

27. The method of claim 26 further comprising the step of adjusting the temperature of the liquid ionic compound to increase the effective ratio.

28. The method of claim 1 further comprising the step of contacting the gaseous mixture with a second liquid ionic compound, said second liquid ionic compound comprising a nitrogen-containing heterocyclic cation.

29. The method of claim 28 wherein the first and second liquid ionic compounds are intermixed, and the steps of contacting the gaseous mixture with the liquid ionic compound and contacting the gaseous mixture with the second liquid ionic compound are performed at the same time.

30. The method of claim 1 wherein the gas is purified to be essentially free of one or more impurities present in the gaseous mixture.