US2004148962A1PendingUtilityA1
Gas liquefaction method using natural gas and mixed gas refrigeration
Priority: Feb 4, 2003Filed: Nov 7, 2003Published: Aug 5, 2004
Est. expiryFeb 4, 2023(expired)· nominal 20-yr term from priority
Inventors:M. Abdul-Aziz RashadRichard FitzgeraldDante Patrick BonaquistJohn B. SaundersMinish Mahendra Shah
F25J 1/0057F25J 1/001F25J 1/0212F25J 1/0022F25J 1/005F25J 1/0015F25J 1/0007F25J 2230/60F25J 2220/62F25J 2210/06F25J 2205/66F25J 1/0017F25J 1/0281F25J 1/0097F25J 1/002F25J 2270/12F25J 2270/06F25J 2215/32F25J 1/0045F25J 1/0219F25J 1/0285F25J 1/0052F25J 1/0221F25J 2230/08F25J 2230/30F25J 2220/64F25J 2270/14F25J 1/004F25J 1/0005F25J 2210/60F25J 1/0037F25J 1/0232
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Claims
Abstract
A gas liquefaction method which uses the pressure energy of a natural gas processing system to generate refrigeration for high temperature cooling of a gas, and uses a mixed gas refrigerant fluid to generate refrigeration for low temperature cooling of the gas to produce liquefied product.
Claims
exact text as granted — not AI-modified1 . A method for producing liquefied natural gas comprising:
(A) cooling a first natural gas stream to produce first cooled natural gas, and expanding the first cooled natural gas to produce refrigeration bearing natural gas; (B) cooling a second natural gas stream by indirect heat exchange with the refrigeration bearing natural gas to produce second cooled natural gas; (C) compressing a mixed refrigerant fluid, cooling the compressed mixed refrigerant fluid, and expanding the cooled mixed refrigerant fluid to produce refrigeration bearing mixed refrigerant fluid; (D) warming the refrigeration bearing mixed refrigerant fluid by indirect heat exchange with the cooling compressed mixed refrigerant fluid and by indirect heat exchange with second cooled natural gas to condense at least some of the second cooled natural gas; and (E) recovering resulting condensed natural gas as product liquefied natural gas.
2 . The method of claim 1 wherein both the first natural gas stream and the second natural gas stream are taken from a natural gas pipeline.
3 . The method of claim 1 wherein the cooling of the first natural gas stream produces a vapor and a liquid fraction, and the vapor fraction is expanded to produce the refrigeration bearing natural gas.
4 . The method of claim 3 wherein the liquid fraction is vaporized and then recovered.
5 . The method of claim 1 wherein at least some of the power for compressing the mixed refrigerant fluid is provided from expanding the first cooled natural gas to produce the refrigeration bearing natural gas.
6 . The method of claim 1 wherein the second natural gas stream undergoes a carbon dioxide removal step prior to said cooling.
7 . The method of claim 1 wherein a portion of the second cooled natural gas is turboexpanded and then warmed to provide some cooling for at least one of the first natural gas stream, the second natural gas stream and the compressed mixed refrigerant fluid.
8 . The method of claim 7 wherein some of the power for compressing the mixed refrigerant fluid is provided by the turboexpansion of the second cooled natural gas portion.
9 . A method for producing liquefied industrial gas comprising:
(A) cooling a natural gas stream to produce cooled natural gas, and expanding the cooled natural gas to produce refrigeration bearing natural gas; (B) cooling an industrial gas stream by indirect heat exchange with the refrigeration bearing natural gas to produce cooled industrial gas; (C) compressing a mixed refrigerant fluid, cooling the compressed mixed refrigerant fluid, and expanding the cooled mixed refrigerant fluid to produce refrigeration bearing mixed refrigerant fluid; (D) warming the refrigeration bearing mixed refrigerant fluid by indirect heat exchange with the cooling compressed mixed refrigerant fluid and by indirect heat exchange with cooled industrial gas to condense at least some of the cooled industrial gas; and (E) recovering resulting condensed industrial gas as product liquefied industrial gas.
10 . The method of claim 9 wherein the cooling of the natural gas stream produces a vapor and a liquid fraction, the vapor fraction is expanded to produce the refrigeration bearing natural gas, and the liquid fraction is vaporized and recovered.
11 . The method of claim 9 wherein at least some of the power for compressing the mixed refrigerant fluid is provided from expanding the cooled natural gas to produce the refrigeration bearing natural gas.
12 . The method of claim 9 wherein the industrial gas is compressed prior to being cooled and at least some of the power for compressing the industrial gas is provided by the expansion of the cooled mixed refrigerant fluid to produce refrigeration bearing mixed refrigerant fluid.
13 . The method of claim 9 wherein the industrial gas comprises nitrogen.Join the waitlist — get patent alerts
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