Compact, modular method and apparatus for liquefying natural gas
First Claim
1. A method for liquefying a compressed gas feed stream, the method comprising the steps of:
- a. providing a compressed gas feed stream at a pressure of between about 1500 psig to about 3500 psig and at near ambient temperature;
b. cooling the feed stream to between about −
10°
F. to about −
100°
F.;
c. expanding the cooled feed stream to form a first bi-phase stream comprising a first refrigerated vapor component and a first liquid component;
d. separating the first refrigerated vapor component and the first liquid component;
e. expanding the separated first liquid component to form a second bi-phase stream comprising a second refrigerated vapor component and a second liquid component;
f. separating the second refrigerated vapor component and the second liquid component; and
g. isolating the separated second liquid component to a means configured for storage and transport.
1 Assignment
0 Petitions
Accused Products
Abstract
A compact and modular cryogenic method and apparatus for liquefying natural gas. The liquefaction process is highly efficient and requires no external refrigeration system, and the apparatus is small enough to be transportable from one remote site to another. A compressed natural gas feed stream is cooled and then expanded to form a bi-phase stream comprising a first refrigerated vapor component and a first liquid component. The first liquid component is then separated from the bi-phase stream and expanded to form a second bi-phase stream comprising a second refrigerated vapor component and a second liquid component. The second liquid component is then introduced into a means configured for storage and transport. The remaining feed stream can then be recycled, and at least a substantial portion of the original feed stream can be processed into liquefied natural gas (LNG). The first and second vapor components are recycled through the system and comprise at least a portion of the feed stream in the repeated steps.
70 Citations
20 Claims
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1. A method for liquefying a compressed gas feed stream, the method comprising the steps of:
-
a. providing a compressed gas feed stream at a pressure of between about 1500 psig to about 3500 psig and at near ambient temperature;
b. cooling the feed stream to between about −
10°
F. to about −
100°
F.;
c. expanding the cooled feed stream to form a first bi-phase stream comprising a first refrigerated vapor component and a first liquid component;
d. separating the first refrigerated vapor component and the first liquid component;
e. expanding the separated first liquid component to form a second bi-phase stream comprising a second refrigerated vapor component and a second liquid component;
f. separating the second refrigerated vapor component and the second liquid component; and
g. isolating the separated second liquid component to a means configured for storage and transport. - View Dependent Claims (2, 3, 4, 5, 6, 7)
-
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8. A compact and modular apparatus for refrigerating and liquefying a gas such as pure methane or a natural gas stream rich in methane, the apparatus comprising:
-
a. a means for cooling a compressed main feed stream entering at a pressure between about 1500 psig to about 3500 psig and at near ambient temperature to a temperature of between about −
10°
F. to about −
100°
F.;
b. a turboexpander configured to expand the cooled, compressed feed stream to form a first bi-phase stream comprising a first refrigerated vapor component and a first liquid component;
c. a primary separation tank configured to separate the first refrigerated vapor component and the first liquid component;
d. a means configured to expand the separated first liquid component to form a second bi-phase stream comprising a second refrigerated vapor component and a second liquid component;
e. a secondary separation tank configured to separate the second refrigerated vapor component and the second liquid component; and
f. a means configured for storage and transport of the separated second liquid component. - View Dependent Claims (9, 10, 11, 12, 13, 14)
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15. A compact and modular apparatus for refrigerating and liquefying a gas such as pure methane or a natural gas stream rich in methane, the apparatus comprising:
-
a. a multistage compressor configured for receiving and compressing a main stream gas at a pressure of about 85 psig and at near ambient temperature to a pressure of between about 1500 psig to about 3500 psig;
b. an after-cooler configured to cool the compressed feed stream to near ambient temperature immediately after each compression stage in the multistage compressor;
c. a heat exchanger configured to cool the compressed feed stream to a temperature of between about −
10°
F. to about −
100°
F., typically between about −
20°
F. to about −
60°
F., and more typically about −
30°
F.;
d. a turboexpander configured to expand the compressed and cooled feed stream to a pressure of between about 15 to about 135 psig, typically between about 80 to about 105 psig, and more typically to between about 90 to about 95 psig, to form a first refrigerated vapor component and a first liquid component having a temperature of between about −
155°
F. to about −
240°
F., typically about −
190°
F. to about −
215°
F., and more typically about −
200°
F. to about −
205°
F.;
e. a primary separation tank configured to separate the first refrigerated vapor component and the first liquid component;
f. a throttle valve configured to expand the first liquid component to a pressure of between about 3 psig to about 7 psig, and more typically to about 5 psig to form a second refrigerated vapor component and a second liquid component having a temperature of between about −
250°
F. to −
265°
F., and typically between about −
252°
F. to about −
258°
F.;
g. a secondary separation tank configured to separate the second refrigerated vapor component and the second liquid component;
h. a means configured for storage and transport of the separated second liquid component; and
i. a means to place the separated first refrigerated vapor component and the separated second refrigerated vapor component into fluid communication with the compressed main feed stream. - View Dependent Claims (16, 17, 18, 19, 20)
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Specification