Method and apparatus for cooling a hydrocarbon stream
Abstract
A method of cooling a hydrocarbon stream such as natural gas, the method at least comprising the steps of: (a) providing a feed stream; (b) passing the feed stream through a gas treatment stage comprising one or more (number: X) parallel gas treatment units, the feed stream being divided into two or more part-feed streams if there is more than one gas treatment unit, to provide one or more first treated streams; (c) passing the first treated stream or streams of step (b) through an NGL extraction stage comprising one or more (number: Y) parallel NGL extraction units, the first treated stream or streams being shared to match the number of NGL extraction units, to provide one or more second treated streams; and (d) passing the second treated stream or streams of step (c) through a cooling stage comprising one or more (number: Z) parallel cooling systems, the second treated stream or streams being shared to match the number of cooling systems, to provide a cooled hydrocarbon stream or streams.
Claims
exact text as granted — not AI-modified1 . Method of cooling a hydrocarbon stream such as natural gas, the method at least comprising the steps of:
(a) providing a feed stream; (b) passing the feed stream through a gas treatment stage comprising one or more (number: X) parallel gas treatment units, the feed stream being divided into two or more part-feed streams if there is more than one gas treatment unit, to provide one or more first treated streams; (c) passing the first treated stream or streams of step (b) through an NGL extraction stage comprising one or more (number: Y) parallel NGL extraction units, the first treated stream or streams being shared to match the number of NGL extraction units, to provide one or more second treated streams; and (d) passing the second treated stream or streams of step (c) through a cooling stage comprising one or more (number: Z) parallel cooling systems, the second treated stream or streams being shared to match the number of cooling systems, to provide a cooled hydrocarbon stream or streams; wherein Y>Z.
2 . Method as claimed in claim 1 , wherein the feed stream is divided into two part-feed streams, and X is 2 and Z is 1.
3 . Method as claimed in claim 1 , wherein Y is 2 and Z is 1.
4 . Method as claimed in claim 1 , wherein the feed stream is divided into three part-feed streams, and X is 3 and Z is 1 or 2.
5 . Method as claimed in claim 1 , wherein Y is 3 and Z is 1 or 2.
6 . Method according to claim 1 , wherein the or each NGL extraction unit provides a second treated stream and one or more separate streams.
7 . Method as claimed in claim 6 , wherein the one or more separate streams comprise one or more of a propane stream, a butane stream and a C 5 + stream.
8 . Method as claimed in claim 6 , wherein the one or more separate streams are fractionated to provide one or more fractionated streams.
9 . Method as claimed in claim 7 , wherein the one or more fractionated streams comprise one or more of a propane stream, a butane stream and a C 5 + stream.
10 . Method according to claim 1 , wherein X is different from Z.
11 . Method according to claim 1 , wherein the cooling step (d) liquefies the second treated stream or streams to provide a liquefied hydrocarbon stream or streams.
12 . Liquefied hydrocarbons comprising the liquefied hydrocarbon stream obtained from the method of claim 11 .
13 . Apparatus for cooling a hydrocarbon stream such as natural gas, the apparatus at least comprising:
(i) a gas treatment stage to receive a feed stream comprising one or more (number: X) parallel gas treatment units, the feed stream being divided if there is more than one gas treatment unit; (ii) an NGL extraction stage to receive the treated feed stream or streams from the gas treatment stage, comprising one or more (number: Y) parallel NGL extraction units; and (iii) a cooling stage to receive the NGL extracted stream or streams from the NGL extraction stage, comprising one or more (number: Z) parallel cooling systems to provide a treated hydrocarbon stream or streams; wherein Y>Z.
14 . Apparatus as claimed in claim 13 , wherein X is 2 and Z is 1.
15 . Apparatus as claimed in claim 13 , wherein Y is 2 and Z is 1.
16 . Apparatus as claimed in claim 13 , wherein X is 3 and Z is 1 or 2.
17 . Apparatus as claimed in claim 13 , wherein Y is 3 and Z is 1 or 2.
18 . Apparatus as claimed in claim 13 , further comprising a fractionator to fractionate all of one or more separate streams provided by the NGL extraction units.
19 . Apparatus according to claim 13 , wherein X is different from Z.
20 . Apparatus as claimed in claim 13 , wherein the or each cooling system is a liquefying system.
21 . Method as claimed in claim 2 , wherein Y is 2 and Z is 1.
22 . Method as claimed in claim 4 , wherein Y is 3 and Z is 1 or 2.
23 . Method according to claim 1 , wherein the cooling step (d) liquefies the second treated stream or streams to provide liquefied natural gas.
24 . Apparatus as claimed in claim 14 , wherein Y is 2 and Z is 1.
25 . Apparatus as claimed in claim 16 , wherein Y is 3 and Z is 1 or 2.Join the waitlist — get patent alerts
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