发明名称 |
Nitrogen rejection unit |
摘要 |
Methods and systems for removing nitrogen during liquefaction of natural are provided. Methods of removing nitrogen include warming a predominantly methane stream in a methane cold box to provide a warmed predominantly methane stream; conducting at least a portion of the warmed predominantly methane stream from the methane cold box to a nitrogen removal unit comprising at least a first nitrogen removal column and a last nitrogen removal column, wherein the first nitrogen removal column is located upstream of the last nitrogen removal column; passing the warmed predominantly methane stream through the last nitrogen removal column to provide a refluxed warmed predominantly methane stream; and routing at least a portion of the refluxed warmed predominantly methane stream to the last nitrogen removal column. |
申请公布号 |
US9335091(B2) |
申请公布日期 |
2016.05.10 |
申请号 |
US201313951021 |
申请日期 |
2013.07.25 |
申请人 |
ConocoPhillips Company |
发明人 |
Qualls Wesley Roy;Ma Qi;Evans Megan Victoria;Herzog Karl Lee;Yao Jame;Chahal Mohan;Gentry Matt Calvin;Praderio Attilio Jose;Bellomy Marc Thomas;Gandhi Satish;Wilkes Mike;James Will |
分类号 |
F25J1/00;F25J3/00;F25J1/02;F25J3/02 |
主分类号 |
F25J1/00 |
代理机构 |
ConocoPhillips Company |
代理人 |
ConocoPhillips Company |
主权项 |
1. A method of removing nitrogen from a natural gas stream comprising:
(a) routing the natural gas stream from a methane cold box of a main liquefaction process to a nitrogen rejection unit comprising: a first distillation column, a second distillation column, a third distillation column, and a condenser, wherein the main liquefaction process comprises: one or more refrigeration cycles external to the nitrogen rejection unit; (b) at least partially condensing the natural gas stream via the condenser, wherein the condenser utilizes a refrigerant used to transfer heat in the one or more refrigeration cycles to form a condensed natural gas stream, wherein the refrigerant is taken from the refrigeration cycle routed into a core-in-shell exchanger forming the condenser and returned to the refrigeration cycle without passing through the first distillation column; and (c) routing at least a portion of the condensed natural gas stream to the third distillation column to separate the at least a portion of the condensed natural gas stream into a third top fraction and a third bottom fraction, wherein the third top fraction comprises a predominantly nitrogen gas stream. |
地址 |
Houston TX US |