发明名称 Integrated Nitrogen Removal in the Production of Liquefied Natural Gas Using Intermediate Feed Gas Separation
摘要 A method and apparatus for liquefying a natural gas feed stream and removing nitrogen therefrom to produce a nitrogen-depleted LNG product, in which a natural gas feed stream is fed into the warm end of a main heat exchanger, cooled and at least partially liquefied, withdrawn from an intermediate location of the main heat exchanger and separated to form a nitrogen-enriched natural gas vapor stream and a nitrogen-depleted natural gas liquid stream, the liquid and vapor streams being reintroduced into an intermediate location of the main heat exchanger and further cooled in parallel to form a first LNG stream and a first at least partially liquefied nitrogen-enriched natural gas stream, respectively.
申请公布号 US2015308737(A1) 申请公布日期 2015.10.29
申请号 US201414260678 申请日期 2014.04.24
申请人 AIR PRODUCTS AND CHEMICALS, INC. 发明人 Chen Fei;Liu Yang;Krishnamurthy Gowri;Ott Christopher Michael;Roberts Mark Julian
分类号 F25J3/02 主分类号 F25J3/02
代理机构 代理人
主权项 1. A method for producing a nitrogen-depleted LNG product, the method comprising: (a) introducing a natural gas feed stream into the warm end of a main heat exchanger, cooling and at least partially liquefying the natural gas feed stream, and withdrawing the cooled and at least partially liquefied stream from an intermediate location of the main heat exchanger; (b) expanding, partially vaporizing and separating the cooled and at least partially liquefied stream to form a nitrogen-enriched natural gas vapor stream and a nitrogen-depleted natural gas liquid stream; (c) separately re-introducing said vapor and liquid streams into an intermediate location of the main heat exchanger, further cooling the vapor and liquid streams in parallel, the liquid stream being further cooled to form a first LNG stream and the vapor stream being further cooled and at least partially liquefied to form a first at least partially liquefied nitrogen-enriched natural gas stream, and withdrawing the first LNG stream and the first at least partially liquefied nitrogen-enriched natural gas stream from the cold end of the main heat exchanger; (d) expanding, partially vaporizing and separating the first at least partially liquefied nitrogen-enriched natural gas stream to form a nitrogen-rich vapor product and a second LNG stream; and (e) expanding, partially vaporizing and separating the second LNG stream to form a nitrogen-depleted LNG product and a nitrogen-enriched natural gas vapor.
地址 Allentown PA US