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    NATURAL GAS LIQUEFACTION PROCESS
    2.
    发明申请
    NATURAL GAS LIQUEFACTION PROCESS 审中-公开
    天然气液化过程

    公开(公告)号：WO2009029140A1

    公开(公告)日：2009-03-05

    申请号：PCT/US2008/008027

    申请日：2008-06-26

    Applicant: EXXONMOBIL UPSTREAM RESEARCH COMPANY ,  MINTA, Moses ,  STONE, John, B. ,  FEIST, Raymond, Scott

    Inventor： MINTA, Moses ,  STONE, John, B. ,  FEIST, Raymond, Scott

    IPC: F25J1/00

    CPC classification number: F25J1/0022 ,  F25J1/0035 ,  F25J1/0037 ,  F25J1/004 ,  F25J1/0042 ,  F25J1/0045 ,  F25J1/005 ,  F25J1/0072 ,  F25J1/0082 ,  F25J1/0092 ,  F25J1/0215 ,  F25J1/0219 ,  F25J1/025 ,  F25J1/0254 ,  F25J1/0288 ,  F25J2210/06 ,  F25J2220/62 ,  F25J2230/30 ,  F25J2270/02 ,  F25J2270/04 ,  F25J2270/08

    Abstract: The described invention relates to processes and systems for treating a gas stream, particularly one rich in methane for forming liquefied natural gas (LNG), said process including: (a) providing a gas stream; (b) providing a refrigerant; (c) compressing said refrigerant to provide a compressed refrigerant; (d) cooling said compressed refrigerant by indirect heat exchange with a cooling fluid; (e) expanding the refrigerant of (d) to cool said refrigerant, thereby producing an expanded, cooled refrigerant; (f) passing said expanded, cooled refrigerant to a first heat exchange area; (g) compressing the gas stream of (a) to a pressure of from greater than or equal to 1,000 psia to less than or equal to 4,500 psia; (h) cooling said compressed gas stream by indirect heat exchange with an external cooling fluid; and heat exchanging the compressed gas stream with the expanded, cooled refrigerant stream.

    Abstract translation: 所描述的本发明涉及用于处理气流的方法和系统，特别是富含甲烷以形成液化天然气（LNG）的方法和系统，所述方法包括：（a）提供气流; （b）提供制冷剂; （c）压缩所述制冷剂以提供压缩的制冷剂; （d）通过与冷却流体的间接热交换来冷却所述压缩的制冷剂; （e）使（d）的制冷剂膨胀以冷却所述制冷剂，由此制造膨胀冷却的制冷剂; （f）将所述膨胀冷却的制冷剂通入第一热交换区域; （g）将（a）的气流压缩至大于或等于1,000psia至小于或等于4500psia的压力; （h）通过与外部冷却流体的间接热交换来冷却所述压缩气流; 以及用膨胀的冷却的制冷剂流将压缩气流进行热交换。

    PROCESS AND INSTALLATION FOR SUPPLYING GASEOUS CARBON MONOXIDE BY CRYOGENIC DISTILLATION
    4.
    发明申请
    PROCESS AND INSTALLATION FOR SUPPLYING GASEOUS CARBON MONOXIDE BY CRYOGENIC DISTILLATION 审中-公开
    通过低温蒸馏提供气体一氧化碳的工艺和安装

    公开(公告)号：WO2012175635A2

    公开(公告)日：2012-12-27

    申请号：PCT/EP2012/062020

    申请日：2012-06-21

    Applicant: L'AIR LIQUIDE, SOCIETE ANONYME POUR L'ETUDE ET L'EXPLOITATION DES PROCEDES GEORGES CLAUDE ,  BROCHERIOU, Emmanuelle ,  PRASAD, Bhadri ,  RIVOAL, Audrey ,  VICTOR, Marie-Pascal

    Inventor： BROCHERIOU, Emmanuelle ,  PRASAD, Bhadri ,  RIVOAL, Audrey ,  VICTOR, Marie-Pascal

    IPC: F25J3/02

    CPC classification number: F25J3/0223 ,  F25J3/0233 ,  F25J3/0252 ,  F25J3/0257 ,  F25J3/0261 ,  F25J2200/70 ,  F25J2200/76 ,  F25J2205/30 ,  F25J2215/04 ,  F25J2250/30 ,  F25J2270/02 ,  F25J2270/04 ,  F25J2270/08 ,  F25J2270/24 ,  F25J2280/02 ,  F25J2280/20

    Abstract: In a process for supplying gaseous carbon monoxide by cryogenic distillation, a feed gas (1), containing carbon monoxide as at least one of its principal components and at least one other components chosen from methane, nitrogen and hydrogen, is purified using an adsorption step in one of at least two adsorbent beds (3) to produce a purified feed gas to be sent to the separation unit comprising at least one distillation column (7, 19, 27), the separation unit separates the feed gas to produce gaseous carbon monoxide and the gaseous carbon monoxide is compressed in a product compressor (35) to produce a final product at a product pressure, refrigeration is supplied to the process by a carbon monoxide cooling cycle in which a cycle fluid is compressed in at least the product compressor, cooled and expanded, at least part of the carbon monoxide is liquefied to form pressurised liquefied carbon monoxide and part of the pressurised liquefied carbon monoxide (51 A, 53A, 59A), is vaporised at the product pressure to form a pressurised gaseous back-up stream which is then mixed with the final product, vaporisation of the carbon monoxide taking place only when there is an increase in demand for pressurised carbon monoxide.

    Abstract translation: 在通过低温蒸馏提供气态一氧化碳的方法中，使用吸附步骤纯化含有一氧化碳作为其主要成分中的至少一种和至少一种选自甲烷，氮和氢的其它组分的进料气体（1） 在至少两个吸附剂床（3）中的一个中以产生待送至包含至少一个蒸馏塔（7,19,27）的分离单元的纯化进料气体，分离单元分离进料气体以产生气态一氧化碳 并且气体一氧化碳在产品压缩机（35）中被压缩以在产品压力下产生最终产品，通过至少在产品压缩机中循环流体被压缩的一氧化碳冷却循环向该过程供应制冷， 冷却和膨胀，至少部分一氧化碳液化以形成加压液化一氧化碳，并且部分加压液化一氧化碳（51A，53A，59A）被蒸发在 产品压力以形成加压的气态后备料流，然后与最终产物混合，一氧化碳的蒸发仅在加压一氧化碳需求增加时发生。

    NITROGEN REJECTION FROM CONDENSED NATURAL GAS
    6.
    发明申请
    NITROGEN REJECTION FROM CONDENSED NATURAL GAS 审中-公开
    来自冷凝天然气的氮气排放

    公开(公告)号：WO2004104143A1

    公开(公告)日：2004-12-02

    申请号：PCT/EP2004/002257

    申请日：2004-03-05

    Applicant: AIR PRODUCTS AND CHEMICALS, INC. ,  BROSTOW, Adam, Adrian ,  ROBERTS, Mark, Julian ,  SPILSBURY, Christopher, Geoffrey

    Inventor： BROSTOW, Adam, Adrian ,  ROBERTS, Mark, Julian ,  SPILSBURY, Christopher, Geoffrey

    IPC: C10L3/10

    CPC classification number: C10L3/10 ,  F25J3/0209 ,  F25J3/0233 ,  F25J3/0257 ,  F25J2200/02 ,  F25J2200/50 ,  F25J2200/74 ,  F25J2200/76 ,  F25J2205/04 ,  F25J2215/04 ,  F25J2240/12 ,  F25J2240/30 ,  F25J2270/04 ,  F25J2270/08 ,  F25J2270/12 ,  F25J2270/14 ,  F25J2270/42 ,  Y10S62/927

    Abstract: Method for the rejection of nitrogen from condensed natural gas which comprises (a) introducing the condensed natural gas into a distillation column at a first location therein, withdrawing a nitrogen-enriched overhead vapor stream from the distillation column, and withdrawing a purified liquefied natural gas stream from the bottom of the column; (b) introducing a cold reflux stream into the distillation column at a second location above the first locatino, wherein the refrigeration to provide the cold reflux stream is obtained by compressing and work expanding a refrigerant stream comprising nitrogen; and (c) either (1) cooling the purified liquefied natural gas stream or cooling the condensed natural gas stream or (2) cooling both the purified liquefied natural gas stream and the condensed natural gas stream, wherein refrigeration for (1) or (2) is obtained by compressing and work expanding the refrigerant stream comprising nitrogen. The refrigerant stream may comprise all or a portion of the nitrogen-rich vapor stream from the distillation column.

    Abstract translation: 从冷凝天然气中排除氮的方法，其包括：（a）在其第一位置将冷凝的天然气引入蒸馏塔，从蒸馏塔中取出富氮塔顶馏出物流，并将纯化的液化天然气 从塔的底部流出; （b）在第一位置上方的第二位置将冷的回流物流引入蒸馏塔，其中提供冷回流的制冷通过压缩和加工包含氮气的制冷剂流而获得; （c）（1）冷却纯化的液化天然气流或冷却冷凝的天然气流，或（2）冷却纯化的液化天然气流和冷凝的天然气流，其中（1）或（2 ）通过压缩和加工包含氮气的制冷剂流而工作获得。 制冷剂流可以包括来自蒸馏塔的全部或一部分富氮蒸气流。

    이산화탄소의 처리 모듈 및 그 처리 방법
    8.
    发明申请
    이산화탄소의 처리 모듈 및 그 처리 방법 审中-公开
    二氧化碳处理模块及其处理方法

    公开(公告)号：WO2013100304A1

    公开(公告)日：2013-07-04

    申请号：PCT/KR2012/006660

    申请日：2012-08-22

    Applicant: 대우조선해양 주식회사 ,  유병용 ,  김성배 ,  우일국 ,  오영태 ,  나희승

    Inventor： 유병용 ,  김성배 ,  우일국 ,  오영태 ,  나희승

    IPC: F25J3/02 ,  F25J3/00

    CPC classification number: F25J3/0266 ,  C10L3/104 ,  F25J1/0027 ,  F25J3/0209 ,  F25J3/0233 ,  F25J2200/02 ,  F25J2200/74 ,  F25J2215/04 ,  F25J2220/82 ,  F25J2260/80 ,  F25J2270/02 ,  F25J2270/08 ,  F25J2280/40 ,  F25J2290/34 ,  Y02C10/12

    Abstract: 본 발명은 사워 가스(Sour Gas)로부터 분리된 액체 이산화탄소를 교축 감압 팽창시키고, 저온으로 기액 분리하여 선박 운송 또는 석유 회수증진용으로 공급하는 실시예와, 한계가스정(stranded gas well)으로부터 발생되는 사워 가스(sour gas)로부터 분리 배출되는 액체 이산화탄소에 한계가스정으로부터 발생되는 메탄을 냉매로써 통과시켜 액체 이산화탄소를 냉각시키는 실시예로부터 한계가스정의 사워 가스로부터 분리되는 물질을 냉매로 하여 이산화탄소를 냉각시킴으로써 이산화탄소 저장 및 포집용이나 석유 회수증진용 등 극저온의 액체 이산화탄소의 수요처에 적합한 온도 및 상태 조건으로 공급될 수 있도록 하는 이산화탄소의 처리 모듈 및 그 처리 방법에 관한 것이다.

    Abstract translation: 根据一个实施例，其中通过节流减压膨胀从酸槽分离的液体二氧化碳，并且在低温下气液分离以供运输或改善石油回收，并且其中由 通过将液体二氧化碳分离并排出，从而将滞留气井作为冷却剂通过作为冷却液的二氧化碳冷却液体二氧化碳，本发明涉及处理二氧化碳的组件， 在适当的温度和状态条件下，当需要用于二氧化碳的储存或收集的二氧化碳的储存或收集需要非常低的液体二氧化碳时，以及通过冷却二氧化碳来改善石油回收等的方法，所述方法使用 与作为冷却剂的绞合气井的酸性气体分离的材料。

    CRYOGENIC AIR SEPARATION SYSTEM FOR ENHANCED LIQUID PRODUCTION
    9.
    发明申请
    CRYOGENIC AIR SEPARATION SYSTEM FOR ENHANCED LIQUID PRODUCTION 审中-公开
    用于增强液体生产的低温空气分离系统

    公开(公告)号：WO2007145915A2

    公开(公告)日：2007-12-21

    申请号：PCT/US2007013193

    申请日：2007-06-05

    Applicant: PRAXAIR TECHNOLOGY INC ,  HAWARD HENRY EDWARD

    Inventor： HAWARD HENRY EDWARD

    IPC: F25J3/04

    CPC classification number: F25J3/0423 ,  F25J3/04048 ,  F25J3/0409 ,  F25J3/04175 ,  F25J3/04284 ,  F25J3/04296 ,  F25J3/04339 ,  F25J3/04412 ,  F25J3/04678 ,  F25J2205/02 ,  F25J2205/04 ,  F25J2210/04 ,  F25J2230/40 ,  F25J2235/02 ,  F25J2235/52 ,  F25J2245/02 ,  F25J2245/40 ,  F25J2270/08 ,  Y10S62/924

    Abstract: Argon, oxygen and nitrogen contained within an incoming air feed (10) is fractionated within an air separation system having a multiple column arrangement (32) that includes a higher pressure column (30) and a lower pressure column (34) to produce oxygen and nitrogen-rich fractions and an argon column (90) to produce an argon-rich fraction for recovery of the argon as an argon product. A two-phase stream (132; 134) can be formed by either expanding at least part of a liquid air stream (82) or by a liquid oxygen column bottoms (132) formed within a higher pressure column (30) of the multiple column arrangement (32). The liquid air stream (82) is formed by liquefying part of the air feed (22) to be fractionated against vaporizing a pumped liquid stream (76) composed of nitrogen and/or oxygen. The diversion of nitrogen vapor (146; 166) contained in the nitrogen-rich fraction increases the liquid to vapor ratio within the lower pressure (34) column to increase the argon recovery.

    Abstract translation: 包含在进入空气进料（10）内的氩，氧和氮在具有多塔排列（32）的空气分离系统内被分馏，所述多塔排列包括高压塔（30）和低压塔（34）以产生氧气， 富氮馏分和氩塔（90），以产生用于回收作为氩产物的氩的富氩馏分。 两相流（132; 134）可以通过膨胀液态空气流（82）的至少一部分或形成在多塔的高压塔（30）内的液氧塔底部（132） 安排（32）。 液体空气流（82）通过液化空气进料（22）的一部分而被分馏形成，以使蒸发由氮和/或氧组成的泵送液体流（76）蒸发。 富氮馏分中所含的氮蒸气（146; 166）的转移增加了较低压力（34）塔内的液体与蒸汽的比例，从而提高氩的回收率。

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