公开(公告)号：US20230304732A1

公开(公告)日：2023-09-28

申请号：US18204005

申请日：2023-05-31

Applicant: EnFlex, Inc.

Inventor： James Zhao ,  Shukui Zhao

IPC: F25J3/02 ,  F25J3/06

CPC classification number: F25J3/0252 ,  F25J3/062 ,  F25J3/0655 ,  F25J3/0645 ,  F25J3/0219 ,  F25J2270/904 ,  F25J2200/02 ,  F25J2205/04 ,  F25J2215/10 ,  F25J2230/20 ,  F25J2230/08 ,  F25J2240/04 ,  F25J2240/40 ,  F25J2270/06 ,  F25J2230/60 ,  F25J2230/30 ,  F25J2215/02 ,  F25J2210/12 ,  F25J2215/64 ,  F25J2230/32 ,  F25J2215/04 ,  F25J2235/60 ,  F25J2245/02 ,  F25J2210/04 ,  F25J2210/62

Abstract: One or more specific embodiments disclosed herein includes a method for separating hydrogen from an olefin hydrocarbon rich compressed effluent vapor stream, employing a integrated heat exchanger, multiple gas-liquid separators, external refrigeration systems, and a rectifier attached to a liquid product drum.

公开(公告)号：US20180251373A1

公开(公告)日：2018-09-06

申请号：US15759908

申请日：2016-07-20

Applicant: L'Air Liquide, Societe Anonyme pour I'Etude et I'Etude et I'Exploitation des Procedes Georges Cla

Inventor： Angela FERNANDEZ ,  Antoine HERNANDEZ ,  Jean-Marc TSEVERY

IPC: C01B3/50 ,  F25J3/02

CPC classification number: C01B3/508 ,  C01B3/506 ,  C01B2203/046 ,  F25J3/0223 ,  F25J3/0252 ,  F25J3/0261 ,  F25J3/0271 ,  F25J2200/70 ,  F25J2200/76 ,  F25J2205/04 ,  F25J2205/30 ,  F25J2215/02 ,  F25J2230/32 ,  F25J2245/02 ,  F25J2270/02 ,  F25J2270/04 ,  F25J2270/24

Abstract: In a method for producing a gaseous mixture of CO and H2, a first gas comprising at least 50% CO is compressed in a first compressor to form a first compressed gas cooled to a first temperature and mixes with a second gas comprising at least 50% hydrogen in order to form the gaseous mixture, at least one of the first and second gases originating from a cryogenic distillation separation unit in which a feed gas containing H2 and CO cools in a first heat exchanger and is separated in at least one distillation column and at least one part of the second gas heats in the separation unit to a third temperature lower than the first temperature and is then sent to mix with the first gas.

公开(公告)号：US09909803B2

公开(公告)日：2018-03-06

申请号：US14997642

申请日：2016-01-18

Applicant: Air Products and Chemicals, Inc.

Inventor： Brian Alfred McNeil ,  Andrew Weaver ,  David Graham Winter

IPC: F25J3/02 ,  C01B3/50 ,  F25J3/08

CPC classification number: F25J3/0223 ,  C01B3/506 ,  C01B2203/0415 ,  C01B2203/046 ,  C01B2203/047 ,  C01B2203/048 ,  C01B2203/145 ,  C01B2203/146 ,  C01B2203/147 ,  F25J3/0233 ,  F25J3/0252 ,  F25J3/0257 ,  F25J3/0261 ,  F25J3/0271 ,  F25J3/08 ,  F25J2200/74 ,  F25J2200/76 ,  F25J2200/94 ,  F25J2205/04 ,  F25J2205/30 ,  F25J2215/02 ,  F25J2245/02 ,  F25J2270/02 ,  F25J2270/04 ,  F25J2270/24

Abstract: A process and apparatus for separating a feed containing hydrogen, carbon monoxide, methane, and optionally nitrogen to form a product gas having a desired H2:CO molar ratio and optionally a hydrogen product gas and a carbon monoxide product gas. The feed is partially condensed to form a hydrogen-enriched vapor fraction and a carbon monoxide-enriched liquid fraction. The hydrogen-enriched vapor fraction and carbon monoxide-enriched liquid fraction are combined in a regulated manner to form an admixture, which is cryogenically separated to form the product mixture having the desired H2:CO molar ratio.

公开(公告)号：US20170197829A1

公开(公告)日：2017-07-13

申请号：US15313053

申请日：2015-05-27

Applicant: Haldor Topsøe A/S

Inventor： Niels Ulrik Andersen

IPC: C01B3/38 ,  C01B3/32 ,  C01B3/36 ,  F25J3/06 ,  B01D53/22 ,  B01D53/047 ,  B01D53/14 ,  F25J3/02 ,  B01J19/24 ,  C07C29/151

CPC classification number: C01B3/38 ,  B01D53/047 ,  B01D53/1475 ,  B01D53/22 ,  B01D2256/16 ,  B01D2256/22 ,  B01J19/245 ,  C01B3/32 ,  C01B3/36 ,  C01B2203/0227 ,  C01B2203/025 ,  C01B2203/0288 ,  C01B2203/0405 ,  C01B2203/042 ,  C01B2203/043 ,  C01B2203/046 ,  C01B2203/0475 ,  C01B2203/061 ,  C01B2203/1235 ,  C07C29/151 ,  C07C29/1518 ,  F25J3/0252 ,  F25J3/0261 ,  F25J3/0655 ,  F25J3/0665 ,  Y02P20/146 ,  Y02P20/152 ,  C07C31/04

Abstract: The present application relates to a production plant comprising—a synthesis gas generation step (1) arranged to receive a hydrocarbon or carboneous feedstock (2) and in a synthesis gas generation process provide a syngas, —a production step (4) arranged to receive the syngas and produce a product stream (5), —a reverse water gas shift step (4) arranged to receive a H2 rich gas stream (7) and a C02 feed (8) and in a RWGS step obtain a reverse shifted gas stream (9), and—means (10) for adding said reverse shifted gas stream (9) to the synthesis gas stream (3).

公开(公告)号：US09682903B2

公开(公告)日：2017-06-20

申请号：US15189419

申请日：2016-06-22

Applicant: Neste Oyj

Inventor： Pekka Savolainen ,  Rogier Van De Velde ,  Martijn Van Den Berg ,  Juha Visuri

IPC: B01D53/22 ,  C07C7/04 ,  C07C7/144 ,  C01B3/50 ,  F25J3/02 ,  C07C7/00 ,  C07C7/11 ,  C01B3/52

CPC classification number: C07C7/005 ,  B01D3/00 ,  B01D3/145 ,  B01D53/229 ,  B01D2256/16 ,  B01D2256/24 ,  B01D2257/108 ,  B01D2257/7022 ,  C01B3/503 ,  C01B3/52 ,  C01B2203/0405 ,  C01B2203/0415 ,  C01B2203/0475 ,  C01B2203/048 ,  C01B2203/0485 ,  C07C7/04 ,  C07C7/11 ,  C07C7/144 ,  C10L3/101 ,  C10L3/103 ,  C10L3/104 ,  C10L2200/0469 ,  C10L2290/543 ,  C10L2290/545 ,  C10L2290/548 ,  F25J3/0219 ,  F25J3/0242 ,  F25J3/0247 ,  F25J3/0252 ,  F25J2205/30 ,  F25J2205/40 ,  F25J2205/80 ,  F25J2210/12 ,  F25J2215/10 ,  F25J2215/64 ,  F25J2245/02 ,  F25J2290/12 ,  C07C9/08

Abstract: A method for treating a gas stream comprising hydrogen and propane, where a combination of membrane separation and elevated pressure distillation is used to separate the hydrogen gas from the propane gas.

公开(公告)号：US20170082358A1

公开(公告)日：2017-03-23

申请号：US15271633

申请日：2016-09-21

Applicant: Bernd Klein

Inventor： Bernd Klein

IPC: F25J3/02 ,  B01D53/22

CPC classification number: F25J3/0261 ,  B01D53/229 ,  C01B3/501 ,  C01B3/506 ,  C01B32/40 ,  C01B2203/146 ,  F25J3/0223 ,  F25J3/0252 ,  F25J3/0271 ,  F25J2200/70 ,  F25J2205/04 ,  F25J2205/40 ,  F25J2205/80 ,  F25J2210/04 ,  F25J2215/02 ,  F25J2245/02

Abstract: A process and plant are proposed for separating a feed mixture predominantly or exclusively containing carbon monoxide and hydrogen, in which the feed mixture is subjected to a cryogenic separation process in which a carbon monoxide-rich liquid and at least one residual gas mixture which is depleted in carbon monoxide and enriched in hydrogen, in comparison with the feed mixture, are formed. It is intended that the at least one residual gas mixture is subjected to a membrane separation process in which at least one hydrogen-rich permeate and at least one carbon monoxide-rich retentate are formed, wherein the or at least one of the carbon monoxide-rich retentates is recirculated to the cryogenic separation process.

公开(公告)号：US20160265840A1

公开(公告)日：2016-09-15

申请号：US15034110

申请日：2014-11-06

Applicant: L'Air Liquide, Societe Anonyme pour l'Etude et l'Exploitation des Procedes Georges Claude

Inventor： Patrick LE BOT

IPC: F25J3/02 ,  B01D53/22 ,  B01D53/047

CPC classification number: F25J3/0266 ,  B01D53/002 ,  B01D53/047 ,  B01D53/229 ,  B01D53/261 ,  B01D2256/22 ,  B01D2257/108 ,  B01D2257/502 ,  B01D2257/7025 ,  B01D2259/40009 ,  B01D2259/40054 ,  F25J3/0223 ,  F25J3/0233 ,  F25J3/0252 ,  F25J3/0261 ,  F25J2205/40 ,  F25J2205/66 ,  F25J2205/80 ,  F25J2215/04 ,  F25J2220/82 ,  F25J2245/90 ,  F25J2290/42 ,  Y02C10/08 ,  Y02C10/12 ,  Y02C20/20

Abstract: The invention relates to a gas depleted of carbon dioxide produced by distillation, which is separated such as to produce a gas depleted of hydrogen, the gas depleted of hydrogen being used as a regeneration gas of a system for purification by adsorption upstream from the distillation, the composition of the regeneration gas at the intake of the purification system not being in the range of flammability in air.

Abstract translation: 本发明涉及通过蒸馏产生的贫化二氧化碳的气体，其被分离以产生贫的氢气，所述贫气用作用于通过蒸馏上游的吸附进行净化的系统的再生气体， 净化系统摄入时的再生气体的组成不在空气中的可燃性的范围内。

公开(公告)号：US20160146534A1

公开(公告)日：2016-05-26

申请号：US14900433

申请日：2014-06-25

Applicant: TECHNIP FRANCE

Inventor： Bruno DESTOUR ,  Yvon SIMON ,  Aurélia DADOU

IPC: F25J3/02 ,  C07C7/04 ,  C07C7/00

CPC classification number: F25J3/0238 ,  B01D53/002 ,  B01D53/047 ,  B01D53/1456 ,  B01D2256/24 ,  B01D2257/304 ,  B01D2257/502 ,  B01D2257/504 ,  B01D2257/80 ,  C07C7/005 ,  C07C7/04 ,  C10G70/043 ,  F25J3/0219 ,  F25J3/0233 ,  F25J3/0252 ,  F25J3/0261 ,  F25J2200/02 ,  F25J2200/74 ,  F25J2205/04 ,  F25J2205/40 ,  F25J2205/60 ,  F25J2210/04 ,  F25J2210/12 ,  F25J2215/62 ,  F25J2230/30 ,  F25J2245/02 ,  F25J2270/04 ,  F25J2270/12 ,  F25J2270/60

Abstract: This method comprises the following steps: treating a feed stream (12) to obtain a treated gas stream (60); cooling the treated gas stream (60) in a heat exchanger (34) to form at least one column feed fraction; feeding each column feed fraction into a distillation column (50); heating at least one downstream flow (106) derived from the column head stream (104) in the heat exchanger (34). The treatment step comprises the forming of an intermediate stream (20) containing at least 20 mole % ethylene and at least 20 mole % carbon monoxide, the method comprising a step to remove the carbon monoxide contained in the intermediate stream (20).

Abstract translation: 该方法包括以下步骤：处理进料流（12）以获得经处理的气流（60）; 在热交换器（34）中冷却经处理的气流（60）以形成至少一个塔进料馏分; 将每个进料馏分进料到蒸馏塔（50）中; 加热源自热交换器（34）中的塔头流（104）的至少一个下游流（106）。 处理步骤包括形成含有至少20摩尔％乙烯和至少20摩尔％一氧化碳的中间料流（20），该方法包括除去中间物流（20）中所含的一氧化碳的步骤。

公开(公告)号：US20160115098A1

公开(公告)日：2016-04-28

申请号：US14524285

申请日：2014-10-27

Applicant: UOP LLC

Inventor： Robert Edison Tsai ,  Xin X. Zhu ,  Tokhanh Ngo ,  William Yanez ,  Bryan K. Glover

IPC: C07C7/00 ,  F25J3/02 ,  C01B3/52

CPC classification number: F25J3/0242 ,  C01B3/34 ,  C01B3/52 ,  C01B2203/0227 ,  C01B2203/0415 ,  C01B2203/048 ,  C01B2203/1247 ,  C07C7/005 ,  F25J3/0247 ,  F25J3/0252 ,  F25J2200/08 ,  F25J2205/02 ,  F25J2215/10 ,  F25J2215/62 ,  F25J2230/08 ,  F25J2230/60 ,  F25J2245/02 ,  F25J2270/90

Abstract: Embodiments of apparatuses and methods for reforming of hydrocarbons including recovery of products are provided. In one example, a method comprises separating a reforming-zone effluent to form a net gas phase stream and a liquid phase hydrocarbon stream. The net gas phase stream is compressed, partially condensed and cooled to form a partially condensed, compressed net gas phase stream. The partially condensed, compressed net gas phase stream is separated to form an intermediate gas phase stream. The intermediate gas phase stream is cooled to form a cooled intermediate gas phase stream. The liquid phase hydrocarbon stream is cooled to form a cooled liquid phase hydrocarbon stream. The cooled intermediate gas phase stream is contacted with the cooled liquid phase hydrocarbon stream to form an H2-rich stream and a cooled second intermediate liquid phase hydrocarbon stream that is enriched with C3/C4 hydrocarbons.

Abstract translation: 提供了包括产物回收的烃类重整装置和方法的实施例。 在一个实例中，一种方法包括分离重整区流出物以形成净气相流和液相烃流。 净气相流被压缩，部分冷凝并冷却以形成部分冷凝的压缩的净气相物流。 部分冷凝的，压缩的净气相物流被分离以形成中间气相物流。 中间气相物流被冷却以形成冷却的中间气相物流。 将液相烃流冷却以形成冷却的液相烃流。 冷却的中间气相物流与冷却的液相烃物流接触以形成富H2的物流和富含C3 / C4烃的冷却的第二中间液相烃物流。

公开(公告)号：US08869554B2

公开(公告)日：2014-10-28

申请号：US13265013

申请日：2010-09-09

Applicant: Kazuhiro Takeda ,  Yosuke Nakagawa ,  Tomoaki Takeda ,  Yasushi Mori

Inventor： Kazuhiro Takeda ,  Yosuke Nakagawa ,  Tomoaki Takeda ,  Yasushi Mori

IPC: F25J3/00 ,  F04B49/06

CPC classification number: F04B49/06 ,  F04B49/065 ,  F04B2203/0209 ,  F04B2205/01 ,  F25J3/0223 ,  F25J3/0252 ,  F25J3/0257 ,  F25J3/0266 ,  F25J3/0295 ,  F25J2230/30 ,  F25J2240/02 ,  F25J2245/02 ,  F25J2280/02 ,  Y02C10/12 ,  Y02E60/34

Abstract: Gas treatment equipment includes a compressor which compresses process gas, a first process module which is disposed downstream of the compressor and which treats the process gas, an expander which is disposed downstream of the first process module and which expands the process gas to obtain power, a second process module which is disposed downstream of the expander and which treats the process gas, and a driver which drives the compressor. A first pressure indicator is disposed at an inlet of the compressor for the process gas and measures a pressure of the process gas, and a second pressure indicator is disposed at an outlet of the second process module for the process gas and measures a pressure of the process gas. A recirculation flow path is connected to both of the outlet of the second process module for the process gas and the inlet of the compressor.

Abstract translation: 气体处理设备包括压缩处理气体的压缩机，设置在压缩机下游并处理过程气体的第一处理模块，设置在第一处理模块下游并膨胀处理气体以获得动力的膨胀器， 第二处理模块，其设置在膨胀机的下游并且处理处理气体;以及驱动器，其驱动压缩机。 第一压力指示器设置在用于处理气体的压缩机的入口处，并且测量处理气体的压力，并且第二压力指示器设置在用于处理气体的第二处理模块的出口处，并且测量压力 工艺气体。 再循环流动路径连接到用于处理气体的第二处理模块的出口和压缩机的入口。