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Patent Agency Ranking
公开(公告)号：US20150232763A1
公开(公告)日：2015-08-20
申请号：US14424829
申请日：2013-08-15
Applicant: Haldor Topsoe A/S
Inventor： Per Juul Dahl , Stefan Andersen
CPC classification number: C10G2/30 , C01B3/382 , C01B3/386 , C01B3/50 , C01B3/501 , C01B3/56 , C01B2203/0244 , C01B2203/0261 , C01B2203/04 , C01B2203/0405 , C01B2203/043 , C01B2203/062 , C01B2203/142 , C01B2203/143 , C01B2203/147 , C01B2203/148 , C01B2203/1604 , C10G2/32 , C10G2300/4031 , Y02P20/129
Abstract: The invention relates to a process for starting up a gas-to-liquid process including the production of synthesis gas and a downstream GTL process. The synthesis gas is produced by the use of autothermal reforming (ATR) or catalytic partial oxidation (CPO) and during the starting period the effluent gas from the ATR or CPO is significantly changed to form an off-gas recycle which is fed to the ATR or CPO. When the downstream GTL process is running, the recycle to ATR or CPO is shifted to its off-gas.
Abstract translation: 本发明涉及一种启动包括合成气生产和下游GTL工艺在内的气 - 液工艺的方法。 通过使用自热重整（ATR）或催化部分氧化（CPO）生产合成气，并且在起始阶段，来自ATR或CPO的流出气体被显着改变以形成进料到ATR的废气再循环 或CPO。 当下游GTL工艺运行时，对ATR或CPO的再循环转移到其废气。
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公开(公告)号：US20230098920A1
公开(公告)日：2023-03-30
申请号：US17801018
申请日：2021-03-01
Applicant: Topsoe A/S
Inventor： Per Juul Dahl , Nitin Sharma
Abstract: A process for producing synthesis gas, the process comprising the steps of a) reforming a hydrocarbon feed in a reforming section thereby obtaining a synthesis gas comprising CH4, CO, CO2, H2 and H2O and impurities comprising ammonia;b) shifting the synthesis gas in a shift section comprising one or more shift steps in series to a shifted synthesis gas; c) separating from the shifted synthesis gas a process condensate originating from cooling and optionally washing of the shifted synthesis gas;d) passing the process condensate to a condensate steam stripper, wherein dissolved shift byproducts comprising ammonia, methanol and amines formed during shifting the synthesis gas are stripped out of the process condensate using steam resulting in a stripper steam stream, e) adding a part of the stripper steam stream from the process condensate steam strip-per to the hydrocarbon feed and/or to the synthesis gas downstream the reforming section, up-stream the last shift step, wherein the remaining part of stripper steam is purged.
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公开(公告)号：US20180238628A1
公开(公告)日：2018-08-23
申请号：US15514961
申请日：2015-10-05
Applicant: Haldor Topsoe A/S
Inventor： Per Juul Dahl
Abstract: A heat exchanger has a pass baffle which is formed as an enclosure with two openings, one opening for connection to a shell-side fluid opening and one opening for passing heat exchanger tubes.
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公开(公告)号：US09464237B2
公开(公告)日：2016-10-11
申请号：US14424829
申请日：2013-08-15
Applicant: Haldor Topsoe A/S
Inventor： Per Juul Dahl , Stefan Andersen
CPC classification number: C10G2/30 , C01B3/382 , C01B3/386 , C01B3/50 , C01B3/501 , C01B3/56 , C01B2203/0244 , C01B2203/0261 , C01B2203/04 , C01B2203/0405 , C01B2203/043 , C01B2203/062 , C01B2203/142 , C01B2203/143 , C01B2203/147 , C01B2203/148 , C01B2203/1604 , C10G2/32 , C10G2300/4031 , Y02P20/129
Abstract: The invention relates to a process for starting up a gas-to-liquid process including the production of synthesis gas and a downstream GTL process. The synthesis gas is produced by the use of autothermal reforming (ATR) or catalytic partial oxidation (CPO) and during the starting period the effluent gas from the ATR or CPO is significantly changed to form an off-gas recycle which is fed to the ATR or CPO. When the downstream GTL process is running, the recycle to ATR or CPO is shifted to its off-gas.
Abstract translation: 本发明涉及一种启动包括合成气生产和下游GTL工艺在内的气 - 液工艺的方法。 通过使用自热重整（ATR）或催化部分氧化（CPO）生产合成气，并且在起始阶段，来自ATR或CPO的流出气体被显着改变以形成进料到ATR的废气再循环 或CPO。 当下游GTL工艺运行时，对ATR或CPO的再循环转移到废气。
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公开(公告)号：US20230121402A1
公开(公告)日：2023-04-20
申请号：US17800997
申请日：2021-03-01
Applicant: Topsoe A/S
Inventor： Per Juul Dahl
Abstract: A process for producing synthesis gas, the process comprising the steps of a) reforming a hydrocarbon feed in a reforming section thereby obtaining a synthesis gas comprising CH4, CO, CO2, H2 and H2O and impurities comprising ammonia; b) shifting the synthesis gas in a shift section comprising one or more shift steps in series to a shifted synthesis gas; c) separating from the shifted synthesis gas a process condensate originating from cooling and optionally washing of the shifted synthesis gas; d) passing a part of the process condensate to a condensate steam stripper, wherein dissolved shift byproducts comprising ammonia, methanol and amines formed during shifting the synthesis gas are stripped out of the process condensate using steam resulting in a stripper steam stream, e) adding the stripper steam stream from the process condensate steam stripper to the hydrocarbon feed and/or to the synthesis gas downstream the reforming section, up-stream the last shift step, wherein the remaining part of the process condensate is purged.
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