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公开(公告)号：US20240326001A1
公开(公告)日：2024-10-03
申请号：US18618315
申请日：2024-03-27
发明人： Albert Kashafovich Shigabutdinov , Vladimir Vasilievich PRESNYAKOV , Ruslan Albertovich SHIGABUTDINOV , Rustem Nazyifovich AKHUNOV , Marat Rinatovich IDRISOV , Maksim Anatolievich NOVIKOV , Aleksei Aleksandrovich KHRAMOV , Andrei Aleksandrovich KONOVNIN , Artur Semenovich URAZAIKIN , Viswanathan Anand SUBRAMANIAN
CPC分类号： B01J8/1809 , B01D3/14 , B01J8/20 , B01J8/22 , B01J2208/00176 , B01J2208/00407 , B01J2208/00539
摘要： The invention relates to the field of processing petroleum products and more particularly to processes of hydroconversion and hydrocracking. A hydrocracking system for petroleum feedstock comprises a liquid-phase hydrocracking (LPH) section that comprises at least one LPH reactor; a gas-phase hydrocracking (GPH) section that comprises at least one GPH reactor; a separation section between the LPH section and the GPH section, comprising at least one high-pressure separator and at least one low-pressure separator; at least one stream supply line from the high-pressure separator to the low-pressure separator, wherein said at least one stream supply line comprises a reducing valve and a throttling cartridge arranged in the supply line downstream of the reducing valve; a heat-transfer medium feed line to the stream supply line and the pressure reducing valve. The technical result is to provide reliable operation of the hydrocracking system due to the prevention of erosive wear and destruction of the system components in the separation section.
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公开(公告)号：US20240198307A1
公开(公告)日：2024-06-20
申请号：US18456049
申请日：2023-08-25
申请人： UOP LLC
IPC分类号： B01J8/04
CPC分类号： B01J8/0496 , B01J8/0492 , B01J2208/00398 , B01J2208/00407 , B01J2208/00415 , B01J2208/00504
摘要： Processes and apparatuses for heating a hydrocarbon process stream, with an electrical heater to provide a portion of the heat requirement necessary for a chemical reaction to occur to one of the components of the hydrocarbon process stream. The electric heater may be in series or in parallel with a second, or main heater. The electric heater may be used between two reaction zones or between a feed exchange heater and a first reaction zone. The electric heater preferably provides between 5 to 40% of the heating requirement for the process stream.
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公开(公告)号：US11873276B2
公开(公告)日：2024-01-16
申请号：US17447828
申请日：2021-09-16
发明人： Hima Bindu Doosa , Saravanan Subramani , Ram Mohan Thakur , Vineeth Venu Nath , Kumaresan Loganathan , Bineesh Kanattukara Vijayan , Madhusudan Sau , Gurpreet Singh Kapur , Sankara Sri Venkata Ramakumar
CPC分类号： C07C5/333 , B01J8/0055 , B01J8/1836 , B01J8/24 , B01J38/02 , B01J38/06 , B01J2208/00115 , B01J2208/00407 , B01J2208/00557
摘要： The present invention discloses process and apparatus for the production of light olefins from their respective alkanes by catalytic dehydrogenation, where in the dehydrogenation reaction is carried out in multiple semi-continuously operated fluidized bed isothermal reactors, connected to a common regenerator and wherein the process is carried out in a sequence of steps in each cycle i.e., entry of hot regenerated catalyst, pre-treatment with reducing gas, dehydrogenation reaction, stripping, transfer of catalyst to regenerator and catalyst regeneration. Process cycle in each reactor starts at different times such that the catalyst inventory in the regenerator is invariable with time.
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公开(公告)号：US09908091B2
公开(公告)日：2018-03-06
申请号：US15059330
申请日：2016-03-03
申请人： Wolfgang Vogel , Rachid Mabrouk , Christoph Stiller , Stefan Hübner , Harald Ranke , Andreas Seliger
发明人： Wolfgang Vogel , Rachid Mabrouk , Christoph Stiller , Stefan Hübner , Harald Ranke , Andreas Seliger
CPC分类号： B01J8/067 , B01J8/062 , B01J2208/00168 , B01J2208/00407 , B01J2208/00415 , B01J2208/00504 , B01J2208/065 , C01B3/38 , C01B3/384 , C01B2203/0233 , C01B2203/0811 , C01B2203/0816 , C01B2203/085 , C01B2203/0866
摘要： A furnace for steam reforming a feed stream containing hydrocarbon, preferably methane, having: a combustion chamber, a plurality of reactor tubes arranged in the combustion chamber for accommodating a catalyst and for passing the feed stream through the reactor tubes, and at least one burner which is configured to burn a combustion fuel in the combustion chamber to heat the reactor tubes. In addition at least one voltage source is provided which is connected to the plurality of reactor tubes in such a manner that in each case an electric current which heats the reactor tubes to heat the feedstock is generable in the reactor tubes.
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公开(公告)号：US20180050986A1
公开(公告)日：2018-02-22
申请号：US15241562
申请日：2016-08-19
发明人： Reza KHANKAL , Henry HWU , Daniel M. HASENBERG , Christina M. BARRY , Mitchell D. REFVIK , Michael S. HANKINSON
IPC分类号： C07C319/06 , B01J8/02
CPC分类号： C07C319/06 , B01J8/0278 , B01J8/0285 , B01J2208/00407 , B01J2208/027 , C07C321/04
摘要： Disclosed herein are systems and processes involving the catalyzed cleavage reaction of dimethyl sulfide to methyl mercaptan. The catalyzed cleavage reaction can be a standalone system or process, or can be integrated with a methyl mercaptan production plant.
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6.发明申请公开(公告)号：US20180031527A1
公开(公告)日：2018-02-01
申请号：US15548835
申请日：2016-02-04
CPC分类号： G01N30/32 , B01J8/001 , B01J8/025 , B01J8/0278 , B01J8/067 , B01J19/2455 , B01J2208/00061 , B01J2208/00407 , B01J2208/00548 , B01J2208/00628 , B01J2208/027 , B01J2219/00033 , G01N30/68 , G01N2030/025 , G05D16/04
摘要： An on-line gas chromatography system for a fixed-bed continuous flow reactor and a method for on-line gas analysis of a catalytic reaction using the gas chromatography system. A reactor flow loop, a gas chromatogram, and a hydrostatic regulator are present in the gas chromatography system, wherein the reactor flow loop contains a fixed-bed reactor, a purge gas source, a feed gas source, and a by-pass line for reaction calibration.
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7.发明申请公开(公告)号：US20170002466A1
公开(公告)日：2017-01-05
申请号：US15125854
申请日：2015-03-05
申请人： HERAKLES
IPC分类号： C23C16/46 , B01J6/00 , B01J8/02 , C23C16/455 , F28F13/06 , F27B5/16 , F27D7/06 , F27D99/00 , F28F3/08 , C04B35/80 , C23C16/458
CPC分类号： C23C16/46 , B01J6/00 , B01J8/0285 , B01J2208/00407 , B01J2208/00415 , B01J2208/00433 , B01J2208/00469 , B01J2208/00884 , B01J2208/00938 , B01J2219/00006 , C04B35/80 , C04B2235/425 , C04B2235/5268 , C23C16/045 , C23C16/452 , C23C16/4557 , C23C16/45591 , C23C16/4583 , F27B5/16 , F27D7/06 , F27D99/0001 , F28C3/005 , F28D2021/0022 , F28F3/086 , F28F13/06
摘要： A thermochemical treatment installation includes a reaction chamber, at least one gas inlet, and a gas preheater chamber situated between the gas inlet and the reaction chamber. The preheater chamber has a plurality of perforated distribution trays held spaced apart one above another. The preheater chamber also includes, between at least the facing distribution trays, a plurality of walls defining flow paths for a gas stream between said trays.
摘要翻译： 热化学处理装置包括位于气体入口和反应室之间的反应室，至少一个气体入口和气体预热器室。 预热室具有多个彼此间隔开的多孔分布盘。 预热器室还包括在至少面对的分配盘之间的多个壁，其限定用于所述托盘之间的气流的流动路径。
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8.发明申请公开(公告)号：US20160288074A1
公开(公告)日：2016-10-06
申请号：US15059330
申请日：2016-03-03
申请人： Wolfgang Vogel , Rachid Mabrouk , Christoph Stiller , Stefan Hübner , Harald Ranke , Andreas Seliger
发明人： Wolfgang Vogel , Rachid Mabrouk , Christoph Stiller , Stefan Hübner , Harald Ranke , Andreas Seliger
CPC分类号： B01J8/067 , B01J8/062 , B01J2208/00168 , B01J2208/00407 , B01J2208/00415 , B01J2208/00504 , B01J2208/065 , C01B3/38 , C01B3/384 , C01B2203/0233 , C01B2203/0811 , C01B2203/0816 , C01B2203/085 , C01B2203/0866
摘要： A furnace for steam reforming a feed stream containing hydrocarbon, preferably methane, having: a combustion chamber, a plurality of reactor tubes arranged in the combustion chamber for accommodating a catalyst and for passing the feed stream through the reactor tubes, and at least one burner which is configured to burn a combustion fuel in the combustion chamber to heat the reactor tubes. In addition at least one voltage source is provided which is connected to the plurality of reactor tubes in such a manner that in each case an electric current which heats the reactor tubes to heat the feedstock is generable in the reactor tubes.
摘要翻译： 一种用于对含烃，优选甲烷的进料流进行蒸汽重整的炉，其具有：燃烧室，布置在所述燃烧室中用于容纳催化剂并使进料流通过反应器管的多个反应器管，以及至少一个燃烧器 其构造成在燃烧室中燃烧燃烧燃料以加热反应器管。 此外，提供了至少一个电压源，其以这样的方式连接到多个反应器管，即在每种情况下，加热反应器管以加热原料的电流在反应器管中是可生成的。
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公开(公告)号：US20160122264A1
公开(公告)日：2016-05-05
申请号：US14898849
申请日：2014-06-16
申请人： BASF SE
CPC分类号： C07C5/48 , B01J8/0496 , B01J8/065 , B01J8/067 , B01J19/249 , B01J23/28 , B01J23/92 , B01J38/02 , B01J2208/00053 , B01J2208/00061 , B01J2208/00115 , B01J2208/00176 , B01J2208/00212 , B01J2208/00221 , B01J2208/00407 , B01J2208/0053 , B01J2208/065 , B01J2219/2462 , B01J2219/2467 , B01J2219/2481 , C07C2523/18 , C07C2523/26 , C07C2523/28 , C07C2523/34 , C07C2523/745 , C07C2523/75 , C07C2523/755 , Y02P20/584 , C07C11/167
摘要： The invention relates to a method for producing 1,3 butadien by means of the oxidative dehydration of n-butenes on a heterogenous particulate multimetal oxide catalyst which contains molybdenum as the active compound and at least one other metal and which is filled into the contact tubes (KR) of two or more tube bundle reactors (R-I, R-II), wherein a heat transfer medium flows around the intermediate space between the contact tubes (KR) of the two or more tube bundle reactors (R-I, R-II). The method includes a production mode and a regeneration mode which are carried out in an alternating manner. In the production mode, an n-butene-containing feed flow is mixed with an oxygen-containing gas flow and conducted as a supply flow (1) over the heterogenous particulate multimetal oxide catalyst filled into the contact tubes (KR) of the two or more tube bundle reactors (R-I, R-II), and the heat transfer medium absorbs the released reaction heat, minus the heat quantity used to heat the supply flow (1) to the reaction temperature in the production mode, by means of an indirect heat exchange and completely or partly dispenses the reaction heat onto a secondary heat transfer medium (H2Oliq) in an external cooler (SBK). In the regeneration mode, the heterogenous particulate multimetal oxide catalyst is regenerated by conducting an oxygen-containing gas mixture (3) over the catalyst and burning off the deposits accumulated on the heterogenous particulate multimetal oxide catalyst. The invention is characterized in that the two or more tube bundle reactors (R-I, R-II) have a single heat transfer medium circuit and as many of the two or more tube bundle reactors (R-I, R-II) as necessary are operated constantly in the production mode so that the released reaction heat, minus the heat quantity used to heat the supply flow (1) to the reaction temperature in the production mode, suffices to keep the temperature of the heat transfer medium in the intermediate spaces between the content tubes (KR) of all the tube bundle reactors (R-I, R-II) at a constant level with a variation range of maximally +/−10 DEG C.
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公开(公告)号：US09314761B2
公开(公告)日：2016-04-19
申请号：US13122864
申请日：2009-10-08
申请人： Karl-Heinz Tetzlaff
发明人： Karl-Heinz Tetzlaff
CPC分类号： B01J8/1836 , B01J8/067 , B01J2208/00398 , B01J2208/00407 , B01J2208/00415 , C01B3/384 , C01B2203/0233 , C01B2203/085 , C01B2203/1011 , C01B2203/1058 , C01B2203/1235 , C01B2203/1241 , C01B2203/84
摘要： A method for the production of synthesis gas from gaseous hydrocarbons includes the use of allothermal steam reforming with catalysts. In order to produce the synthesis gas efficiently without exhaust gas in a compact apparatus, energy is at least partly supplied by electrical energy, that the energy is supplied by electrically heated contact surfaces and that the energy is supplied by contact surfaces within a fixed bed of catalyst pellets and/or within a fluidized bed at least partly consisting of catalyst particles.
摘要翻译： 用于从气态烃生产合成气的方法包括使用与催化剂进行的同热蒸汽重整。 为了在紧凑的装置中有效地生产合成气体而不排出废气，能量至少部分地由电能提供，能量由电加热的接触表面供应，并且能量由固定床内的接触表面供应 催化剂颗粒和/或在至少部分由催化剂颗粒组成的流化床内。
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