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公开(公告)号:WO2021203121A1
公开(公告)日:2021-10-07
申请号:PCT/US2021/070314
申请日:2021-03-25
Applicant: JOHNSON MATTHEY PUBLIC LIMITED COMPANY , FEDEYKO, Joseph
Inventor: BIDAL, Yannick , CHEN, Hai-Ying , HARRIS, Matthew , LU, Jing , GREENHAM, Neil
IPC: B01J23/42 , B01D53/94 , B01J29/76 , B01J29/78 , B01J35/00 , B01D2251/2062 , B01D2251/2067 , B01D2255/1021 , B01D2255/2073 , B01D2255/20761 , B01D2255/50 , B01D2255/504 , B01D2255/9022 , B01D2255/904 , B01D2255/9207 , B01D2257/404 , B01D2257/406 , B01D2258/012 , B01D53/9418 , B01D53/9436 , B01D53/9468 , B01J2229/62 , B01J29/44 , B01J29/763 , B01J29/783 , B01J29/80 , B01J35/0006 , B01J35/1014 , B01J35/1019 , B01J37/0244 , F01N2370/02 , F01N3/2066 , F01N3/28
Abstract: The invention relates to a catalytic article comprising a substrate having an inlet and an outlet; a first coating comprising a blend of: (1) platinum on a support, and (2) a first SCR catalyst comprising a Cu- and Mn- exchanged molecular sieve; and a second coating comprising a second SCR catalyst; wherein the support comprises at least one of a zeolite or a SiO2-Al2O3 mixed oxide. The platinum may be fixed on the support in solution.
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公开(公告)号:WO2020237200A1
公开(公告)日:2020-11-26
申请号:PCT/US2020/034353
申请日:2020-05-22
Applicant: POROCEL INDUSTRIES, LLC
Inventor: MCHUGH, Terence , SEAMANS, James , VISIOLI, Brian , KINCANNON, Pettus , THOMPSON, John, Wesley , ENDERLIN, Alexander
IPC: C10G70/02 , B01D53/50 , B01J23/85 , B01J23/92 , B01J23/94 , B01J38/12 , B01J38/62 , B01D2255/20746 , B01D2255/20753 , B01D2255/20769 , B01D2257/30 , B01D53/48 , B01D53/8603 , B01J21/04 , B01J23/882 , B01J23/883 , B01J35/023 , B01J35/1014 , B01J35/1019 , B01J35/1023 , B01J37/0036 , B01J37/0201 , B01J37/06 , B01J38/485 , C10G2300/202 , C10G2300/207 , C10G2300/4018 , C10G2300/703 , C10G45/08
Abstract: Disclosed herein are methods, systems, and compositions for providing catalysts for tail gas clean up in sulfur recovery operations. Aspects of the disclosure involve obtaining catalyst that was used in a first process, which is not a tailgas treating process and then using the so- obtained catalyst in a tailgas treating process. For example, the catalyst may originally be a hydroprocessing catalyst. A beneficial aspect of the disclosed methods and systems is that the re-use of spent hydroprocessing catalyst reduces hazardous waste generation by operators from spent catalyst disposal. Ultimately, this helps reduce the environmental impact of the catalyst life cycle. The disclosed methods and systems also provide an economically attractive source of high-performance catalyst for tailgas treatment, which benefits the spent catalyst generator, the catalyst provider, and the catalyst consumer.
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公开(公告)号:WO2022081415A2
公开(公告)日:2022-04-21
申请号:PCT/US2021/053978
申请日:2021-10-07
Applicant: EXXONMOBIL RESEARCH AND ENGINEERING COMPANY
Inventor: CHUN, Changmin , SATTLER, Wesley , GATT, Joseph, E. , HAJKOWSKI, Keith, R. , O'NEAL, Everett, J. , GUNTHER, William, R. , SKOULIDAS, Anastasios
IPC: B01J23/755 , B01J35/04 , B01J37/08 , B01J21/04 , C01B3/40 , B01J23/46 , B01J37/02 , B01J23/89 , B01J29/12 , B01J23/00 , B01J23/94 , B01J38/14 , B01J8/04 , B01J12/00 , B01J21/06 , B01J35/10 , B01J19/2485 , B01J21/066 , B01J2208/00017 , B01J2208/00548 , B01J23/002 , B01J23/005 , B01J23/10 , B01J23/464 , B01J29/106 , B01J29/74 , B01J35/0006 , B01J35/002 , B01J35/1009 , B01J35/1014 , B01J37/0215 , B01J37/038 , B01J37/04 , B01J37/082 , B01J38/12 , B01J8/008 , B01J8/0438 , B01J8/0492 , B01J8/0496 , C01B2203/0233 , C01B2203/0811 , C01B2203/1058 , C01B2203/1064 , C01B2203/1082 , C01B3/382 , C01B3/384 , C10G11/04 , C10G11/22 , C10G2300/70
Abstract: Catalyst systems are provided for reforming of hydrocarbons, along with methods for using such catalyst systems. The catalyst systems can be deposited or otherwise coated on a surface or structure, such as a monolith, to achieve improved activity and/or structural stability. The metal oxide support layer corresponds to a metal oxide support layer that is thermally phase stable at temperatures of 800°C to 1600°C, such as alpha-alumina. The catalyst systems can be beneficial for use in cyclical reaction environments, such as reverse flow reactors or other types of reactors that are operated using flows in opposing directions and different times within a reaction cycle, e.g. a catalyst system comprising nickel and alpha-alumina for cyclic methane reforming.
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公开(公告)号:WO2021127143A1
公开(公告)日:2021-06-24
申请号:PCT/US2020/065552
申请日:2020-12-17
Applicant: SAUDI ARABIAN OIL COMPANY , ARAMCO AMERICAS
Inventor: AL-ALLOUSH, Saeed , TAHA, Othman
IPC: C10G11/18 , B01J8/18 , B01J2208/00061 , B01J2208/0007 , B01J2208/00088 , B01J2208/00097 , B01J2208/00442 , B01J2208/00557 , B01J2208/00628 , B01J2208/00672 , B01J2208/00725 , B01J2208/00991 , B01J29/084 , B01J29/088 , B01J29/40 , B01J29/80 , B01J29/85 , B01J35/0026 , B01J35/023 , B01J35/1014 , B01J35/1019 , B01J35/1038 , B01J35/1042 , B01J8/0055 , B01J8/1809 , B01J8/1854 , B01J8/1881 , B01J8/26 , C10G11/187 , C10G2300/405 , C10G2300/70
Abstract: A method for fluid catalytic cracking (FCC) of petroleum oil feedstock includes reacting the petroleum oil feedstock with a catalyst mixture in a reaction zone of an FCC unit to obtain a product stream including desulfurized hydrocarbon product, unreacted petroleum oil feedstock, and spent catalyst. During the reacting a process control system develops a process model based on data collected during the reacting, the process model characterizing a relationship among the feed rate of the base cracking catalyst, the feed rate of the FCC additive, the operating conditions, the composition of the product stream, and emissions from the reaction; and one or more of (i) a target feed rate of the base cracking catalyst, (ii) a target feed rate of the FCC additive, and (iii) one or more target operating conditions of the reaction in the reaction zone to reduce the emissions from the FCC unit and to increase a yield of the desulfurized hydrocarbon product in the product stream are determined.
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公开(公告)号:WO2020146181A1
公开(公告)日:2020-07-16
申请号:PCT/US2020/012009
申请日:2020-01-02
Applicant: SAUDI ARABIAN OIL COMPANY , KOSEOGLU, Omer Refa , SAWAN, Ali
Inventor: KOSEOGLU, Omer Refa , SAWAN, Ali
IPC: C07C29/04 , B01J35/10 , C10G11/18 , C10G9/00 , C10L1/02 , B01J27/02 , B01J27/20 , B01J35/023 , B01J35/1014 , B01J35/1061 , B01J35/1066 , C10G2300/1096 , C10G2300/202 , C10G2300/307 , C10G2300/308 , C10G2300/4006 , C10G2300/4081 , C10G2400/04 , C10G2400/08 , C10G35/06 , C10G35/14 , C10G35/24 , C10G50/00 , C10G57/02 , C10L1/026 , C10L1/08
Abstract: A process for the production of middle distillates by the catalytically promoted hydration of olefmic compounds having a carbon number ranging from 7 to 14 to convert the olefins to the corresponding mixed alcohols having a higher boiling point that is in the diesel range, the process being conducted in a continuous stirred tank reactor, e.g., an ebullated-bed reactor, utilizing catalysts that include soluble homogeneous acidic compounds and solid heterogeneous compounds such as resins, and amorphous or structured metal oxides containing elements selected from IUPAC Groups 4-10, 13 and 14, and having Lewis or Bronsted acid sites.
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公开(公告)号:WO2022082119A2
公开(公告)日:2022-04-21
申请号:PCT/US2021/062626
申请日:2021-12-09
Applicant: EXXONMOBIL RESEARCH AND ENGINEERING COMPANY
Inventor: SATTLER, Wesley , HAJKOWSKI, Keith, R. , CHUN, Changmin , NANDI, Partha , GRANKINA, Vera , GATT, Joseph, E. , MA, Ning , SKOULIDAS, Anastasios , GUNTHER, William, R. , O'NEAL, Everett, J.
IPC: B01J23/755 , B01J35/04 , B01J37/08 , B01J21/04 , C01B3/40 , B01J23/46 , B01J37/02 , B01J23/00 , B01J23/94 , B01J38/14 , B01J8/04 , B01J12/00 , B01J35/10 , B01J19/2485 , B01J21/066 , B01J2208/00017 , B01J2208/00548 , B01J23/002 , B01J23/005 , B01J23/10 , B01J23/464 , B01J29/74 , B01J35/0006 , B01J35/1009 , B01J35/1014 , B01J37/0215 , B01J37/038 , B01J37/04 , B01J37/082 , B01J38/12 , B01J8/008 , B01J8/0438 , B01J8/0492 , B01J8/0496 , C01B2203/0233 , C01B2203/0811 , C01B2203/1058 , C01B2203/1064 , C01B2203/1082 , C01B3/382 , C01B3/384 , C10G11/04 , C10G11/22 , C10G2300/70
Abstract: Systems and methods are provided for using size-reversing materials in vessels where direct heating is used to at least partially provide heat for reforming reactions under cyclic reforming conditions. An example of a size-reversing material is the combination of NiO and AI2O3. It has been discovered that size-reversing materials can undergo a phase transition that can assist with re-dispersion of metal at elevated temperatures. This can assist with maintaining catalytic activity for reforming over longer time periods in the presence of cyclic reforming conditions.
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公开(公告)号:WO2021224806A2
公开(公告)日:2021-11-11
申请号:PCT/IB2021/053767
申请日:2021-05-05
Applicant: RELIANCE INDUSTRIES LIMITED
Inventor: GUPTA, Virendra Kumar , MAKWANA, Umesh , DESAI, Bhavesh Kiritbhai , VYAS, Priyanshu Bharatkumar , SHAH, Sanket Kirankumar , BHAJIWALA, Hiren Manojkumar , CHAUHAN, Sanjay Govindbhai
IPC: C08L23/00 , C08F4/00 , B01J21/063 , B01J21/10 , B01J35/023 , B01J35/1014 , B01J35/1076 , B01J37/0009
Abstract: The present disclosure relates to a process for preparation of a catalyst with a polyolefin coat. The process of the present disclosure is simple, economical and requires 50% less reaction time to obtain a desired catalyst with polyolefin coat. The catalyst obtained by the process of the present disclosure is capable of reducing generation of polymer fines by at least 50%, which leads to improved plant operability and throughput.
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公开(公告)号:WO2022269376A1
公开(公告)日:2022-12-29
申请号:PCT/IB2022/054105
申请日:2022-05-04
Applicant: CHEVRON U.S.A. INC.
Inventor: OUYANG, Xiaoying , KUPERMAN, Alexander E.
IPC: C10G49/04 , C10G45/08 , B01J23/887 , B01J23/888 , B01J21/06 , B01J37/03 , B01J35/10 , B01J37/00 , B01J37/20 , B01J21/063 , B01J23/8871 , B01J23/8877 , B01J23/8885 , B01J27/0515 , B01J35/0026 , B01J35/1014 , B01J35/1019 , B01J35/1038 , B01J35/1042 , B01J37/0009 , B01J37/0203 , B01J37/0205 , C10G47/06
Abstract: Multi-metallic bulk catalysts and methods for synthesizing the same are provided. The multi-metallic bulk catalysts contain nickel, molybdenum tungsten, yttrium, and optionally, copper, titanium and/or niobium. The catalysts are useful for hydroprocessing, particularly hydrodesulfurization and hydrodenitrogenation, of hydrocarbon feedstocks.
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公开(公告)号:WO2021260138A1
公开(公告)日:2021-12-30
申请号:PCT/EP2021/067395
申请日:2021-06-24
Applicant: BASF SE
Inventor: CHOI, Sung Yeun , KARPOV, Andrey , WALSDORFF, Christian , HUBACH, Patrick
IPC: B01J21/04 , B01J23/50 , B01J23/68 , B01J35/02 , B01J35/10 , B01J37/00 , B01J37/02 , B01J37/08 , B01J35/00 , C01F7/02 , C01F7/44 , C01G47/00 , C04B35/111 , C07D301/10 , B01J23/688 , B01J35/0026 , B01J35/023 , B01J35/026 , B01J35/1009 , B01J35/1014 , B01J35/1042 , B01J35/1061 , B01J35/108 , B01J37/0009 , B01J37/0072 , B01J37/0201
Abstract: A shaped catalyst body for producing ethylene oxide by gas-phase oxidation of ethylene, having a BET surface area in the range of 2 to 20 m2/g and comprising silver and a rhenium promotor deposited on a porous alpha-alumina catalyst support, characterized in that the support has a calcination history of at least 1460 °C. The catalyst support has a high surface area and little ethylene oxide isomerization and/or decomposition activity. The invention further relates to a porous alpha-alumina catalyst support having a BET surface area of 1.7 to 10 m2/g, the porous alpha-alumina catalyst support being obtainable by a) preparing a precursor material comprising a transition alumina and/or an alumina hydrate; b) forming the precursor material into shaped bodies; and c) calcining the shaped bodies at a temperature of 1460 °C to 1700 °C to obtain the porous alpha-alumina support. The invention also relates to a process for producing ethylene oxide by gas-phase oxidation of ethylene, comprising reacting ethylene and oxygen in the presence of a shaped catalyst body as described above.
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公开(公告)号:WO2021126514A1
公开(公告)日:2021-06-24
申请号:PCT/US2020/062672
申请日:2020-12-01
Applicant: EXXONMOBIL CHEMICAL PATENTS INC.
Inventor: BAI, Chuansheng , KHEIR, Ali, A. , METZGER, Eric, D. , DIAZ URRUTIA, Christian, A. , RUNGTA, Meha , ASLAM, Umar
IPC: B01J21/08 , B01J23/00 , B01J23/46 , B01J35/00 , B01J35/10 , B01J37/02 , B01J37/08 , B01J37/18 , B01J21/10 , B01J23/50 , B01J23/62 , C10G2/00 , B01J23/005 , B01J23/007 , B01J23/464 , B01J23/468 , B01J35/002 , B01J35/0066 , B01J35/1014 , B01J37/0201 , B01J37/0207 , B01J37/088 , C10G47/10
Abstract: Disclosed are catalyst compositions comprising two or more metal elements with high performances for selective alkyl-demethylation of C2+-hydrocarbyl-substituted aromatics, processes for making such catalyst compositions, and alkyl-demethylation processes using same. Also disclosed are preferred processes for making alkyl-demethylation catalyst compositions including a high-temperature calcination step, and preferred alkyl-demethylation processes having a high H2/HC molar ratio.
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