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公开(公告)号:US12162817B2
公开(公告)日:2024-12-10
申请号:US17265054
申请日:2019-07-30
Applicant: Archer Daniels Midland Company
Inventor: James Brazdil , Chi-Cheng Ma
IPC: C07C213/02 , B01J25/02 , B01J29/068 , B01J29/072 , B01J29/14 , B01J29/76
Abstract: Improvements in catalyst systems and associated processes for the conversion of glycolaldehyde to monoethanolamine are disclosed. The catalyst systems exhibit improved selectivity to this desired product and consequently reduced selectivity to byproducts such as diethanolamine and ethylene glycol. These beneficial effects are achieved through the use of acids, and particularly Lewis acids, as co-catalysts of the reductive amination reaction, in conjunction with a hydrogenation catalyst.
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公开(公告)号:US11891347B2
公开(公告)日:2024-02-06
申请号:US17584610
申请日:2022-01-26
Applicant: Exelus Inc.
Inventor: Mitrajit Mukherjee , Eric Daniel Gauthier , Kelly Ann Coley
IPC: B01J29/06 , C07C2/58 , B01J29/08 , B01J29/70 , B01J37/30 , B01J37/02 , C01B39/20 , C01B39/02 , C01B39/46 , C10G29/20 , B01J29/90 , B01J29/12 , B01J38/10 , B01J29/74 , C07C2/56 , C07C2/54 , C07C9/14 , C07C9/16 , B01J29/14 , B01J37/08 , C10G99/00
CPC classification number: C07C2/58 , B01J29/08 , B01J29/082 , B01J29/084 , B01J29/087 , B01J29/088 , B01J29/123 , B01J29/126 , B01J29/143 , B01J29/7007 , B01J29/7057 , B01J29/7407 , B01J29/90 , B01J37/0201 , B01J37/024 , B01J37/08 , B01J37/30 , B01J38/10 , C01B39/026 , C01B39/20 , C01B39/46 , C07C2/54 , C07C2/56 , C07C9/14 , C07C9/16 , C10G29/205 , B01J2229/10 , B01J2229/18 , B01J2229/186 , B01J2229/20 , B01J2229/40 , C07C2529/08 , C07C2529/12 , C07C2529/14 , C07C2529/70 , C10G99/00 , C10G2300/104 , C10G2300/1081 , C10G2300/1092 , C10G2300/305 , C10G2300/70 , C10G2400/02 , Y02P20/584 , C07C2/58 , C07C9/16
Abstract: Improved alkylation catalysts, alkylation methods, and methods of making alkylation catalysts are described. The alkylation method comprises reaction over a solid acid, zeolite-based catalyst and can be conducted for relatively long periods at steady state conditions. The alkylation catalyst comprises a crystalline zeolite structure, a Si/Al molar ratio of 20 or less, less than 0.5 weight percent alkali metals, and further having a characteristic catalyst life property. Some catalysts may contain rare earth elements in the range of 10 to 35 wt %. One method of making a catalyst includes a calcination step following exchange of the rare earth element(s) conducted at a temperature of at least 575° C. to stabilize the resulting structure followed by an deammoniation treatment. An improved method of deammoniation uses low temperature oxidation.
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公开(公告)号:US11801498B2
公开(公告)日:2023-10-31
申请号:US17805494
申请日:2022-06-06
Inventor: Albert M. Tsybulevski , Eduardo Bolivar , Alexander Avraamovich Greish , Leonid Modestovich Kustov
CPC classification number: B01J29/143 , B01D53/8609 , B01J29/087 , B01J29/103 , B01J29/163 , B01J35/023 , B01J35/04 , B01D2255/50 , B01D2257/302 , B01D2258/0283
Abstract: The present invention relates to the catalytic processes for rendering harmless the flue gases of the power stations or more precisely to the catalysts for sulfur oxides reduction to elemental sulfur. The novel catalyst presents the binary polycations of copper and zinc or copper and manganese incorporated into the low silica faujasite X (LSX) having transition metals ratio Cu:Zn or Cu:Mn in the range of 2:1 to 4:1.
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公开(公告)号:US11439992B2
公开(公告)日:2022-09-13
申请号:US16899138
申请日:2020-06-11
Applicant: BASF Corporation
Inventor: Qi Fu , Barbara Slawski , Peter Pfab
IPC: B01J29/72 , C01B39/02 , B01J29/76 , B01J29/072 , B01D53/94 , B01J35/04 , B01J37/02 , B01J29/14 , B01J37/30 , F01N3/10 , F01N3/20
Abstract: The present disclosure relates to processes for formation of a molecular sieve, particularly a metal-promoted molecular sieve, and more particularly an Iron(III) exchanged zeolite. Preferably, the zeolite is of the chabazite form or similar structure. The processes can include combining a zeolite with Iron(III) cations in an aqueous medium. The process can be carried out at a pH of less than about 7, and a buffering material can be used with the aqueous medium. The processes beneficially result in Iron exchange that can approach 100% along with removal of cations (such as sodium, NH4, and H) from the zeolite. An Iron(III)-exchanged zeolite prepared according to the disclosed processes can include about 2,000 ppm or less of cation and about 1% by weight or greater of Iron(III). The disclosure also provides catalysts (e.g., SCR catalysts) and exhaust treatment systems including the Iron(III)-exchanged zeolite.
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公开(公告)号:US20220144724A1
公开(公告)日:2022-05-12
申请号:US17584610
申请日:2022-01-26
Applicant: Exelus Inc.
Inventor: Mitrajit Mukherjee , Eric Daniel Gauthier , Kelly Ann Coley
IPC: C07C2/58 , B01J29/08 , B01J29/70 , B01J37/30 , B01J37/02 , C01B39/20 , C01B39/02 , C01B39/46 , C10G29/20 , B01J29/90 , B01J29/12 , B01J38/10 , B01J29/74 , C07C2/56 , C07C2/54 , C07C9/14 , C07C9/16 , B01J29/14 , B01J37/08
Abstract: Improved alkylation catalysts, alkylation methods, and methods of making alkylation catalysts are described. The alkylation method comprises reaction over a solid acid, zeolite-based catalyst and can be conducted for relatively long periods at steady state conditions. The alkylation catalyst comprises a crystalline zeolite structure, a Si/Al molar ratio of 20 or less, less than 0.5 weight percent alkali metals, and further having a characteristic catalyst life property. Some catalysts may contain rare earth elements in the range of 10 to 35 wt %. One method of making a catalyst includes a calcination step following exchange of the rare earth element(s) conducted at a temperature of at least 575° C. to stabilize the resulting structure followed by an deammoniation treatment. An improved method of deammoniation uses low temperature oxidation.
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公开(公告)号:US20220088582A1
公开(公告)日:2022-03-24
申请号:US17477768
申请日:2021-09-17
Inventor: Ananth Kishore Kumar Sontyana , Nikita Sharma , Shivanand Mukund Pai , Bharat Lakshman Newalkar , Kamal Kishore Pant
IPC: B01J37/02 , B01J37/08 , B01J37/04 , B01J37/00 , B01J21/04 , B01J23/755 , B01J29/14 , B01J37/16 , B01J8/02 , C07C2/84 , C07C7/04 , C07C5/367
Abstract: An aspect of the present disclosure relates to a process for preparing a composite hydroalkylation catalyst including: (a) effecting impregnation of a hydrogenation metal on an inorganic oxide to form a metal impregnated inorganic oxide; (b) effecting calcination of the metal impregnated inorganic oxide to obtain a calcined metal impregnated inorganic oxide; (c) preparing a composite mixture comprising a molecular sieve, the calcined metal impregnated inorganic oxide and a binder; (d) preparing an extruded catalyst; and (e) effecting calcination of the extruded catalyst to obtain the composite hydroalkylation catalyst. The composite hydroalkylation catalyst prepared using this process affords dramatic improvement in conversion of mononuclear aromatic hydrocarbon and the yield of the hydroalkyled mononuclear aromatic hydrocarbon (e.g. CHB).
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公开(公告)号:US20210309604A1
公开(公告)日:2021-10-07
申请号:US17265054
申请日:2019-07-30
Applicant: Archer Daniels Midland Company
Inventor: James Brazdil , Chi-Cheng Ma
IPC: C07C213/02 , B01J29/76 , B01J29/068 , B01J29/072 , B01J29/14 , B01J25/02
Abstract: Improvements in catalyst systems and associated processes for the conversion of glycolaldehyde to monoethanolamine are disclosed. The catalyst systems exhibit improved selectivity to this desired product and consequently reduced selectivity to byproducts such as diethanolamine and ethylene glycol. These beneficial effects are achieved through the use of acids, and particularly Lewis acids, as co-catalysts of the reductive amination reaction, in conjunction with a hydrogenation catalyst.
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公开(公告)号:US20210189266A1
公开(公告)日:2021-06-24
申请号:US16721361
申请日:2019-12-19
Applicant: Saudi Arabian Oil Company
Inventor: Omer Refa KOSEOGLU
Abstract: The processes and systems herein integrate hydroprocessing and coking in a manner to effectively upgrade/desulfurize crude oil feedstocks. An initial liquid hydrocarbon feedstock, such as crude oil, is upgraded by fractionating both the hydrocarbon feedstock and coker thermally cracked hydrocarbon products in a fractionating zone. A coker recycle stream is thermally cracked to produce coker thermally cracked hydrocarbon products that are passed to the fractionating zone. The hydrocarbon distillates are hydroprocessed under conditions effective for desulfurization and conversion into lighter hydrocarbon distillates to produce a hydroprocessed liquid hydrocarbon effluent, such as a bottomless synthetic crude oil.
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公开(公告)号:US20210162387A1
公开(公告)日:2021-06-03
申请号:US17167280
申请日:2021-02-04
Applicant: Furukawa Electric Co., Ltd.
Inventor: Sadahiro KATO , Masayuki FUKUSHIMA , Hiroko TAKAHASHI , Yuichiro BANBA , Kaori SEKINE , Takao MASUDA , Yuta NAKASAKA , Takuya YOSHIKAWA
IPC: B01J29/89 , B01J23/46 , B01J23/44 , B01J23/42 , B01J23/745 , B01J23/75 , B01J23/755 , B01J35/00 , B01J35/10 , B01J37/02 , B01J37/10 , B01J37/00 , B01J29/12 , B01J29/14
Abstract: A catalyst structure includes a carrier having a porous structure composed of a zeolite type compound and at least one catalytic material existing in the carrier. The carrier has channels communicating with each other, and the catalytic material is a metal fine particle and exists at least in the channel of the carrier.
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公开(公告)号:US10800691B2
公开(公告)日:2020-10-13
申请号:US15309593
申请日:2015-05-06
Applicant: Hindustan Petroleum Corporation Ltd
Inventor: Ramesh Kanaparthi , Peddy Venkat Chalapathi Rao , Nettem Choudary Venkateswarlu , Sriganesh Gandham
IPC: B01J23/00 , B01J23/72 , B01J23/75 , B01J27/02 , B01J29/14 , C02F1/66 , C02F1/72 , C02F11/08 , C02F101/10 , C02F103/36
Abstract: The present subject matter relates to the development of active catalyst composite based on supported transition metal oxides, especially, Cu, Co that are effective in the removal sulfides in the diluted spent caustic. The process for the reduction of sulfides in spent caustic comprises of reacting various organic and inorganic sulfides with molecular oxygen in the presence of active catalyst at various reaction temperatures ranging ambient to 200° C. and pressures between atmospheric pressure to 60 bars. The process also relates to complete scheme for the removal of sulfides in spent caustic.
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