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21.
公开(公告)号:US11654421B2
公开(公告)日:2023-05-23
申请号:US16947701
申请日:2020-08-13
发明人: Chuansheng Bai , Majosefina Cunningham , Jihad M. Dakka , Preeti Kamakoti , Aruna Ramkrishnan , Anjaneya S. Kovvali , Anita S. Lee
IPC分类号: B01J23/80 , C07C41/01 , B01J37/04 , B01J37/03 , B01J37/30 , B01J37/00 , B01J37/08 , B01J37/34 , B01J37/06 , B01J37/02 , B01J37/18 , B01J35/00 , B01J35/02 , B01J35/10 , B01J21/18
CPC分类号: B01J23/80 , B01J21/18 , B01J35/0013 , B01J35/026 , B01J35/1014 , B01J35/1019 , B01J35/1038 , B01J35/1042 , B01J35/1047 , B01J35/1061 , B01J37/0036 , B01J37/0236 , B01J37/031 , B01J37/04 , B01J37/06 , B01J37/088 , B01J37/18 , B01J37/30 , B01J37/348 , C07C41/01
摘要: Methods of producing metal catalysts can include mixing two or more metal salts and an aluminum salt in water to produce a metal catalyst precursor solution; mixing the metal catalyst precursor solution and an alkali metal buffer solution to produce a precipitate; ion exchanging the alkali metal in the precipitate for a non-alkali cation to produce a low-alkali metal precipitate comprising 3 wt % or less alkali metal by weight of the precipitate on a dry basis; producing a powder from the low-alkali metal precipitate; and calcining the powder to produce a metal catalyst. Such metal catalysts may be useful in producing bifunctional catalyst systems that are useful in, among other things, converting syngas to dimethyl ether in a single reactor.
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22.
公开(公告)号:US11623868B2
公开(公告)日:2023-04-11
申请号:US17250534
申请日:2019-08-02
申请人: BASF SE
发明人: Hannah Schreyer , Andrei-Nicolae Parvulescu , Ulrich Mueller , Christian Riemann , Ralf Boehling , Christoph Schappert , Bernd Hinrichsen , Stefan Dumser , Stefanie Clade
IPC分类号: B01J29/76 , C01B39/48 , B01D53/86 , B01D53/94 , B01J37/00 , B01J37/04 , B01J37/06 , B01J37/10 , B01J37/30 , B01J39/02 , B01J39/14
摘要: Disclosed herein is a continuous process for preparing zeolitic material with a CHA-type framework structure comprising SiO2 and X2O3 and the zeolitic material so-obtained. The processes comprises (i) preparing a mixture comprising one or more sources of SiO2, one or more sources of X2O3, seed crystals, one or more tetraalkylammonium cation R5R6R7R8N+-containing compounds as structure directing agent, and a liquid solvent system; (ii) continuously feeding the mixture prepared in (i) into a continuous flow reactor at a liquid hourly space velocity; and (iii) crystallizing the zeolitic material with a CHA-type framework structure from the mixture in the continuous flow reactor.
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公开(公告)号:US11590481B2
公开(公告)日:2023-02-28
申请号:US17349989
申请日:2021-06-17
摘要: Provided herein are methods for hydroisomerization of a hydrocarbon feedstock comprising contacting the hydrocarbon feedstock with hydrogen and a catalyst to yield a hydrocarbon product having an increase in branched hydrocarbons relative to the hydrocarbon feedstock. The present catalysts comprise a heteroatom-doped Beta zeolite having a trivalent cation as a framework metal oxide, an extra-framework species comprised of cerium and/or cobalt, and from 0.01 to 1.5 wt. % of a group VIII or VIB metal, or a combination thereof.
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公开(公告)号:US11529620B2
公开(公告)日:2022-12-20
申请号:US17057970
申请日:2019-06-18
申请人: BASF SE
发明人: Andrei-Nicolae Parvulescu , Robert McGuire , Ulrich Mueller , Xiangju Meng , Feng-Shou Xiao , Toshiyuki Yokoi , Dirk De Vos , Bernd Marler , Hermann Gies , Ute Kolb , Weiping Zhang
IPC分类号: C01B39/02 , B01J29/76 , B01D53/94 , B01J35/10 , B01J37/04 , B01J37/06 , B01J37/08 , B01J37/30 , C01B39/48
摘要: The present invention relates to a process for the preparation of a zeolitic material SiO2 and X2O3 in its framework structure, wherein X stands for a trivalent element, wherein said process comprises interzeolitic conversion of a first zeolitic material comprising SiO2 and X2O3 in its framework structure, wherein the first zeolitic material has an FER-, TON-, MTT-, BEA-, MEL-, MWW-, MFS-, and/or MFI-type framework structure to a second zeolitic material comprising SiO2 and X2O3 in its framework structure, wherein the second zeolitic material obtained in (2) has a different type of framework structure than the first zeolitic material. Furthermore, the present invention relates to a zeolitic material per se as obtainable and/or obtained according to the inventive process and to its use, in particular as a molecular sieve, as an adsorbent, for ion-exchange, or as a catalyst and/or as a catalyst support.
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公开(公告)号:US20220348529A1
公开(公告)日:2022-11-03
申请号:US17410322
申请日:2021-08-24
申请人: HYUNDAI MOTOR COMPANY , Kia Corporation , Research & Business Foundation SUNGKYUNKWAN UNIVERSITY
发明人: Chae Hwan HONG , Jin Woo CHOUNG , Young Gul HUR , Jong Wook BAE , Hyun Seung JUNG , Xu WANG
摘要: A method of preparing a catalyst for synthesizing dimethyl ether from synthetic gas includes preparing a mesoporous ferrierite zeolite (FER), and co-precipitating a precursor of a mesoporous ferrierite zeolite and a Cu—Zn—Al-based oxide (CZA) to obtain a hybrid CZA/mesoFER catalyst.
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公开(公告)号:US11471862B2
公开(公告)日:2022-10-18
申请号:US16613760
申请日:2018-05-16
申请人: BASF CORPORATION
IPC分类号: B01J29/08 , B01J21/04 , B01J21/16 , B01J23/10 , B01J35/08 , B01J37/10 , B01J37/30 , C10G11/05 , C10G11/18
摘要: A microspherical fluid catalytic cracking (FCC) catalyst includes Y zeolite and a gamma-alumina.
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公开(公告)号:US11447432B2
公开(公告)日:2022-09-20
申请号:US16470321
申请日:2017-12-19
申请人: GASOLFIN B.V.
摘要: The invention is directed to a process to prepare propylene from a hydrocarbon feed comprising pentane by contacting the hydrocarbon feed with a heterogeneous cracking catalyst as present in one or more fixed beds thereby obtaining a cracked effluent. The heterogeneous catalyst comprises a matrix component and a molecular sieve comprising framework alumina, framework silica and a framework metal selected from the group of Zn, Fe, Ce, La, Y, Ga and/or Zr. Propylene is isolated from the cracked effluent.
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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
申请人: BASF Corporation
发明人: Qi Fu , Barbara Slawski , Peter Pfab
IPC分类号: B01J29/72 , C01B39/02 , B01J29/76 , B01J29/072 , B01D53/94 , B01J35/04 , B01J37/02 , B01J29/14 , B01J37/30 , F01N3/10 , F01N3/20
摘要: 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:US11427516B2
公开(公告)日:2022-08-30
申请号:US16952183
申请日:2020-11-19
申请人: Jiangnan University
发明人: Xiaohao Liu , Yuebing Xu , Feng Jiang , Bing Liu , Dapeng Liu , Ting Wang
IPC分类号: C07C1/04 , B01J35/00 , B01J37/02 , B01J37/06 , B01J21/08 , B01J23/78 , B01J21/04 , B01J29/064 , B01J37/03 , B01J37/00 , B01J37/08 , B01J37/30 , B01J23/889
摘要: The present disclosure discloses a multistage nanoreactor catalyst and preparation and application thereof, belonging to the technical field of synthesis gas conversion. The catalyst consists of a core of an iron-based Fischer-Tropsch catalyst, a transition layer of a porous oxide or porous carbon material, and a shell layer of a molecular sieve having an aromatization function. The molecular sieve of the shell layer can be further modified by a metal element or a non-metal element, and the outer surface of the molecular sieve is further modified by a silicon-oxygen compound to adjust the acidic site on the outer surface and the aperture of the molecular sieve, thereby inhibiting the formation of heavy aromatic hydrocarbons. According to the disclosure, the shell layer molecular sieve with a transition layer and a shell layer containing or not containing auxiliaries, and with or without surface modification can be prepared by the iron-based Fischer-Tropsch catalyst through multiple steps. The catalyst can be used for direct preparation of aromatic compounds, especially light aromatic compounds, from synthesis gas; the selectivity of light aromatic hydrocarbons in hydrocarbons can be 75% or above, and the content in the liquid phase product is not less than 95%; and the catalyst has good stability and good industrial application prospect.
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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
申请人: Exelus Inc.
IPC分类号: 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
摘要: 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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