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公开(公告)号:US12048917B2
公开(公告)日:2024-07-30
申请号:US17463887
申请日:2021-09-01
申请人: SHELL OIL COMPANY
发明人: Opinder Kishan Bhan
IPC分类号: B01J23/883 , B01J8/18 , B01J31/06 , B01J35/64 , B01J35/69 , B01J37/00 , B01J37/04 , B01J37/08 , C10G45/08 , C10G45/20
CPC分类号: B01J23/883 , B01J8/1845 , B01J31/06 , B01J35/647 , B01J35/651 , B01J35/653 , B01J35/657 , B01J35/69 , B01J37/0027 , B01J37/04 , B01J37/082 , C10G45/08 , C10G45/20 , C10G2300/202 , C10G2300/308 , C10G2300/4006 , C10G2300/4012 , C10G2300/4018 , C10G2300/70
摘要: The specification discloses a highly macroporous catalyst for hydroprocessing and hydroconversion of heavy hydrocarbon feedstocks. The high macroporosity catalyst incudes an inorganic oxide, molybdenum, and nickel components. It has a pore structure such that at least 18% of its total pore volume is in pores of a diameter greater than 5,000 angstroms and at least 25% of its total pore volume is in pores of a diameter greater than 1,000 angstroms. Preferably, the pore structure is bimodal. The catalyst is made by co-mulling the catalytic components with a high molecular weight polyacrylamide followed by forming the co-mulled mixture into a particle or an extrudate. The particle or extrudate is dried and calcined under controlled calcination temperature conditions to yield a calcined particle or extrudate of the high macroporosity catalyst composition.
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公开(公告)号:US20240226859A1
公开(公告)日:2024-07-11
申请号:US18616525
申请日:2024-03-26
发明人: Amir Sabahi , Eswaramoorthi Iyyamperumal , Nataly G. Vargas , William Knowles , Andrew Loebl , Julie Francis
IPC分类号: B01J29/08 , B01J6/00 , B01J29/00 , B01J29/06 , B01J29/40 , B01J29/65 , B01J29/70 , B01J29/80 , B01J35/23 , B01J35/63 , B01J35/64 , B01J35/66 , B01J35/69 , B01J37/00 , B01J37/03 , B01J37/06 , B01J37/10 , B01J37/28 , B01J37/30 , C10G11/05 , C10G11/18
CPC分类号: B01J29/088 , B01J6/001 , B01J29/005 , B01J29/06 , B01J29/061 , B01J29/085 , B01J29/70 , B01J29/7038 , B01J29/7049 , B01J29/7057 , B01J29/80 , B01J35/23 , B01J35/63 , B01J35/647 , B01J35/66 , B01J35/69 , B01J37/0009 , B01J37/0045 , B01J37/036 , B01J37/038 , B01J37/06 , B01J37/10 , B01J37/28 , B01J37/30 , C10G11/05 , C10G11/18 , B01J2029/062 , B01J29/40 , B01J29/65 , B01J29/7007 , B01J29/7042 , B01J2229/186 , B01J2229/36 , B01J2229/42 , C07C2527/14 , C07C2527/16 , C07C2527/167 , C07C2527/18 , C07C2527/182 , C07C2529/06 , C07C2529/08 , C07C2529/40 , C07C2529/70
摘要: Process for the preparation of a catalyst by adding, clay, boehmite, a first silica to form a slurry, digesting the slurry with a monoprotic acid to a pH of less than 4, adding one or more zeolites, adding a rare earth component to the slurry and mixing, adjusting the slurry pH to below 4 with monoprotic acid, adding a second silica anywhere in the preceding steps, destabilizing the slurry by raising the pH, shaping and collecting the resulting catalyst, wherein the resulting catalyst has enhanced mesoporosity.
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公开(公告)号:US20240360370A1
公开(公告)日:2024-10-31
申请号:US18308123
申请日:2023-04-27
发明人: Aaron Chi Akah , Ziyauddin Qureshi , Abdullah Mohammed Aitani , Mohammed Abdul Bari Siddiqui , Musaed Salem Al-Ghrami , Mansour Ali Al-Herz , Qi Xu , Abdulkadir Tanimu
CPC分类号: C10G11/20 , B01J29/084 , B01J29/40 , B01J29/7007 , B01J35/19 , B01J35/40 , B01J35/615 , B01J35/617 , B01J35/618 , B01J35/633 , B01J35/647 , B01J35/651 , B01J35/69
摘要: A process for converting a hydrocarbon feed includes contacting a hydrocarbon feed with steam in the presence of a cracking catalyst under steam enhanced catalytic cracking conditions. The contacting the hydrocarbon feed with the steam in the presence of the cracking catalyst causes at least a portion of the hydrocarbon feed to undergo steam catalytic cracking reactions to produce a cracked effluent comprising C2 to C4 olefins, C6 to C10 aromatic compounds, or both. The cracking catalyst is a nanoparticle. The nanoparticle has a core and a shell. The core includes at least one zeolite particle, where the at least one zeolite particle includes ZSM-5 zeolites, Beta zeolites, Y-zeolites, or combinations of these zeolites. The shell is mesoporous and incudes silica (SiO2), alumina (Al2O3), or silica and alumina.
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公开(公告)号:US12023657B2
公开(公告)日:2024-07-02
申请号:US17240703
申请日:2021-04-26
发明人: Philip Nubel
IPC分类号: B01J29/40 , B01J29/42 , B01J29/48 , B01J35/40 , B01J35/61 , B01J35/64 , B01J35/69 , B01J37/08 , C01B39/02 , C07C5/22 , C07C5/27 , C07C15/08 , B01J29/04 , B01J35/66
CPC分类号: B01J29/405 , B01J29/40 , B01J29/42 , B01J29/48 , B01J35/40 , B01J35/613 , B01J35/615 , B01J35/643 , B01J35/647 , B01J35/69 , B01J37/08 , C01B39/026 , C07C5/222 , C07C5/2737 , C07C5/2775 , C07C15/08 , B01J29/041 , B01J29/042 , B01J29/045 , B01J35/66 , B01J2229/10 , B01J2229/16 , B01J2229/20 , B01J2229/37 , B01J2229/38 , B01J2229/40 , C07C2529/40 , C07C2529/48 , Y02P20/52 , C07C5/2737 , C07C15/08 , C07C5/2775 , C07C15/08
摘要: A method of making a xylene isomerization catalyst comprises the steps of (i) contacting a ZSM-5 zeolite starting material having a silica to alumina molar ratio of 20 to 50 and having a mesopore surface area in the range of 50 m2/gram to 200 m2/gram in a reactor with a base to provide an intermediate zeolite material; (ii) recovering the intermediate ZSM-5 zeolite material of step (i); (iii) contacting the intermediate zeolite material with an acid to provide an acid treated ZSM-5 zeolite product; (iv) recovering the acid treated ZSM-5 zeolite material; and (v) calcining the acid treated ZSM-5 zeolite material to provide a desilicated ZSM-5 zeolite product having a silica to alumina molar ratio of 20 to 150 and having a mesopore surface area in the range of 100 m2/gram to 400 m2/gram.
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公开(公告)号:US20240157344A1
公开(公告)日:2024-05-16
申请号:US18507197
申请日:2023-11-13
申请人: SHELL USA, INC.
发明人: Opinder Kishan Bhan
IPC分类号: B01J23/883 , B01J8/18 , B01J31/06 , B01J35/64 , B01J35/69 , B01J37/00 , B01J37/04 , B01J37/08 , C10G45/08 , C10G45/20
CPC分类号: B01J23/883 , B01J8/1845 , B01J31/06 , B01J35/647 , B01J35/651 , B01J35/653 , B01J35/657 , B01J35/69 , B01J37/0027 , B01J37/04 , B01J37/082 , C10G45/08 , C10G45/20 , C10G2300/202 , C10G2300/308 , C10G2300/4006 , C10G2300/4012 , C10G2300/4018 , C10G2300/70
摘要: The specification discloses a highly macroporous catalyst for hydroprocessing and hydroconversion of heavy hydrocarbon feedstocks. The high macroporosity catalyst incudes an inorganic oxide, molybdenum, and nickel components. It has a pore structure such that at least 18% of its total pore volume is in pores of a diameter greater than 5,000 angstroms and at least 25% of its total pore volume is in pores of a diameter greater than 1,000 angstroms. Preferably, the pore structure is bimodal. The catalyst is made by co-mulling the catalytic components with a high molecular weight polyacrylamide followed by forming the co-mulled mixture into a particle or an extrudate. The particle or extrudate is dried and calcined under controlled calcination temperature conditions to yield a calcined particle or extrudate of the high macroporosity catalyst composition.
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