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公开(公告)号:US11724973B2
公开(公告)日:2023-08-15
申请号:US17790243
申请日:2020-12-17
Applicant: SABIC Global Technologies B.V.
Inventor: Vijay Dinkar Bodas , Guillermo Canelon Leal , Mohammed B. Ansari , Sami Al Mutairi
IPC: C07C5/27
CPC classification number: C07C5/2724 , C07C2523/42
Abstract: A method for processing pentanes obtained from a DIB unit is disclosed. The process can include separating a first stream containing pentanes obtained from a DIB unit, in a separation column to obtain a second stream comprising iso-pentane and a third stream comprising n-pentane and neo-pentane; and subjecting the third stream to a butane isomerization unit producing a fourth stream containing iso-pentane, n-pentane, and neo-pentane.
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公开(公告)号:US11358916B2
公开(公告)日:2022-06-14
申请号:US17047001
申请日:2019-04-23
Applicant: SABIC Global Technologies B.V.
Inventor: Vijay Dinkar Bodas , Sultan Al-Otaibe , Guillermo Leal , Mohammed Bismillah Ansari
Abstract: Described is a process for producing field butane. The process includes increasing the n-butane concentration in field butane. The process may include a concentration process that includes distillation and a thermal cracking process.
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公开(公告)号:US11124470B2
公开(公告)日:2021-09-21
申请号:US16496511
申请日:2018-03-29
Applicant: SABIC Global Technologies B.V.
Inventor: Guillermo Leal , Mohammed Bismillah Ansari , Vijay Dinkar Bodas
Abstract: A method of producing methyl tertiary butyl ether (MTBE) and propylene is disclosed. The method involves the use of a crude C4 stream and the integration of a MTBE synthesis process and a cracking process. The method may include processing a byproduct stream from an MTBE synthesis unit to produce high purity olefin streams for an olefins conversion technology unit.
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公开(公告)号:US12037313B2
公开(公告)日:2024-07-16
申请号:US17292261
申请日:2019-11-20
Applicant: SABIC Global Technologies B.V.
Inventor: Vijay Dinkar Bodas , Guillermo Leal , Mohammed Bismillah Ansari
CPC classification number: C07C41/06 , C07C4/02 , C07C5/05 , C07C5/32 , C07C5/42 , C07C7/04 , C07C29/04 , C07C6/04 , C07C7/04 , C07C9/10 , C07C7/04 , C07C9/12 , C07C5/05 , C07C11/08 , C07C41/06 , C07C43/046 , C07C29/04 , C07C31/12 , C07C7/04 , C07C11/08 , C07C5/32 , C07C11/04 , C07C5/32 , C07C11/09 , C07C5/42 , C07C11/09 , C07C4/02 , C07C11/04
Abstract: A process for producing ethylene and at least one of butanol and an alkyl tert-butyl ether from field butane includes separating the field butane into an n-butane stream and an isobutane stream; cracking the n-butane stream to obtain a cracked product stream comprising n-butane, 1-butene, 2-butene, butadienes, or a combination comprising at least one of the foregoing; and at least one of the following: (1) separating the cracked product stream to obtain a butane stream and a butene stream, and reacting the butene stream with water to obtain a fuel additive comprising butanol, and (2) dehydrogenating the isobutane stream in a dehydrogenation unit to form an isobutene stream and reacting the isobutene stream with an aliphatic alcohol to produce an alkyl tert-butyl ether.
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公开(公告)号:US11161796B2
公开(公告)日:2021-11-02
申请号:US17264430
申请日:2019-09-16
Applicant: SABIC Global Technologies B.V.
Inventor: Guillermo Leal , Mohammed Bismillah Ansari , Vijay Dinkar Bodas , Sultan Eid Al-Otaibi , Mohammed A. Al-Ghamdi , Naif Mohammed Al-Naddah Al-Otaibi
Abstract: A method for the production of a fuel additive includes passing a hydrocarbon stream comprising crude mixed C4 hydrocarbons through a first hydrogenation unit to produce a first product stream; passing the first product stream from the first hydrogenation unit to a methyl tert-butyl ether synthesis unit forming methyl tert-butyl ether and a byproduct stream; passing the byproduct stream through a first distillation unit to separate the byproduct stream into a first 1-butene stream, an isobutane stream, and a 2-butene and n-butane stream; forming a second product stream by passing the 2-butene and n-butane stream to a selective conversion unit; passing the second product stream into a second distillation unit to form an n-butane stream and a second 1-butene stream; passing the second 1-butene stream to a fuel additive production unit; and passing the first 1-butene stream to the fuel additive production unit to form the fuel additive.
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公开(公告)号:US10829706B2
公开(公告)日:2020-11-10
申请号:US16631100
申请日:2018-07-17
Applicant: SABIC Global Technologies B.V.
Inventor: Vijay Dinkar Bodas , Sultan Eid Al-Otaibi , Guillermo Leal , Mohammed Bismillah Ansari , Naif Mohammed Al Naddah Al-Otaibi
Abstract: A method of manufacturing a cetane-boosting fuel additive includes reacting formaldehyde and 2-ethylhexanol at a mole ratio of 10:1 to 1:1, or 5:1 to 1.5:1, or 4:1 to 2:1, or 3.5:1 to 2.5:1 in the presence of a heterogeneous acid catalyst at a temperature of 300 to 375° K to obtain a cetane-boosting product mixture comprising H3C(CH2)3CH(CH2CH3)CH2(OCH2)nOH, H3C(CH2)3CH(CH2CH3)CH2(OCH2)nOCH2CH(CH2CH3)(CH2)3CH3, or a combination thereof, wherein n has an average value of 2.8 to 3.2, preferably an average value of 3.
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公开(公告)号:US20200157444A1
公开(公告)日:2020-05-21
申请号:US16631100
申请日:2018-07-17
Applicant: SABIC Global Technologies B.V.
Inventor: Vijay Dinkar Bodas , Sultan Eid Al-Otaibi , Guillermo Leal , Mohammed Bismillah Ansari , Naif Mohammed Al Naddah Al-Otaibi
Abstract: A method of manufacturing a cetane-boosting fuel additive includes reacting formaldehyde and 2-ethylhexanol at a mole ratio of 10:1 to 1:1, or 5:1 to 1.5:1, or 4:1 to 2:1, or 3.5:1 to 2.5:1 in the presence of a heterogeneous acid catalyst at a temperature of 300 to 375° K to obtain a cetane-boosting product mixture comprising H3C(CH2)3CH(CH2CH3)CH2(OCH2)nOH, H3C(CH2)3CH(CH2CH3)CH2(OCH2)nOCH2CH(CH2CH3)(CH2)3CH3, or a combination thereof, wherein n has an average value of 2.8 to 3.2, preferably an average value of 3.
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公开(公告)号:US12264123B2
公开(公告)日:2025-04-01
申请号:US17436753
申请日:2020-03-05
Applicant: SABIC Global Technologies B.V. , Saudi Arabian Oil Company
Inventor: Guillermo Leal , Naif Mohammed Al-Naddah Al-Otaibi , Kareemuddin Mahaboob Shaik , Mohammed Bismillah Ansari , Vijay Dinkar Bodas
IPC: C07C29/04 , B01D3/00 , C07C4/06 , C07C5/03 , C07C5/05 , C07C7/00 , C07C7/04 , C10L1/02 , C10L1/182
Abstract: A method of producing a fuel additive includes passing a feed stream comprising C4 hydrocarbons through a first hydrogenation unit producing a first process stream; passing the first process stream through a distillation unit; withdrawing a 2-butene stream from the distillation unit: passing the 2-butene stream through a second hydrogenation unit producing a 1-butene stream; passing at least a portion of the 1-butene stream through a separation unit; and passing the 1-butene stream through a hydration unit producing the fuel additive.
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公开(公告)号:US12017165B2
公开(公告)日:2024-06-25
申请号:US17608224
申请日:2020-05-05
Applicant: SABIC GLOBAL TECHNOLOGIES B.V.
Inventor: Vijay Dinkar Bodas , Mohammed Bismillah Ansari
IPC: B01D3/22
CPC classification number: B01D3/22
Abstract: This disclosure describes one or more trays for use in distillation columns. The trays include a plate having a plurality of through holes that extend between a first surface of the plate and a second surface of the plate. The plurality of through holes include a first set of through holes each having substantially a first diameter and a second set of through holes each having substantially a second diameter that is different from the first diameter. The trays also include a weir coupled to the plate and extending from the first surface. The weir is positioned between the first set of through holes and the second set of through holes.
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公开(公告)号:US11865533B2
公开(公告)日:2024-01-09
申请号:US17435451
申请日:2020-03-10
Applicant: SABIC GLOBAL TECHNOLOGIES B.V.
CPC classification number: B01J8/0278 , B01J8/001 , B01J19/002 , B01J19/2445 , C07C5/327 , G05B19/05 , G05B2219/15052
Abstract: Houdry lumps can be reduced by controlling the reactors in a fixed bed dehydrogenation process for producing olefins according to defined rules. A programmable logic controller can apply the rules to the operation of the dehydrogenation unit and control the operation of individual reactors according to the rules. By doing so, the performance of dehydrogenation units can be improved without adding any heat generating inerts, such as CuO-α alumina For example, the dehydrogenation units can be operated according to combinatorics in the programmable logic controller such that the farthest two reactors in the dehydrogenation unit never operate in parallel in the dehydrogenation or air regeneration steps.
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