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公开(公告)号:US20220371978A1
公开(公告)日:2022-11-24
申请号:US17783841
申请日:2020-12-10
Applicant: SABIC Global Technologies B.V.
Inventor: Guillermo LEAL , Mohammed B. ANSARI , Vijay Dinkar BODAS , Umesh HASYAGAR , Vinod NAIR
Abstract: Systems and methods for producing MTBE are disclosed. A C4 feed stream containing isobutylene and other C4 hydrocarbons is fed into a reactor unit for producing MTBE. The effluent of the reactor unit comprising MTBE is further processed to produce a MTBE product stream that comprises at least 90 wt. % MTBE. At least a portion of the MTBE product stream is then recycled back to the reactor unit.
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公开(公告)号:US20200032149A1
公开(公告)日:2020-01-30
申请号:US16497908
申请日:2018-03-29
Applicant: SABIC Global Technologies B.V.
Inventor: Vijay Dinkar BODAS , Sultan AL-OTAIBE , Guillermo LEAL , Mohammed Bismillah ANSARI
IPC: C10G61/06
Abstract: A process for producing natural gasoline. The process includes increasing the n-pentane concentration of debutanized natural gasoline. The process may include a first concentration process that includes distillation and a second concentration process that includes simulated moving bed adsorption.
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公开(公告)号:US20220162144A1
公开(公告)日:2022-05-26
申请号:US17434191
申请日:2020-02-27
Applicant: SABIC Global Technologies B.V.
Inventor: Vijay Dinkar BODAS , Guillermo LEAL , Mohammed Bismillah Ansari
IPC: C07C29/151 , C07C29/80 , C07C41/34
Abstract: A method of producing methanol is disclosed. The method involves adding alkali to crude methanol and distilling the crude methanol in one or more distillation columns. The method also includes flowing a vapor side draw from one of the distillation columns, where the vapor side draw comprises fusel oil substantially free from alkali The fusel oil is recycled to a methanol synthesis reactor and/or a MTBE synthesis reactor.
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公开(公告)号:US20210147317A1
公开(公告)日:2021-05-20
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:US20210139803A1
公开(公告)日:2021-05-13
申请号:US16487222
申请日:2018-02-24
Applicant: SABIC GLOBAL TECHNOLOGIES B.V. , SAUDI ARABIAN OIL COMPANY
Inventor: Guillermo LEAL , Kareemuddin M. SHAIK , Mohammed Bismillah ANSARI , Hassan BABIKER , Somak PAUL , Kamalakar GUNDA
Abstract: An octane-enhancing additive includes a mixed butanol composition, sec-butyl ether, methanol, methyl tert-butyl ether, and a C4-dimer, the mixed butanol composition comprising sec-butanol and tert-butanol, and the C4-dimer comprising di-isobutylene, 2,2,4 trimethylpentane, 2,3,3 trimethylpentane, or a combination comprising at least one of the foregoing.
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公开(公告)号:US20210078922A1
公开(公告)日:2021-03-18
申请号:US16954381
申请日:2018-12-12
Applicant: SABIC Global Technologies B.V.
Inventor: Khaja Aliuddin SHARIF , Mohammed Bismillah ANSARI , Guillermo LEAL
Abstract: Systems and processes for producing isomerized alkenes are disclosed. The systems mainly include an isomerization unit, a dehydrogenation unit, and a MTBE synthesis unit. A hydrocarbon stream is fed into the isomerization unit to form iso-alkanes in a sulfur free hydrocarbon stream. The sulfur free hydrocarbon stream is heated and then combined with a sulfur-containing hydrocarbon stream comprising sulfur containing compounds to form a reactant feed stream to the dehydrogenation unit. The iso-alkanes is dehydrogenated to form iso-alkenes. The formed iso-alkenes comprising isobutylene can be used as a feed stock for the MTBE synthesis unit.
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公开(公告)号:US20210002196A1
公开(公告)日:2021-01-07
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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8.
公开(公告)号:US20200071286A1
公开(公告)日:2020-03-05
申请号:US16467178
申请日:2017-12-13
Applicant: SABIC Global Technologies B.V.
Inventor: Guillermo LEAL , Mohammed Bismillah ANSARI , Vijay BODAS , Sultan AL OTAIBE
IPC: C07D307/60 , C07D307/33 , C07D307/08 , C07C29/17
Abstract: Certain embodiments are directed to an integrated process for the production of Maleic Anhydride (MAN), 1,4 Butanediol (BDO), Gamma-ButyroLactone (GBL), and PolyButylene Terephthalate (PBT) utilizing NC4 rich stream from a recycle stream after or before processing by a Total Hydrogenation Unit (THU).
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公开(公告)号:US20200031739A1
公开(公告)日:2020-01-30
申请号:US16604215
申请日:2018-05-01
Applicant: SABIC GLOBAL Technologies B.V.
Inventor: Mohammed Bismillah ANSARI , Vijay Dinkar BODAS , Guillermo LEAL , Sultan AL-OTAIBE
Abstract: Systems and methods of dehydrogenating a hydrocarbon in a fixed bed dehydrogenation unit. A method for dehydrogenating a hydrocarbon is applied to a fixed bed reactor. The hydrocarbon flows to a fixed bed reactor to be dehydrogenated in presence of a catalyst in the fixed bed reactor. The catalyst in the fixed bed reactor is then regenerated. The period for dehydrogenation, the period for catalyst regeneration and the period for total slack time are controlled such that total slack time is less than both half of the period for dehydrogenation and half of the period for regeneration. One of the advantages of the process comes from optimization of the slack time, thereby increasing the catalyst utilization rate and number of reactors concurrently online.
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10.
公开(公告)号:US20200024227A1
公开(公告)日:2020-01-23
申请号:US16496497
申请日:2018-03-07
Applicant: SABIC Global Technologies B.V.
Inventor: Mohammed Bismillah ANSARI , Vijay Dinkar BODAS , Guillermo LEAL
IPC: C07C273/04 , C07C273/14 , C07C269/00 , C07D317/36
Abstract: Systems and methods for integrated glycerol carbonate and/or urea production. This disclosure pertains to development of a process for production of glycerol carbonate and/or urea from ammonia, carbon dioxide and glycerol. The process integrates glycerol carbonate production into a urea production process. The urea produced in the production facility may be used to produce glycerol carbonate by reacting urea with glycerol. The ammonia generated by glycerol carbonate production may be recycled back to urea production. Unreacted urea from the glycerol carbonate production may be separated and recycled to the urea product stream. The systems and methods can reduce the cost for urea production and increase product value of the excessive glycerol produced from other chemical plants.
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