公开(公告)号：US20240182364A1

公开(公告)日：2024-06-06

申请号：US18553856

申请日：2022-04-13

Applicant: SABIC Global Technologies B.V.

Inventor： Khaja Aliuddin SHARIEF ,  Mohammed Bismillah ANSARI ,  Venkata Malleswara Rao TADIBOYINA

IPC: C04B28/14 ,  C04B7/32 ,  C04B7/44 ,  C04B7/52 ,  C04B22/14 ,  C04B111/10

CPC classification number: C04B28/14 ,  C04B7/32 ,  C04B7/44 ,  C04B7/52 ,  C04B22/149 ,  C04B2111/1081

Abstract: Methods of producing cement using a spent hydrocarbon dehydrogenation catalyst are disclosed. A spent hydrocarbon dehydrogenation catalyst comprising alumina is processed to produce a processed raw material. The processed raw material is then used as a component for producing the cement. Compositions of cement including the processed raw material are disclosed.

公开(公告)号：US20230278940A1

公开(公告)日：2023-09-07

申请号：US18005589

申请日：2021-07-16

Applicant: SABIC GLOBAL TECHNOLOGIES B.V.

Inventor： Vijay Dinkar BODAS ,  Mohammed Bismillah ANSARI

IPC: C07C2/76 ,  C07C4/04 ,  C07C41/06 ,  C07C5/27 ,  C07C5/333 ,  C07C5/42

CPC classification number: C07C2/76 ,  C07C4/04 ,  C07C41/06 ,  C07C5/2724 ,  C07C5/3337 ,  C07C5/42 ,  C07C2521/04 ,  C07C2523/24 ,  C07C2523/42 ,  C07C2527/053 ,  C07C2527/126

Abstract: Systems and methods for processing a C3 and C4 hydrocarbon mixture have been disclosed. The C3 and C4 hydrocarbon mixture is separated to remove propane from C4 hydrocarbons. The resulting C4 hydrocarbons are then processed in an isomerization unit to produce additional isobutane. The isobutane of the isomerization unit effluent is dehydrogenated in a dehydrogenation unit to produce isobutene. The resulting isobutene is reacted with an alkanol to produce an alkyl tert-butyl ether.

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

IPC: C07C5/333 ,  C07C41/06 ,  B01J8/24

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.

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

IPC: C07C41/06 ,  C07C5/05 ,  C07C6/04 ,  C07C7/04 ,  C07C7/163

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.

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).

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

IPC: C07C5/333 ,  B01J23/26 ,  B01J23/62 ,  B01J38/02 ,  B01J8/02 ,  B01J8/00

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.

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.