公开(公告)号：US10717936B2

公开(公告)日：2020-07-21

申请号：US16318464

申请日：2017-07-17

Applicant: SABIC Global Technologies B.V.

Inventor： Alexander Stanislaus ,  Ravichander Narayanaswamy ,  Krishna Kumar Ramamurthy ,  Santosh Ganji ,  Abrar A. Hakeem ,  Ashim Kumar Ghosh ,  Girish Koripelly ,  Mohammad Javeed

IPC: C10G1/10 ,  B01J29/08 ,  B01J29/18 ,  B01J29/40 ,  B01J29/85 ,  B29B17/04 ,  C10B53/07 ,  C10G11/18 ,  C10G45/02 ,  C10G69/06 ,  C10K1/00 ,  C10G45/58 ,  C10G1/08 ,  C10G1/00 ,  C10K1/32 ,  C10B57/06 ,  C10G47/00 ,  B29K27/00

Abstract: A process for processing mixed plastics comprising simultaneous pyrolysis and dechlorination of the mixed plastics, the process comprising contacting the mixed plastics with a zeolitic catalyst in a pyrolysis unit to produce a hydrocarbon product comprising a gas phase and a liquid phase; and separating the hydrocarbon product into a hydrocarbon gas stream and a hydrocarbon liquid stream, wherein the hydrocarbon gas stream comprises at least a portion of the gas phase of the hydrocarbon product, wherein the hydrocarbon liquid stream comprises at least a portion of the liquid phase of the hydrocarbon product, wherein the hydrocarbon liquid stream comprises one or more chloride compounds in an amount of less than about 100 ppmw chloride, based on the total weight of the hydrocarbon liquid stream, and wherein the hydrocarbon liquid stream is characterized by a viscosity of less than about 400 cP at a temperature of 300° C.

公开(公告)号：US20180353944A1

公开(公告)日：2018-12-13

申请号：US15780296

申请日：2016-12-05

Applicant: SABIC GLOBAL TECHNOLOGIES B.V.

Inventor： Alla Khanmamedova ,  Ashim Kumar Ghosh ,  Scott Stevenson ,  David Sullivan ,  Pooja Bajaj

IPC: B01J29/44 ,  C10G45/64 ,  B01J37/02 ,  B01J37/08 ,  B01J35/02 ,  B01J37/30

CPC classification number: B01J29/44 ,  B01J23/42 ,  B01J29/068 ,  B01J35/002 ,  B01J35/0073 ,  B01J35/023 ,  B01J37/0201 ,  B01J37/08 ,  B01J37/18 ,  B01J37/30 ,  C10G45/64 ,  C10G47/18

Abstract: The invention relates to a process for preparing a hydrocracking catalyst, comprising (i) contacting a shaped body comprising a zeolite and a binder with an aqueous solution of a hydrogenation metal compound which is a complex or a salt of a hydrogenation metal to deposit the hydrogenation metal onto the shaped body, wherein the aqueous solution comprises an ammonium salt and (ii) calcining the shaped body obtained by step (i).

公开(公告)号：US09550178B2

公开(公告)日：2017-01-24

申请号：US14907598

申请日：2015-07-28

Applicant: SABIC Global Technologies B.V.

Inventor： Ashim Kumar Ghosh ,  Alla Khanmamedova ,  Mike Mier ,  Jonathan Banke

IPC: C07C1/26 ,  B01J29/85 ,  B01J7/00 ,  B01J35/10 ,  C01B39/54

CPC classification number: B01J29/85 ,  B01J7/00 ,  B01J35/002 ,  B01J35/023 ,  B01J35/1061 ,  B01J2229/37 ,  C01B39/54 ,  C07C1/26 ,  C07C2529/85 ,  Y02P20/52 ,  Y02P20/584 ,  Y02P30/42 ,  C07C11/04 ,  C07C11/06 ,  C07C11/08

Abstract: Disclosed is a method for converting an alkyl halide to an olefin. The method includes contacting a silicoaluminophosphate (SAPO) catalyst with a feed that includes an alkyl halide under reaction conditions sufficient to produce an olefin hydrocarbon product that includes C2 to C4 olefins. The SAPO catalyst has bimodal acidity designated as weak acid sites and strong acid sites. The weak acid concentration is less than 0.55 mmol/g-cat and the total acid concentration is less than 1.5 mmol/g-cat.

Abstract translation: 公开了将烷基卤转化为烯烃的方法。 该方法包括在足以产生包括C 2至C 4烯烃的烯烃产物的反应条件下使硅铝磷酸盐（SAPO）催化剂与包含烷基卤的进料接触。 SAPO催化剂具有指定为弱酸性位点和强酸性位点的双峰酸性。 弱酸浓度小于0.55 mmol / g-cat，总酸浓度小于1.5 mmol / g-cat。

公开(公告)号：US20160347681A1

公开(公告)日：2016-12-01

申请号：US15153873

申请日：2016-05-13

Applicant: SABIC Global Technologies B.V.

Inventor： Ashim Kumar Ghosh ,  Edouard Mamedov ,  Neeta Kulkarni ,  Armando Araujo ,  Mike Mier

IPC: C07C1/30 ,  B01J29/46 ,  B01J29/40

CPC classification number: B01J29/46 ,  B01J29/40 ,  B01J29/405 ,  B01J35/1019 ,  B01J37/0201 ,  B01J37/0203 ,  B01J37/30 ,  C07C1/26 ,  C07C2529/40 ,  C07C2529/46 ,  Y02P20/52 ,  C07C11/04 ,  C07C11/06 ,  C07C11/08

Abstract: Disclosed is a method for converting an alkyl halide to an olefin. The method can include contacting a zeolite catalyst having a chemical formula of My/nH(x-y)AlxSi(96-x)O192, where M is a metal cation having a valence of n under reaction conditions sufficient to produce an olefin hydrocarbon product comprising C2 to C4 olefins. M can include cations of metals from Groups IA, IIA, IIIA. IVB, VB, VIB VIIB, IB, IIB, IIIA or IVA, or any combination of metal cations thereof and y is 0.4≦y≦5.0.

Abstract translation: 公开了将烷基卤转化为烯烃的方法。 该方法可以包括使化学式为My / nH（xy）Al x Si（96-x）O192的沸石催化剂接触，其中M是在足以产生包含C2的烯烃产物的反应条件下具有n价的金属阳离子 到C4烯烃。 M可以包括IA，IIA，IIIA族金属的阳离子。 IVB，VB，VIB VIIB，IB，IIB，IIIA或IVA，或其金属阳离子的任何组合，y为0.4≤y≤5.0。