公开(公告)号：WO2016185335A1

公开(公告)日：2016-11-24

申请号：PCT/IB2016/052753

申请日：2016-05-12

Applicant: SABIC GLOBAL TECHNOLOGIES B.V.

Inventor： AL-QAHTANI, Thabet Mohammed ,  KARIM, Khalid ,  BASHIR, Mubarik Ali ,  AL-HAMMAD, Ali ,  AHMED, Labeeb Chaudhary ,  AL-KHUDEER, Saud ,  AL-JALOUD, Abdullah Turki

IPC: C10G2/00 ,  C10G35/095 ,  C07C15/04 ,  C07C15/06 ,  C07C15/08 ,  C07C4/14 ,  C10G47/00 ,  C10G63/04

CPC classification number: C10G2/30 ,  B01J19/245 ,  B01J2219/24 ,  C07C2/42 ,  C07C4/14 ,  C10G35/095 ,  C10G47/00 ,  C10G63/04 ,  C10G2300/1022 ,  C10G2400/30 ,  C07C15/04 ,  C07C15/06 ,  C07C15/08

Abstract: Disclosed herein is a system and method capable of producing benzene from a product stream.

Abstract translation: 本文公开了一种能够从产品流中生产苯的系统和方法。

公开(公告)号：WO2017032672A1

公开(公告)日：2017-03-02

申请号：PCT/EP2016/069554

申请日：2016-08-18

Applicant: SABIC GLOBAL TECHNOLOGIES B.V.

Inventor： KHANMAMEDOVA, Alla ,  SCOTT, Stevenson ,  FICKEL, Dustin

IPC: C07C15/04 ,  C07C5/41 ,  C10G47/18 ,  C07C5/13 ,  B01J29/44 ,  C10G35/095 ,  C10G35/085 ,  C07C4/06 ,  C07C4/14 ,  C10G45/70 ,  C10G45/62 ,  C10G45/64 ,  B01J23/56 ,  C07C4/08 ,  C07C4/18

CPC classification number: C10G47/18 ,  B01J23/56 ,  B01J29/44 ,  B01J35/023 ,  B01J2229/186 ,  B01J2229/20 ,  B01J2229/42 ,  C07C4/06 ,  C07C4/08 ,  C07C4/14 ,  C07C4/18 ,  C07C5/13 ,  C07C5/41 ,  C07C15/04 ,  C10G35/085 ,  C10G35/095 ,  C10G45/62 ,  C10G45/64 ,  C10G45/70 ,  C10G2300/1044 ,  C10G2400/30 ,  Y02P20/52

Abstract: The invention relates to a process for producing benzene comprising the steps of: (a) providing a hydrocracking feed stream comprising C 5 -C 12 hydrocarbons, (b) contacting the hydrocracking feed stream in the presence of hydrogen with a hydrocracking catalyst under process conditions including a temperature of 425-580°C, a pressure of 300-5000 kPa gauge and a Weight Hourly Space Velocity of 3-30 h -1 to produce a hydrocracking product stream comprising BTX and (c) separating the BTX from the hydrocracking product stream, wherein the hydrocracking catalyst comprises a shaped body comprising a zeolite and a binder and a hydrogenation metal deposited on the shaped body, wherein the amount of the hydrogenation metal is 0.010-0.30 wt-% with respect to the total catalyst and wherein the zeolite is ZSM-5 having a silica (SiO 2 ) to alumina (Al 2 O 3 ) molar ratio of 25-75.

Abstract translation: 本发明涉及一种生产苯的方法，包括以下步骤：（a）提供包含C5-C12烃的加氢裂化原料流，（b）在加氢裂化催化剂存在下，在加氢裂化催化剂存在下使加氢裂化原料流与 温度为425-580℃，压力为300-5000kPa表压，重量每小时空速为3-30h-1，以产生包含BTX的加氢裂化产物流，和（c）从加氢裂化产物流中分离出BTX， 其中所述加氢裂化催化剂包括成形体，其包含沸石和粘合剂以及沉积在所述成型体上的氢化金属，其中所述氢化金属的量相对于所述总催化剂为0.010-0.30重量％，并且其中所述沸石为ZSM -5具有二氧化硅（SiO 2）与氧化铝（Al 2 O 3）的摩尔比为25-75。

公开(公告)号：WO2016185334A1

公开(公告)日：2016-11-24

申请号：PCT/IB2016/052752

申请日：2016-05-12

Applicant: SABIC GLOBAL TECHNOLOGIES B.V.

Inventor： AL-QAHTANI, Thabet Mohammed ,  KARIM, Khalid ,  BASHIR, Mubarik Ali ,  AL-HAMMAD, Ali ,  AHMED, Labeeb Chaudhary ,  AL-KHUDEER, Saud ,  AL-JALOUD, Abdullah Turki

IPC: C10G2/00 ,  C10G35/095 ,  C10G63/04 ,  C10G47/00 ,  C07C15/04 ,  C07C15/06 ,  C07C15/08 ,  C07C4/14 ,  C07C11/08 ,  C07C11/16

CPC classification number: C07C5/48 ,  B01J8/04 ,  B01J8/08 ,  B01J8/24 ,  C07C2/00 ,  C07C4/16 ,  C07C7/005 ,  C07C7/04 ,  C10G2/30 ,  C10G35/095 ,  C10G47/00 ,  C10G63/04 ,  C10G2300/1022 ,  C10G2400/20 ,  C10G2400/30 ,  C07C11/167 ,  C07C11/08

Abstract: Disclosed herein is a system and method capable of producing butadiene from a product stream.

Abstract translation: 本文公开了一种能够从产物流中生产丁二烯的系统和方法。

公开(公告)号：WO2020086740A1

公开(公告)日：2020-04-30

申请号：PCT/US2019/057696

申请日：2019-10-23

Applicant: SAUDI ARABIAN OIL COMPANY ,  ARAMCO SERVICES COMPANY

Inventor： XU, Qi ,  ABUDAWOUD, Raed H. ,  ZHANG, Zhonglin

IPC: C10G35/00 ,  C07C4/12 ,  C07C4/14 ,  C07C6/12 ,  C07C7/00 ,  C07C15/04 ,  C07C15/06 ,  C07C15/08 ,  C07C5/27 ,  B01D53/047

Abstract: Embodiments include processes and systems for maximizing the production of benzene and para-xylene from heavy reformate. Embodiments include a C9 dealkylation reactor, a transalkylation reactor, and a C10+ dealkylation reactor. The process and system for producing benzene and para-xylene may be configured to additionally produce alkanes in the presence of hydrogen or olefins in the absence of hydrogen. Embodiments may include an aromatic extraction unit to separate non-aromatics from aromatics.

公开(公告)号：WO2011138357A1

公开(公告)日：2011-11-10

申请号：PCT/EP2011/057101

申请日：2011-05-04

Applicant: BASF SE ,  PROCHAZKA, Roman ,  BITTERLICH, Stefan ,  MACHHAMMER, Otto ,  DEUERLEIN, Stephan ,  KLINGLER, Dirk ,  PANTOUFLAS, Emmanouil ,  KINDLER, Alois ,  ZOELS, Bernd ,  WERTHER, Joachim ,  HARTGE, Ernst-Ulrich ,  WANG, Peng ,  SCHULT, Bernhard ,  RIMOSCHAT, Frank ,  ROHDE, Heiko

Inventor： PROCHAZKA, Roman ,  BITTERLICH, Stefan ,  MACHHAMMER, Otto ,  DEUERLEIN, Stephan ,  KLINGLER, Dirk ,  PANTOUFLAS, Emmanouil ,  KINDLER, Alois ,  ZOELS, Bernd ,  WERTHER, Joachim ,  HARTGE, Ernst-Ulrich ,  WANG, Peng ,  SCHULT, Bernhard ,  RIMOSCHAT, Frank ,  ROHDE, Heiko

IPC: C10G1/00 ,  C10G1/02 ,  C10G11/00 ,  C10G35/00 ,  C07C4/14 ,  C10B53/02

CPC classification number: C10G1/02 ,  C10B53/02 ,  C10G1/002 ,  C10G11/00 ,  C10G35/00 ,  C10G2300/1014 ,  C10G2400/30 ,  Y02E50/14 ,  Y02P30/20

Abstract: Die vorliegende Erfindung betrifft ein Verfahren zur Herstellung niedermolekularer aromatischer Wertstoffe aus einem aus Biomasse erzeugten ligninhaltigen Ausgangsmaterial.

Abstract translation: 本发明涉及一种用于从由生物质的木质素起始原料产生的信号制备低分子量的芳香族材料的方法。

公开(公告)号：WO2017205083A8

公开(公告)日：2017-11-30

申请号：PCT/US2017/032374

申请日：2017-05-12

Applicant: SABIC GLOBAL TECHNOLOGIES B.V. ,  BAFNA, Sheetal ,  DESHPANDE, Sanjeev ,  HUCKMAN, Michael ,  STEVENSON, Scott

Inventor： BAFNA, Sheetal ,  DESHPANDE, Sanjeev ,  HUCKMAN, Michael ,  STEVENSON, Scott

IPC: C10G9/36 ,  C10G45/32 ,  C10G45/02 ,  C10G11/00 ,  C10G67/14 ,  C07C15/04 ,  C07C15/06 ,  C07C15/08 ,  C10G45/58 ,  C10G67/04 ,  C10G45/44 ,  C07C4/14 ,  C10G69/00 ,  C10G11/18 ,  C10G69/06 ,  C10G69/14

Abstract: An integrated process for forming a combined feedstock stream comprising catalytically cracking a first hydrocarbon feedstock to form a full range cracked full naphtha stream and a first light olefins stream, steam cracking a second hydrocarbon feedstock to form a pyrolysis gasoline stream and a second light olefins stream mixing at least a portion of each of the full range cracked naphtha stream and the pyrolysis gasoline stream to form a combined stream, hydro-processing the combined stream to form a hydro-processed combined stream splitting the hydro-processed combined stream into a C 5 /C 6 stream, and a first aromatic rich stream, splitting the first aromatic rich stream into a second aromatic rich stream and a heavy oil stream.

公开(公告)号：WO2017205083A1

公开(公告)日：2017-11-30

申请号：PCT/US2017/032374

申请日：2017-05-12

Applicant: SABIC GLOBAL TECHNOLOGIES B.V. ,  BAFNA, Sheetal ,  DESHPANFDE, Sanjiiv ,  HUCKMAN, Michael ,  STEVENSON, Scott

Inventor： BAFNA, Sheetal ,  DESHPANFDE, Sanjiiv ,  HUCKMAN, Michael ,  STEVENSON, Scott

IPC: C10G9/36 ,  C10G45/32 ,  C10G45/02 ,  C10G11/00 ,  C10G67/14 ,  C07C15/04 ,  C07C15/06 ,  C07C15/08 ,  C10G45/58 ,  C10G67/04 ,  C10G45/44 ,  C07C4/14 ,  C10G69/00 ,  C10G11/18 ,  C10G69/06 ,  C10G69/14

Abstract: An integrated process for forming a combined feedstock stream comprising catalytically cracking a first hydrocarbon feedstock to form a full range cracked full naphtha stream and a first light olefins stream, steam cracking a second hydrocarbon feedstock to form a pyrolysis gasoline stream and a second light olefins stream mixing at least a portion of each of the full range cracked naphtha stream and the pyrolysis gasoline stream to form a combined stream, hydro-processing the combined stream to form a hydro-processed combined stream splitting the hydro-processed combined stream into a C 5 /C 6 stream, and a first aromatic rich stream, splitting the first aromatic rich stream into a second aromatic rich stream and a heavy oil stream.

Abstract translation: 一种形成组合原料流的综合方法，其包括催化裂化第一烃原料以形成全程裂化全石脑油流和第一轻质烯烃流，蒸汽裂化第二烃原料以形成热解 汽油料流和第二轻质烯烃料流，所述第二轻质烯烃料流将全范围裂化石脑油料流和裂解汽油料流中的每一个的至少一部分混合以形成组合料流，对组合料流进行加氢处理以形成加氢处理的组合料流， 处理后的组合物流转化为C 5 / C 6物流和第一富芳烃物流，将第一富芳烃物流分成第二富芳烃物流和重油 流。

公开(公告)号：WO98056738A1

公开(公告)日：1998-12-17

申请号：PCT/US1998/011115

申请日：1998-06-02

IPC: C07C5/22 ,  C07B61/00 ,  C07C2/66 ,  C07C4/14 ,  C07C11/02 ,  C07C15/02 ,  C07C1/00

CPC classification number: C07C11/02 ,  Y02P20/127

Abstract: An isomerization process for C4 to C15 olefins carried out by the reaction of C4 to C15 olefins, having a first skeletal distribution, with aromatic compounds under alkylation conditions to produce an alkylated aromatic product, dealkylation of the alkylated aromatic product under dealkylation conditions to produce a dealkylated product comprising said aromatic compounds and olefins corresponding to the olefins in the alkylation and having a second skeletal distribution different than said first skeletal distribution. Acidic catalysts such as molecular sieves are used in both alkylation and dealkylation. The reactions may be carried out in either straight pass fixed beds or in catalytic distillation reactors.

Abstract translation: 通过在烷基化条件下具有第一骨架分布的C4至C15烯烃与芳族化合物的反应产生烷基化芳族产物进行C4至C15烯烃的异构化方法，在脱烷基化条件下烷基化芳族产物的脱烷基化产生 脱烷基化产物包含所述芳族化合物和对应于烷基化中的烯烃的烯烃，并且具有不同于所述第一骨架分布的第二骨架分布。 酸性催化剂如分子筛用于烷基化和脱烷基化。 反应可以在直通固定床或催化蒸馏反应器中进行。