公开(公告)号：US20060270885A1

公开(公告)日：2006-11-30

申请号：US11149504

申请日：2005-05-31

申请人： Christopher Boyer ,  Mitchell Loescher ,  Jinsuo Xu ,  Frits Dautzenberg

发明人： Christopher Boyer ,  Mitchell Loescher ,  Jinsuo Xu ,  Frits Dautzenberg

IPC分类号： C07C5/13

CPC分类号： C10G45/62 ,  C07C5/2791 ,  C07C2521/06 ,  C07C2523/10 ,  C07C2523/14 ,  C07C2523/28 ,  C07C2523/30 ,  C07C2523/42 ,  C07C2523/44 ,  C07C2523/46 ,  C07C2523/62 ,  C07C2523/745 ,  C07C2523/75 ,  C07C2523/755 ,  C07C2527/053 ,  C07C2527/167 ,  C10G45/60 ,  Y02P20/127 ,  C07C9/16

摘要： A process for the isomerization of heptane preferably contained within a naphtha stream is disclosed wherein the naphtha is stripped of the butanes and the pentanes and hexanes are removed for isomerization. The heptanes and heavier are fed to a distillation column reactor containing an isomerization catalyst where the normal heptane is isomerized to mono and di branched heptane and removed as overheads. The cyclic heptanes and heavier are removed as bottoms and for feed to a catalytic reforming process.

摘要翻译： 公开了一种用于庚烷异构化的方法，其优选包含在石脑油流中，其中将石脑油汽提出丁烷，并除去戊烷和己烷进行异构化。 将庚烷和较重的庚烷加入到含有异构化催化剂的蒸馏塔反应器中，其中正庚烷被异构化为单和二支化庚烷，并作为塔顶馏出物除去。 循环庚烷和较重的作为塔底产物和进料进行催化重整过程。

公开(公告)号：US20060264318A1

公开(公告)日：2006-11-23

申请号：US11446320

申请日：2006-06-02

申请人： Zhiping Shan ,  Peter Waller ,  Bowden Maingay ,  Philip Angevine ,  Jacobus Jansen ,  Chuen Yeh ,  Thomas Maschmeyer ,  Frits Dautzenberg ,  Leonardo Marchese ,  Heloise Pastore

发明人： Zhiping Shan ,  Peter Waller ,  Bowden Maingay ,  Philip Angevine ,  Jacobus Jansen ,  Chuen Yeh ,  Thomas Maschmeyer ,  Frits Dautzenberg ,  Leonardo Marchese ,  Heloise Pastore

IPC分类号： B01J29/04

CPC分类号： C10G11/04 ,  B01J21/06 ,  B01J21/12 ,  B01J23/26 ,  B01J23/38 ,  B01J23/44 ,  B01J23/50 ,  B01J23/52 ,  B01J29/005 ,  B01J29/0308 ,  B01J29/04 ,  B01J29/041 ,  B01J29/084 ,  B01J29/166 ,  B01J29/18 ,  B01J29/40 ,  B01J29/60 ,  B01J29/65 ,  B01J29/70 ,  B01J29/7007 ,  B01J29/80 ,  B01J29/85 ,  B01J29/87 ,  B01J29/88 ,  B01J29/89 ,  B01J35/002 ,  B01J35/1023 ,  B01J35/1028 ,  B01J35/1038 ,  B01J35/1042 ,  B01J35/1047 ,  B01J35/1061 ,  B01J35/108 ,  B01J37/0018 ,  B01J37/033 ,  B01J37/10 ,  B01J2229/183 ,  B01J2229/186 ,  B01J2229/32 ,  B01J2229/36 ,  B01J2229/42 ,  B01J2229/62 ,  C01B13/366 ,  C01B33/126 ,  C01B37/005 ,  C01B37/02 ,  C01P2006/12 ,  C01P2006/14 ,  C01P2006/16 ,  C07C2/66 ,  C07C45/46 ,  C07D215/227 ,  C07D301/06 ,  C07D301/10 ,  C10G2/332 ,  C10G11/05 ,  C10G27/04 ,  C10G29/205 ,  C10G45/00 ,  C10G45/04 ,  C10G45/12 ,  C10G45/60 ,  C10G45/62 ,  C10G45/64 ,  C10G45/68 ,  C10G47/00 ,  C10G47/14 ,  C10G47/16 ,  C10G49/02 ,  C10G49/08 ,  C10G50/00 ,  C10G2300/1096 ,  C10G2300/301 ,  C10G2300/4018 ,  C10G2400/04 ,  C10G2400/10 ,  C10G2400/30 ,  C07C15/073 ,  C07C49/84

摘要： A catalytic material includes microporous zeolites supported on a mesoporous inorganic oxide support. The microporous zeolite can include zeolite Beta, zeolite Y (including “ultra stable Y”—USY), mordenite, Zeolite L, ZSM-5, ZSM-11, ZSM-12, ZSM-20, Theta-1, ZSM-23, ZSM-34, ZSM-35, ZSM-48, SSZ-32, PSH-3, MCM-22, MCM-49, MCM-56, ITQ-1, ITQ-2, ITQ-4, ITQ-21, SAPO-5, SAPO-11, SAPO-37, Breck-6, ALPO4-5, etc. The mesoporous inorganic oxide can be e.g., silica or silicate. The catalytic material can be further modified by introducing some metals e.g. aluminum, titanium, molybdenum, nickel, cobalt, iron, tungsten, palladium and platinum. It can be used as catalysts for acylation, alkylation, dimerization, oligomerization, polymerization, hydrogenation, dehydrogenation, aromatization, isomerization, hydrotreating, catalytic cracking and hydrocracking reactions.

公开(公告)号：US20050197499A1

公开(公告)日：2005-09-08

申请号：US10795726

申请日：2004-03-08

申请人： Zhiping Shan ,  Chuen Yeh ,  Philip Angevine ,  Frits Dautzenberg ,  Jacobus Jansen

发明人： Zhiping Shan ,  Chuen Yeh ,  Philip Angevine ,  Frits Dautzenberg ,  Jacobus Jansen

IPC分类号： C07D301/12 ,  C07D201/04

CPC分类号： C07D301/19 ,  Y02P20/125

摘要： An integrated process combines olefin epoxidation with production of cyclohexanone and cyclohexanol for nylon. Cyclohexanone and cyclohexanol normally produced by the oxidation of cyclohexane, in which cyclohexyl hydroperoxide is generated and is removed or decomposed down stream. However, this invention utilizes the intermediate of cyclohexyl hydroperoxide as an oxidant for the olefin epoxidation and meanwhile generates a valuable product.

摘要翻译： 一体化方法将烯烃环氧化与生产环己酮和环己醇用于尼龙。 通常通过环己烷氧化生成环己酮和环己醇，其中产生环己基氢过氧化物并在流下被除去或分解。 然而，本发明利用环己基氢过氧化物的中间体作为烯烃环氧化的氧化剂，同时产生有价值的产物。