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1. 发明申请

WO2010071989A1 LOW-PRESSURE FISCHER-TROPSCH PROCESS 审中-公开
标题翻译：低压FISCHER-TROPSCH工艺
公开(公告)号：WO2010071989A1
公开(公告)日：2010-07-01
申请号：PCT/CA2009/001862
申请日：2009-12-21
申请人： CANADA CHEMICAL CORPORATION , AYASSE, Conrad
发明人： AYASSE, Conrad
IPC分类号： C10G2/00 , C07C1/04 , C10L1/08
CPC分类号： B01J23/8913 , B01J23/8896 , B01J35/0026 , B01J35/023 , B01J35/1019 , B01J35/1042 , B01J37/0201 , C01B3/38 , C01B3/382 , C01B3/384 , C01B2203/0233 , C01B2203/0244 , C01B2203/025 , C01B2203/04 , C01B2203/0405 , C01B2203/0495 , C01B2203/062 , C01B2203/0877 , C01B2203/0883 , C01B2203/0888 , C01B2203/0894 , C01B2203/1241 , C01B2203/1258 , C01B2203/1294 , C10G2/332 , C10G2300/4025 , C10G2400/04 , C10L1/08 , Y02P20/52
摘要： A Fischer-Tϊopsch process for producing diesel fuel or diesel blending stock with a high cetane number, in a concentration of 65-90wt% at pressures below 200 psia, using a cobalt catalyst with a rhenium and/or ruthenium promoter. The catalyst is a cobalt catalyst with crystallites having an average diameter greater than 16 nanometers, and the resulting hydrocarbon product after a rough flash, contains less than 10wt% waxes (>C 23 ).
摘要翻译：用于使用具有铼和/或钌助催化剂的钴催化剂来生产具有高十六烷值的柴油燃料或柴油混合原料的费歇尔 - 托普法，其浓度为65-90重量％，压力低于200磅/平方英寸。催化剂是具有平均直径大于16纳米的微晶的钴催化剂，并且粗略闪蒸后的所得烃产物含有少于10重量％的蜡（> C23）。

2. 发明申请

WO1996006816A1 CATALYTIC PROCESS FOR THE PRODUCTION OF HYDROCARBONS 审中-公开
标题翻译：用于生产烃类的催化方法
公开(公告)号：WO1996006816A1
公开(公告)日：1996-03-07
申请号：PCT/CA1994000477
申请日：1994-08-29
申请人： CANADA CHEMICAL CORPORATION , AYASSE, Conrad
发明人： CANADA CHEMICAL CORPORATION
IPC分类号： C07C01/04
CPC分类号： C10G2/33 , C07C1/0435 , C07C1/044 , C07C2523/06 , C07C2523/72 , C07C2523/745 , C07C2523/75 , C07C2529/035 , C07C2529/40 , Y02P20/52
摘要： Single-stage catalytic conversion of a gas mixture, having a molar ratio of hydrogen to carbon monoxide greater than 1,9, to hydrocarbons boiling in the gasoline or diesel range, is achieved using three catalysts in admixture. The first is a Fischer-Tropsch catalyst with catalytic activity for the conversion of H2 and CO into hydrocarbons. The second is a methanol conversion catalyst with catalytic activity for the conversion of methanol into hydrocarbons, such as a crystalline alluminosilicate zeolite or crystalline silicate. Finally, the third is a methanol synthesis catalyst with catalytic activity for both the water-gas shift reaction and methanol synthesis. This combination of catalysts provides high carbon conversion of CO to hydrocarbons, and a high yield of liquid products.
摘要翻译：使用三种催化剂在混合物中，将氢气与一氧化碳的摩尔比大于1.9的气体混合物单独催化转化成汽油或柴油范围内沸腾的烃。第一种是具有催化活性的费 - 托催化剂，用于将H 2和CO转化成烃。第二种是具有甲醇转化为烃的催化活性的甲醇转化催化剂，例如结晶的硅铝酸盐沸石或结晶硅酸盐。最后，第三种是具有催化活性的甲醇合成催化剂，用于水煤气变换反应和甲醇合成。这种催化剂的组合提供CO对烃的高碳转化率和高产率的液体产物。

3. 发明申请

WO2008055353A1 LOW PRESSURE FIXED BED FISCHER-TROPSCH PROCESS AND APPARATUS 审中-公开
标题翻译：低压固定床FISCHER-TROPSCH PROCESS AND APPARATUS
公开(公告)号：WO2008055353A1
公开(公告)日：2008-05-15
申请号：PCT/CA2007/002014
申请日：2007-11-08
申请人： Canada Chemical Corporation , AYASSE, Conrad
发明人： AYASSE, Conrad
IPC分类号： C10G2/00 , B01J21/06 , B01J8/06
CPC分类号： B01J35/023 , B01J8/067 , B01J21/04 , B01J21/08 , B01J23/75 , B01J23/8896 , B01J23/8913 , B01J35/08 , B01J2208/00274 , B01J2208/00283 , B01J2208/00539 , B01J2208/00548 , B01J2219/00006 , C10G2/332 , C10G2/333
摘要： Diesel fuel or diesel blending stock with high cetane number is produced as a Fisher-Tropsch product in a concentration of 55-90+ weight percent without hydrocracking using a fixed bed Fisher-Tropsch reactor at pressures below 1.37 MPa using a cobalt catalyst comprising catalyst support particles having an average particle size between 0.8 mm and 5 mm and a cobalt component having a loading of between 5 and 35 wt% of the total catalyst composition. After a rough flash, a more pure diesel can be produced.
摘要翻译：使用具有高十六烷值的柴油燃料或柴油混合原料以55-90重量％的浓度产生，不使用固定床的费 - 托反应器，在低于1.37MPa的压力下使用含有催化剂载体的钴催化剂进行加氢裂化平均粒度为0.8mm至5mm的颗粒和负载量为总催化剂组合物的5-35wt％之间的钴组分。粗糙的闪光后，可以生产出更纯净的柴油。

4. 发明申请

WO2004082809A1 PROCESS FOR REMOVAL OF ACID GASES 审中-公开
标题翻译：去除酸性气体的方法
公开(公告)号：WO2004082809A1
公开(公告)日：2004-09-30
申请号：PCT/GB2004/000791
申请日：2004-02-27
申请人： BP EXPLORATION OPERATING COMPANY LIMITED , CANADA CHEMICAL CORPORATION , AYASSE, Conrad , DYMOV, Boris, P. , WALKER, Graeme, Alan, Orgill
发明人： AYASSE, Conrad , DYMOV, Boris, P. , WALKER, Graeme, Alan, Orgill
IPC分类号： B01D53/14
CPC分类号： B01D53/1493
摘要： A process for the removal of an acid gas from a gaseous feed stream comprising contacting the gaseous feed stream with an absorbing fluid to produce (a) a refined gaseous stream having a reduced acid gas content and (b) an acid gas rich absorbing fluid, wherein the absorbing fluid comprises an aqueous solution of a tertiary alkylamine having a concentration of tertiary alkylamine of above 60% by weight, and the tertiary alkylamine is selected from the group consisting of: diamines of formula: (I) (R 1 ) 2 N(CR 2 R 3 ) n N(R 1 ) 2 triamines of formula: (II) (R 1 ) 2 N(CR 2 R 3 ) n N(R)(CR 2 R 3 ) n N(R 1 ) 2 and tetramines of formula: (III) (R 1 ) 2 N(CR 2 R 3 ) n N(R)(CR 2 R 3 ) n N(R)(CR 2 R 3 ) n N(R 1 ) 2 where each R is independently a substituted or unsubstituted C 1 - C 4 alkyl; each R 1 is independently a substituted or unsubstituted C 1 - C 4 alkyl or, alternatively, the two R 1 groups together with the nitrogen atom form a heterocyclic ring; R 2 and R 3 are independently a hydrogen or a C 1 - C 4 alkyl group, and each of the CR 2 R 3 groups are the same or different and n is an integer from 1 to 4.
摘要翻译：一种用于从气态进料流中除去酸性气体的方法，包括使气态进料流与吸收流体接触以产生（a）具有降低的酸性气体含量的精炼气流，和（b）富含酸性气体的吸收流体，其中所述吸收流体包含叔烷基胺浓度高于60重量％的叔烷基胺的水溶液，所述叔烷基胺选自：式（I）（R 1）的二胺：（II）（R 1）2 N（CR 2 R 3）n N（R）（CR 1）2 NR（CR 2 R 3）n N（R 1） 2 R 3）n N（R 1）2和式（III）（R 1）2 N（CR 2 R 3）n N（R）（CR 2 R nN（R）（CR 2 R 3）n N（R 1）2，其中每个R独立地是取代或未取代的C 1 -C 4烷基; 每个R 1独立地是取代或未取代的C 1 -C 4烷基，或者，两个R 1基团与氮原子一起形成杂环; R 2和R 3独立地为氢或C 1 -C 4烷基，CR 2 R 3基团各自相同或不同，n为1至4的整数。

5. 发明申请

WO2010071967A1 LOW-PRESSURE FISCHER-TROPSCH PROCESS 审中-公开
标题翻译：低压FISCHER-TROPSCH工艺
公开(公告)号：WO2010071967A1
公开(公告)日：2010-07-01
申请号：PCT/CA2008/002306
申请日：2008-12-22
申请人： CANADA CHEMICAL CORPORATION , AYASSE, Conrad
发明人： AYASSE, Conrad
IPC分类号： C10G2/00 , B01J23/75 , B01J23/84
CPC分类号： B01J23/8913 , B01J21/04 , B01J21/08 , B01J23/75 , B01J23/8896 , B01J35/006 , B01J35/0066 , B01J35/023 , B01J37/0201 , B01J37/18 , C01B3/38 , C01B2203/0233 , C01B2203/0244 , C01B2203/025 , C01B2203/04 , C01B2203/0405 , C01B2203/0495 , C01B2203/062 , C01B2203/0888 , C01B2203/0894 , C01B2203/1258 , C01B2203/1294 , C10G2400/04 , Y02E50/346 , Y02P20/52 , Y02T50/678
摘要： A Fischer-Tropsch process for producing diesel fuel or diesel blending stock with a high cetane number, in a concentration of 65-90wt% at pressures below 200 psia, using a cobalt catalyst with a rehenium and/or ruthenium promoter, The catalyst is a cobalt catalyst with crystallites having an average diameter greater than 16 nanometers, and the resulting hydrocarbon product after a rough flash, contains less than 10wt% waxes (>C 23 ).
摘要翻译：使用具有铼和/或钌助催化剂的钴催化剂生产具有高十六烷值的柴油燃料或柴油混合原料的费 - 托方法，浓度为65-90wt％，压力低于200psia。催化剂为具有平均直径大于16纳米的微晶的钴催化剂，粗糙闪蒸后的所得烃产物含有少于10重量％的蜡（> C23）。

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