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1. 发明申请

WO2007068008A3 ALKYLATION PROCESS 审中-公开
标题翻译：烷基化方法
公开(公告)号：WO2007068008A3
公开(公告)日：2007-09-20
申请号：PCT/ZA2006000145
申请日：2006-12-08
申请人： SASOL TECH PTY LTD , DE KLERK ARNO , NEL REINIER JOHANNES JACOBUS , SAKUNEKA TEBOGO MOLAPISANE
发明人： DE KLERK ARNO , NEL REINIER JOHANNES JACOBUS , SAKUNEKA TEBOGO MOLAPISANE
IPC分类号： C07C2/70 , C07C15/02 , C07C15/067 , C07C15/073 , C07C15/085 , C10G50/00
CPC分类号： C07C2/70 , C07C2527/173 , C10G29/205
摘要： The invention provides a process for the alkylation of one or more streams containing one or more aromatics selected from the group including benzene, toluene, o-xylene, p-xylene, m-xylene, and ethyl benzene with olefins wherein the process is carried out at an aromatics to olefin ratio of from 1:6 to 1:30 on a molar basis, said process being carried out under oligomerisation conditions in the presence of a solid phosphorous catalyst at a temperature of from 140°C to 240°C and a pressure of from 1.5 MPa to 10 MPa whereby both oligomerisation and alkylation occur together.
摘要翻译：本发明提供了一种含有一种或多种选自包括苯，甲苯，邻二甲苯，对二甲苯，间二甲苯和乙基苯的芳族化合物的一种或多种芳烃的烷基化方法，其中进行该方法在摩尔浓度为1:6至1:30的芳烃与烯烃比为1:6的情况下，所述方法在低温条件下，在固体磷催化剂存在下，在140℃至240℃的温度和压力为1.5MPa至10MPa，由此低聚和烷基化一起发生。

2. 发明申请

WO2008124852A3 FISCHER-TROPSCH JET FUEL PROCESS 审中-公开
标题翻译： FISCHER-TROPSCH喷气式燃料过程
公开(公告)号：WO2008124852A3
公开(公告)日：2009-02-05
申请号：PCT/ZA2008000029
申请日：2008-04-10
申请人： SASOL TECH PTY LTD , DE KLERK ARNO
发明人： DE KLERK ARNO
IPC分类号： C10G2/00 , C10G29/20 , C10G35/04 , C10G47/00 , C10G49/00 , C10G50/00 , C10G69/10 , C10G69/12 , C10G69/14
CPC分类号： C10G50/00 , C10G2/32 , C10G29/205 , C10G35/04 , C10G47/00 , C10G49/00 , C10G69/10 , C10G69/123 , C10G69/126 , C10G69/14 , C10G2300/1022 , C10G2300/4025 , C10G2400/08
摘要： The invention provides a Fischer-Tropsch jet fuel refining process which has a jet fuel yield in excess of 60% by mass, said process including at least four of the following five conversion processes: a. hydrocracking one or more of a FT kerosene and heavier material fraction and a C9 and heavier FT syncrude fraction; b. oligomerising an FT syncrude fraction including hydrocarbons in the range C2 to C8; c. hydrotreating one or more of an FT syncrude fraction, a product from process b.,and an alkylated FT syncrude fraction; d. aromatizing one or more of an FT syncrude fraction including hydrocarbons in the range C2 to C8, a product from process a., a product from process b, a product from process c., and a product from an aromatic alkylation process; and e. alkylating one or more of an FT syncrude fraction including hydrocarbons in the C2 to C6 range, a product from process b., and a product from process d.
摘要翻译：本发明提供了具有超过60质量％的喷气燃料产率的费 - 托喷气燃料精炼方法，所述方法包括以下五种转化方法中的至少四种：a。加氢裂化一种或多种FT煤油和较重物质馏分以及C9和较重的FT合成馏分; 湾使包含C2至C8范围内的烃的FT顺式馏分低聚; C。加氢处理一种或多种FT顺式馏分，来自方法b的产物和烷基化的FT共聚物馏分; 天。将包括C2至C8范围内的烃的FT合成馏分中的一种或多种，来自方法a的产物，来自方法b的产物，来自方法c的产物和来自芳族烷基化方法的产物芳族化; 和e。将包括C2至C6范围内的碳氢化合物的FT合成馏分中的一种或多种，来自方法b的产物和来自方法d的产物烷基化。

3. 发明申请

WO2008144782A2 FISCHER-TROPSCH GASOLINE PROCESS 审中-公开
标题翻译： FISCHER-TROPSCH汽油加工
公开(公告)号：WO2008144782A2
公开(公告)日：2008-11-27
申请号：PCT/ZA2008000040
申请日：2008-05-20
申请人： SASOL TECH PTY LTD , DE KLERK ARNO
发明人： DE KLERK ARNO
CPC分类号： C10G11/00 , C10G2300/1022 , C10G2400/02
摘要： The invention provides a Fischer-Tropsch motor-gasoline refining process which has a motor-gasoline selectivity in excess of 65% by mass based on the total motor-gasoline, jet fuel, and distillate production and a yield of motor-gasoline, jet fuel and distillate in excess of 65% of the total C2 and heavier Fischer-Tropsch syncrude product, said process including at least three of the following six conversion processes: a. cracking FT kerosene and heavier material fraction or fractions from an FT syncrude; b. oligomerising one or more of an FT syncrude fraction including hydrocarbons in the range C2 to C8, and a product from process a.; c. hydrotreating one or more of an FT syncrude fraction, a product from process b.,and an alkylated FT syncrude fraction; d. aromatizing one or more of an FT syncrude fraction, including hydrocarbons in the range C2 to C8, a product from process a., a product from process b., a product from process c., and an product from an aromatic alkylation process; e. alkylating one or more of an FT syncrude fraction including hydrocarbons in the C2 to C6 range, a product from process b., and a product from process d; and f. skeletally isomerising one or more of an FT syncrude fraction including hydrocarbons in the C4 to C6 range, a product from process a., a product from process b., a product from process c., a product from process d., and a product from process e.
摘要翻译：本发明提供了一种费 - 托汽油精炼方法，其汽油选择性超过基于汽油，喷气燃料和馏出物总产量的65质量％，汽油，汽油，和蒸馏物超过总C2和较重费 - 托合成产物的65％，所述方法包括以下六种转化方法中的至少三种：a。从FT合成物中裂解FT煤油和较重物质馏分或馏分; 湾将包括C2至C8范围内的烃的FT合成馏分中的一种或多种低聚物和来自方法a的产物; C。加氢处理一种或多种FT顺式馏分，来自方法b的产物和烷基化的FT共聚物馏分; 天。使一个或多个FT合成部分芳构化，包括C2至C8范围内的烃，来自方法a的产物，来自方法b的产物，来自方法c的产物和来自芳族烷基化方法的产物; 即将包括C2至C6范围内的碳氢化合物的一个或多个FT合成馏分烷烃化，来自方法b的产物和来自方法d的产物; 和f。骨架异构化一种或多种包括C 4至C 6范围内的烃的FT合成馏分，来自方法a的产物，来自方法b的产物，来自方法c的产物，来自方法d的产物和产物从过程e

4. 发明专利

AU2008237023B2 Fischer-Tropsch jet fuel process 未知
公开(公告)号：AU2008237023B2
公开(公告)日：2012-02-16
申请号：AU2008237023
申请日：2008-04-10
申请人： SASOL TECH PTY LTD
发明人： DE KLERK ARNO
IPC分类号： C10G2/00 , C10G29/20 , C10G35/04 , C10G47/00 , C10G49/00 , C10G50/00 , C10G69/10 , C10G69/12 , C10G69/14
摘要： The invention provides a Fischer-Tropsch jet fuel refining process which has a jet fuel yield in excess of 60% by mass, said process including at least four of the following five conversion processes: a. hydrocracking one or more of a FT kerosene and heavier material fraction and a C9 and heavier FT syncrude fraction; b. oligomerising an FT syncrude fraction including hydrocarbons in the range C2 to C8; c. hydrotreating one or more of an FT syncrude fraction, a product from process b.,and an alkylated FT syncrude fraction; d. aromatizing one or more of an FT syncrude fraction including hydrocarbons in the range C2 to C8, a product from process a., a product from process b, a product from process c., and a product from an aromatic alkylation process; and e. alkylating one or more of an FT syncrude fraction including hydrocarbons in the C2 to C6 range, a product from process b., and a product from process d.

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