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1. 发明申请

WO2005065813A1 HEAT EXCHANGE SYSTEM FOR A SLURRY BUBBLE COLUMN REACTOR 审中-公开
标题翻译：一种浆状泡沫反应器的热交换系统
公开(公告)号：WO2005065813A1
公开(公告)日：2005-07-21
申请号：PCT/GB2005/000040
申请日：2005-01-07
申请人： STATOIL ASA , PETROSA , REES, David Christopher , SORAKER Pal , LIAN Petter , VANKAN Sander
发明人： SORAKER Pal , LIAN Petter , VANKAN Sander
IPC分类号： B01J8/22
CPC分类号： B01J8/1836 , B01J8/22 , B01J2208/00132 , C10G2/343 , F28D7/163 , F28F9/0132 , F28F9/0275
摘要： A heat exchange system for a slurry bubble column reactor (11), comprising a bundle of generally parallel heat exchange tubes (16) for transporting heat exchange fluid in the longitudinal direction of the column, a header (24) at one end of the tube bundle for supplying heat exchange fluid to or removing heat exchange fluid from the tubes (16); and two or more sub-headers (25) connected to the header (24) via distribution conduits (26). The sub-headers (25) are also connected to the tubes (16), thereby connecting the header (24) to the tubes (16). The sub-headers (25) are located at at least two different positions in the longitudinal direction of the tubes (16) and at least two different positions in the transverse direction of the tubes (16).
摘要翻译：一种用于浆液鼓泡塔反应器（11）的热交换系统，包括一组大致平行的热交换管（16），用于沿塔的纵向方向传送热交换流体，管的一端处的集管（24）用于向所述管（16）供应热交换流体或从所述管（16）除去热交换流体的束; 以及经由分配管道（26）连接到集管（24）的两个或更多个子集管（25）。子集管（25）也连接到管（16），从而将集管（24）连接到管（16）。子集管（25）位于管（16）的纵向方向上的至少两个不同位置和管（16）的横向方向上的至少两个不同位置。

2. 发明申请

WO2005082512A1 DOWNCOMERS FOR SLURRY BUBBLE COLUMN REACTORS 审中-公开
标题翻译：浆料泡沫柱反应器的代表
公开(公告)号：WO2005082512A1
公开(公告)日：2005-09-09
申请号：PCT/GB2005/000579
申请日：2005-02-17
申请人： STATOIL ASA , PETROSA , REES, David, Christopher , MYRSTAD, Trond , SORAKER, Pal , JULIUSSEN, Olav , WIIG, Per, Oscar
发明人： MYRSTAD, Trond , SORAKER, Pal , JULIUSSEN, Olav , WIIG, Per, Oscar
IPC分类号： B01J8/22
CPC分类号： B01J8/226
摘要： A slurry bubble column reactor (11) arranged in use to include a slurry phase (12) and above the slurry phase (12), a gas phase (15), the reactor (11) includes a downcomer (16) secured within it. The downcomer (16) comprises an elongate tube, the tube having a lower portion (18) and an upper portion (17). The lower portion (18) has a slurry outlet in the region of the bottom of the tube while the upper portion (17) has a slurry inlet arranged to allow slurry to enter the tube and a gas outlet (21) in the region of the top of the tube. The slurry inlet comprises a series of slots (22) in the wall of the upper portion. The uppermost part of the upper portion (17) extends above the surface of the slurry phase (12) in use and is open for fluid communication with the gas phase (15) above the slurry phase (12), thereby providing the gas outlet (21), and the slots (22) in the upper portion (17) are at a position below the surface of the slurry (12) in use.
摘要翻译：浆料鼓泡塔反应器（11），其布置在使用中以包括淤浆相（12）和浆料相（12）之上，气相（15），反应器（11）包括固定在其内的降液管（16）。降液管（16）包括细长管，该管具有下部（18）和上部（17）。下部（18）在管的底部区域具有浆料出口，而上部（17）具有布置成允许浆料进入管的浆料入口和在该区域内的气体出口（21）管顶。浆料入口包括在上部壁的壁中的一系列狭槽（22）。上部（17）的最上部在使用中在浆液相（12）的表面上方延伸，并且与浆液相（12）上方的气相（15）开放以便流体连通，由此提供气体出口 21），并且上部（17）中的槽（22）在使用中处于浆液（12）的表面下方的位置。

3. 发明申请

WO2004043596A2 FISCHER-TROPSCH CATALYSTS 审中-公开
标题翻译： FISCHER-TROPSCH催化剂
公开(公告)号：WO2004043596A2
公开(公告)日：2004-05-27
申请号：PCT/GB2003/004873
申请日：2003-11-10
申请人： STATOIL ASA , PETROSA , REES, David, Christopher , RYTTER, Erling , ERI, Sigrid , SCHANKE, Dag
发明人： RYTTER, Erling , ERI, Sigrid , SCHANKE, Dag
IPC分类号： B01J35/10
CPC分类号： C10G2/332 , B01J23/75 , B01J23/8896 , B01J35/023 , B01J35/10 , B01J35/1019 , B01J35/1042 , B01J35/1061 , C10G2300/703
摘要： A catalyst for use in a Fischer-Tropsch synthesis reaction which comprises cobalt supported on alumina, in which: the catalyst average particle size is in the range 20 to 100 µm; the specific surface area of the impregnated and calcined catalyst particles is greater than 80 m 2 /g; the average pore size of the impregnated and calcined catalyst is at least 90Å (9nm); and the pore volume of the impregnated and calcined catalyst is greater than 0.35 cm 3 /g.
摘要翻译：用于费 - 托合成反应的催化剂，其包含负载在氧化铝上的钴，其中：催化剂平均粒度为20-100微米; 浸渍和煅烧的催化剂颗粒的比表面积大于80m 2 / g; 浸渍并煅烧的催化剂的平均孔径至少为90埃; （9纳米）; 并且浸渍并煅烧的催化剂的孔体积大于0.35cm 3 / g。

4. 发明申请

WO2005072866A1 FISCHER-TROPSCH CATALYSTS 审中-公开
标题翻译： FISCHER-TROPSCH催化剂
公开(公告)号：WO2005072866A1
公开(公告)日：2005-08-11
申请号：PCT/GB2005/000287
申请日：2005-01-27
申请人： STATOIL ASA , PETROSA , REES, David, Christopher , RYTTER, Erling , SKAGSETH, Torild, Hulsund , WIGUM, Hanne , SINCADU, Nonyameko
发明人： RYTTER, Erling , SKAGSETH, Torild, Hulsund , WIGUM, Hanne , SINCADU, Nonyameko
IPC分类号： B01J23/75
CPC分类号： C10G47/00 , B01J21/005 , B01J23/005 , B01J23/36 , B01J23/75 , B01J23/755 , B01J23/80 , B01J23/83 , B01J23/8896 , B01J23/8913 , B01J23/892 , B01J35/002 , B01J35/1014 , B01J35/109 , B01J35/1095 , B01J37/0205 , B01J37/0207 , C10G2/331 , C10G2/332 , C10G2/333 , C10G2/342 , C10G45/58 , C10G2300/703
摘要： A method of producing an alumina-supported catalyst for use in a Fischer-Tropsch synthesis reaction, which comprises: calcining an initial γ-alumina support material at a temperature of at least 550°C to produce a modified alumina support material; impregnating the modified alumina support material with a source cobalt; calcining the impregnated support material at a temperature of 700°C to 1200°C, and activating the catalyst.
摘要翻译：一种制备用于费 - 托合成反应的氧化铝负载的催化剂的方法，其包括：在至少550℃的温度下煅烧初始γ-氧化铝载体材料以产生改性的氧化铝载体材料; 用源钴浸渍改性氧化铝载体材料; 在700℃至1200℃的温度下煅烧浸渍的载体材料，并活化催化剂。

5. 发明申请

WO2004055322A1 A METHOD FOR OIL RECOVERY FROM AN OIL FIELD 审中-公开
标题翻译：一种从油田中回收油的方法
公开(公告)号：WO2004055322A1
公开(公告)日：2004-07-01
申请号：PCT/NO2002/000477
申请日：2002-12-13
申请人： STATOIL ASA , PETROSA (THE PETROLEUM OIL & GAS CORPORATION OF SA (PTY) LTD , SHAW, Gareth, David, Huntley , OLSVIK, Ola , RYTTER, Erling , SOGGE, Jostein , STENSEN, Jan, Åge
发明人： SHAW, Gareth, David, Huntley , OLSVIK, Ola , RYTTER, Erling , SOGGE, Jostein , STENSEN, Jan, Åge
IPC分类号： E21B43/16
CPC分类号： C10G2/32 , C01B3/382 , C01B2203/0244 , C01B2203/0283 , C01B2203/062 , C01B2203/0844 , C01B2203/1241 , C01B2203/142 , C01B2203/82 , C01B2203/84 , E21B43/168
摘要： A method for increasing oil recovery from an oil reservoir in which method surplus gas streams from a plant for synthesis of higher hydrocarbons from natural gas is injected into the reservoir, is described. The surplus streams from the plant is the tailgas from the synthesis and optionally nitrogen from an air separation unit which delivers oxygen or oxygen enriched air to the plant for synthesis of higher hydrocarbons.
摘要翻译：描述了一种用于从储油器中提高采油的方法，其中方法将来自用于合成来自天然气的高级烃的工厂的剩余气流注入储存器。来自植物的剩余物流是来自合成的尾气和任选的来自空气分离单元的氮气，其将氧气或富氧空气输送到用于合成高级烃的工厂。

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