公开(公告)号：JP2012183536A

公开(公告)日：2012-09-27

申请号：JP2012102784

申请日：2012-04-27

Applicant: Statoil Asa ,  Petro Sa ,  スタトイル・エーエスエー ,  ペトロエスエー

Inventor： RYTTER ERLING ,  SKAGSETH TORILD HULSUND ,  WIGUM HANNE ,  SINCADU NONYAMEKO

IPC: B01J23/889 ,  B01J21/00 ,  B01J23/00 ,  B01J23/36 ,  B01J23/75 ,  B01J23/755 ,  B01J23/80 ,  B01J23/83 ,  B01J23/89 ,  B01J35/00 ,  B01J35/10 ,  B01J37/02 ,  C07C1/04 ,  C10G2/00 ,  C10G45/58 ,  C10G47/00

CPC classification number: 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

Abstract: PROBLEM TO BE SOLVED: To provide an alumina-supported cobalt catalyst used in Fisher-Tropsch synthesis reaction.SOLUTION: A method of producing the alumina-supported cobalt catalyst includes calcining an initial γ-alumina-supported material at a temperature of at least 550°C to generate a modified alumina support material, impregnating the modified alumina support material with a source of cobalt, calcining the impregnated support material at a temperature from 700°C to 1,200°C, and activating the catalyst.

Abstract translation: 待解决的问题：提供用于费 - 托合成反应的氧化铝负载的钴催化剂。 解决方案：一种生产负载氧化铝的钴催化剂的方法包括在至少550℃的温度下煅烧初始的γ-氧化铝负载的材料以产生改性氧化铝载体材料，用改性的氧化铝载体材料浸渍 在700℃至1200℃的温度下焙烧浸渍的载体材料并活化催化剂。 版权所有（C）2012，JPO＆INPIT

公开(公告)号：WO2004043596A3

公开(公告)日：2004-08-12

申请号：PCT/GB0304873

申请日：2003-11-10

Applicant: STATOIL ASA ,  PETRO SA ,  RYTTER ERLING ,  ERI SIGRID ,  SCHANKE DAG ,  REES DAVID CHRISTOPHER

Inventor： RYTTER ERLING ,  ERI SIGRID ,  SCHANKE DAG

IPC: B01J23/75 ,  B01J23/889 ,  B01J35/02 ,  B01J35/10 ,  C10G2/00 ,  C07C1/04

CPC classification number: C10G2/332 ,  B01J23/75 ,  B01J23/8896 ,  B01J35/023 ,  B01J35/10 ,  B01J35/1019 ,  B01J35/1042 ,  B01J35/1061 ,  C10G2300/703

Abstract: 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 /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 /g.

Abstract translation: 一种用于费 - 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20-100μm; 浸渍和煅烧的催化剂颗粒的比表面积大于80m 2 / g; 浸渍和煅烧的催化剂的平均孔径至少为90（9nm）; 并且浸渍和煅烧的催化剂的孔体积大于0.35cm 3 / g。

公开(公告)号：WO2006112724A3

公开(公告)日：2007-02-22

申请号：PCT/NO2006000142

申请日：2006-04-19

Applicant: STATOIL ASA ,  DE KOEIJER GELEIN ,  RYTTER ERLING ,  SIVERTSEN BOERGE RYGH ,  KOBRO HENRIK

Inventor： DE KOEIJER GELEIN ,  RYTTER ERLING ,  SIVERTSEN BOERGE RYGH ,  KOBRO HENRIK

IPC: C01B3/38 ,  B01D53/047 ,  B01D53/22 ,  C01B20060101 ,  C01B3/34 ,  C01B3/48 ,  C01B3/56 ,  C01B13/02 ,  C01B32/50

CPC classification number: F02C3/22 ,  C01B3/34 ,  C01B3/48 ,  C01B3/56 ,  C01B13/0233 ,  C01B13/0248 ,  C01B13/0251 ,  C01B13/0259 ,  C01B13/0288 ,  C01B32/50 ,  C01B2203/0233 ,  C01B2203/0283 ,  C01B2203/04 ,  C01B2203/0405 ,  C01B2203/043 ,  C01B2203/047 ,  C01B2203/0475 ,  C01B2203/048 ,  C01B2203/0495 ,  C01B2203/0816 ,  C01B2203/0822 ,  C01B2203/0827 ,  C01B2210/0046 ,  F23C2900/99011 ,  F23L2900/07002 ,  Y02E20/16 ,  Y02P20/128 ,  Y02P20/13

Abstract: A process for the production of electric energy and CO2 from a hydrocarbon feedstock 1 comprising steam reforming of the feedstock producing synthesis gas (22) wherein the the synthesis gas is separated into a hydrogen rich and carbon lean stream (50) said hydrogen rich and carbon lean stream is combusted with compressed air for producing a combustion product which is expanded in a turbine (6) generating electric energy, said rest stream (50) is recirculated as fuel (52) for producing heat for said steam reforming is described. Further a power plant for performing the process is described.

Abstract translation: 一种从烃原料1生产电能和二氧化碳的方法，包括原料产生合成气（22）的蒸汽重整，其中合成气被分离成富氢和贫碳物流（50），所述富氢和碳 贫气流与压缩空气一起燃烧，用于产生在产生电能的涡轮机（6）中膨胀的燃烧产物，所述休息流（50）作为用于产生用于所述蒸汽重整的热量的燃料（52）再循环。 此外，还描述了用于执行该过程的发电厂。

公开(公告)号：WO2007141558A3

公开(公告)日：2008-04-10

申请号：PCT/GB2007002165

申请日：2007-06-11

Applicant: STATOIL ASA ,  COCKBAIN JULIAN ,  EDWIN EMIL ,  BRUSTAD MORTEN ,  AASER KNUT-IVAR ,  RYTTER ERLING ,  MIKKELSEN OYVIND ,  JOHANSEN JOHAN ARNOLD

Inventor： EDWIN EMIL ,  BRUSTAD MORTEN ,  AASER KNUT-IVAR ,  RYTTER ERLING ,  MIKKELSEN OYVIND ,  JOHANSEN JOHAN ARNOLD

IPC: D01F9/133 ,  B01J8/10 ,  C01B31/02

CPC classification number: D01F9/133 ,  B01J8/003 ,  B01J8/004 ,  B01J8/0045 ,  B01J8/085 ,  B01J8/10 ,  B01J19/02 ,  B01J2208/00176 ,  B01J2208/00203 ,  B01J2208/00212 ,  B01J2208/00309 ,  B01J2208/0053 ,  B01J2208/0084 ,  B01J2219/0218 ,  B01J2219/0286 ,  C01B32/05

Abstract: This invention provides a reactor (1) for carbon nano- fibre production comprising a generally horizontal elongate cylindrical reaction vessel (902) arranged to rotate about its cylindrical axis and containing in use a particulate catalyst-containing reaction bed (72), said reaction vessel having a gas inlet port (1001) and a gas outlet port (1002) positioned such that one of said inlet and outlet ports is in said bed and the other is outside said bed.

Abstract translation: 本发明提供了一种用于碳纳米纤维生产的反应器（1），其包括大致水平的细长圆柱形反应容器（902），其布置成围绕其圆柱轴线旋转并且在使用中包含含颗粒催化剂的反应床（72），所述反应容器 具有气体入口（1001）和气体出口（1002），其定位成使得所述入口和出口中的一个位于所述床中，而另一个位于所述床之外。

公开(公告)号：WO0187773A9

公开(公告)日：2003-07-24

申请号：PCT/NO0100196

申请日：2001-05-11

Applicant: STATOIL ASA ,  RYTTER ERLING ,  ROENNEKLEIV MORTEN ,  OLSBYE UNNI

Inventor： RYTTER ERLING ,  ROENNEKLEIV MORTEN ,  OLSBYE UNNI

IPC: B01J23/00 ,  C01B13/36 ,  C01F7/00 ,  C07C5/32

CPC classification number: C01B13/363 ,  B01J23/007 ,  C01F7/005 ,  C01P2002/22 ,  C01P2002/72 ,  C07C5/325 ,  C07C2521/16 ,  C07C2523/14 ,  C07C2523/42 ,  C07C2523/62

Abstract: A hydrotalcite-based material having an improved mechanical strength, said hydrotalcite having the following general formula: M aM b(OH)c(A )d xH2O wherein M is at least one divalent metal; M is at least one trivalent metal; A is an n-valent anion, n is 1 or 2 and a and b are positive numbers, a > b, which hydrotalcite is deposited on alumina or an alumina precursor, a process of preparing said hydrotalcite-based material, the use thereof as a catalyst support material, a catalyst for the dehydrogenation of propane, and a process using such a catalyst in the dehydrogenation of propane.

Abstract translation: 具有改善的机械强度的水滑石基材料，所述水滑石具有以下通式：M 2+ aM 3+ b（OH）c（A n - ）d x x H 2 O其中M 2 +>为至少一种二价金属; M 3+是至少一种三价金属; A是n价阴离子，n为1或2，a和b为正数，a> b，其中水滑石沉积在氧化铝或氧化铝前体上，制备所述水滑石基材料的方法，其用途为 催化剂载体材料，用于丙烷脱氢的催化剂，以及在丙烷脱氢中使用这种催化剂的方法。

公开(公告)号：WO2005052229A3

公开(公告)日：2005-07-28

申请号：PCT/GB2004004920

申请日：2004-11-22

Applicant: STATOIL ASA ,  EDWIN EMIL ,  ARNESEN TORE ,  AASER KNUT-IVAR ,  RYTTER ERLING ,  JOHANSEN JOHAN ARNOLD ,  FORS JOHN ,  COCKBAIN JULIAN R M

Inventor： EDWIN EMIL ,  ARNESEN TORE ,  AASER KNUT-IVAR ,  RYTTER ERLING ,  JOHANSEN JOHAN ARNOLD ,  FORS JOHN

IPC: B01J8/00 ,  B01J8/02 ,  B01J8/12 ,  B01J8/24 ,  B01J8/28 ,  B01J19/02 ,  C01B3/00 ,  C01B3/26 ,  C01B31/02 ,  D01F9/127 ,  D01F9/133

CPC classification number: D01F9/1272 ,  B01J4/002 ,  B01J8/003 ,  B01J8/004 ,  B01J8/0055 ,  B01J8/006 ,  B01J8/009 ,  B01J8/0264 ,  B01J8/0278 ,  B01J8/12 ,  B01J8/125 ,  B01J8/24 ,  B01J8/28 ,  B01J19/02 ,  B01J2208/00176 ,  B01J2208/00415 ,  B01J2208/00495 ,  B01J2208/0053 ,  B01J2219/0218 ,  B01J2219/185 ,  B01J2219/1941 ,  B01J2219/1943 ,  B01J2219/1946 ,  B82Y30/00 ,  C01B3/0021 ,  C01B3/26 ,  C01B32/05 ,  D01F9/127 ,  D01F9/1271 ,  D01F9/1273 ,  D01F9/1278 ,  D01F9/133 ,  Y02E60/325 ,  Y10S977/843

Abstract: This invention relates to a method for the production of particulate carbon products in a reactor vessel wherein gas flow between a gas inlet port and a gas outlet port suspends a bed of catalyst-containing particulate material in said vessel and wherein the product is discharged from said vessel by falling from the bed.

Abstract translation: 本发明涉及一种用于在反应器容器中生产颗粒状碳产品的方法，其中在气体入口和气体出口之间的气流悬浮在所述容器中的含催化剂的颗粒材料床，并且其中产物从所述 船从床上掉下来。

公开(公告)号：CA2509945C

公开(公告)日：2011-10-11

申请号：CA2509945

申请日：2003-12-12

Applicant: STATOIL ASA

Inventor： OLSVIK OLA ,  RYTTER ERLING ,  SOGGE JOSTEIN ,  STENSEN JAN AGE

IPC: E21B43/16 ,  E21B43/40 ,  F25J3/04

Abstract: A method for increasing oil recovery from an oil reservoir by injection of gas into the reservoir, is described. The method comprises separation of air into an oxygen-rich fraction and a nitrogen-rich fraction, reformation of natural gas together with oxygen to produce a synthesis gas for production of methanol or other oxygenated hydrocarbons or higher hydrocarbons. The raw synthesis products and a waste gas from the synthesis are separated, and the nitrogen-rich fraction and at least a part of the waste gas are injected into the oil reservoir to increase the oil recovery from the reservoir. A plant for performing the method is also described.

公开(公告)号：NO20090086A

公开(公告)日：2009-03-09

申请号：NO20090086

申请日：2009-01-06

Applicant: STATOIL ASA

Inventor： EDWIN EMIL ,  BRUSTAD MORTEN ,  AASER KNUT-IVAR ,  RYTTER ERLING ,  MIKKELSEN OYVIND ,  JOHANSEN JOHAN ARNOLD

IPC: B01J19/28 ,  B01J8/00 ,  B01J8/10 ,  B01J8/18 ,  D01F9/133

CPC classification number: D01F9/133 ,  B01J8/003 ,  B01J8/004 ,  B01J8/0045 ,  B01J8/085 ,  B01J8/10 ,  B01J19/02 ,  B01J2208/00176 ,  B01J2208/00203 ,  B01J2208/00212 ,  B01J2208/00309 ,  B01J2208/0053 ,  B01J2208/0084 ,  B01J2219/0218 ,  B01J2219/0286 ,  C01B32/05

公开(公告)号：AU2003301952B2

公开(公告)日：2009-01-15

申请号：AU2003301952

申请日：2003-11-10

Applicant: PETROLEUM OIL & GAS CORPORATION OF SOUTH AFRICA PTY LTD ,  STATOIL ASA

Inventor： ERI SIGRID ,  SCHANKE DAG ,  RYTTER ERLING

IPC: B01J35/10 ,  B01J23/75 ,  B01J23/889 ,  B01J35/02 ,  C10G2/00

公开(公告)号：NO20071464L

公开(公告)日：2008-09-22

申请号：NO20071464

申请日：2007-03-19

Applicant: STATOIL ASA

Inventor： RYTTER ERLING ,  BORRESEN BORRE TORE ,  AARTUN INGRID ,  KROGH BENTE ,  RONNEKLEIV MORTEN

IPC: B01J20/02 ,  B01D53/04 ,  B01J20/04 ,  C01B3/00 ,  C01B3/56

Abstract: A method for production of hydrogen including reforming of a carbon comprising fuel is provided together with production plants adapted for obtaining hydrogen at lower temperatures and/or higher pressures and obtaining a CO2 rich rest gas stream. A reformer and a water gas shift reactor are also provided.