JP4731553B2 - 膨張するスラリー床内への気体の反応物質からの液体のまた任意に気体の炭化水素の生成 - Google Patents
膨張するスラリー床内への気体の反応物質からの液体のまた任意に気体の炭化水素の生成 Download PDFInfo
- Publication number
- JP4731553B2 JP4731553B2 JP2007512614A JP2007512614A JP4731553B2 JP 4731553 B2 JP4731553 B2 JP 4731553B2 JP 2007512614 A JP2007512614 A JP 2007512614A JP 2007512614 A JP2007512614 A JP 2007512614A JP 4731553 B2 JP4731553 B2 JP 4731553B2
- Authority
- JP
- Japan
- Prior art keywords
- slurry bed
- gaseous
- slurry
- gas
- recycle
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000002002 slurry Substances 0.000 title claims description 107
- 239000000376 reactant Substances 0.000 title claims description 47
- 229930195733 hydrocarbon Natural products 0.000 title claims description 25
- 150000002430 hydrocarbons Chemical class 0.000 title claims description 25
- 238000004519 manufacturing process Methods 0.000 title claims description 6
- 239000007788 liquid Substances 0.000 title description 7
- 239000007789 gas Substances 0.000 claims description 96
- 239000003054 catalyst Substances 0.000 claims description 36
- 238000006243 chemical reaction Methods 0.000 claims description 36
- 230000015572 biosynthetic process Effects 0.000 claims description 34
- 238000003786 synthesis reaction Methods 0.000 claims description 34
- 239000000047 product Substances 0.000 claims description 28
- 238000000034 method Methods 0.000 claims description 27
- 239000002245 particle Substances 0.000 claims description 26
- 239000000463 material Substances 0.000 claims description 25
- 239000004215 Carbon black (E152) Substances 0.000 claims description 20
- 239000012263 liquid product Substances 0.000 claims description 19
- 239000007791 liquid phase Substances 0.000 claims description 13
- 239000000725 suspension Substances 0.000 claims description 9
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 7
- 229910052739 hydrogen Inorganic materials 0.000 claims description 7
- 230000003134 recirculating effect Effects 0.000 claims description 5
- 239000007787 solid Substances 0.000 claims description 4
- 239000011949 solid catalyst Substances 0.000 claims description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 10
- 238000013461 design Methods 0.000 description 9
- 239000012071 phase Substances 0.000 description 9
- 238000000926 separation method Methods 0.000 description 8
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 6
- 238000001816 cooling Methods 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 5
- 239000001257 hydrogen Substances 0.000 description 5
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 3
- 229910017052 cobalt Inorganic materials 0.000 description 3
- 239000010941 cobalt Substances 0.000 description 3
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 3
- 238000004891 communication Methods 0.000 description 3
- 238000007872 degassing Methods 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000003345 natural gas Substances 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 238000009835 boiling Methods 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000003034 coal gas Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000006257 total synthesis reaction Methods 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2/00—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
- C10G2/30—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
- C10G2/32—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts
- C10G2/34—Apparatus, reactors
- C10G2/342—Apparatus, reactors with moving solid catalysts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
- B01J8/22—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
- C07C1/02—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon
- C07C1/04—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon from carbon monoxide with hydrogen
- C07C1/0405—Apparatus
- C07C1/041—Reactors
- C07C1/0415—Reactors with moving catalysts
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2/00—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
- C10G2/30—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
- C10G2/32—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts
- C10G2/34—Apparatus, reactors
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/582—Recycling of unreacted starting or intermediate materials
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Description
Claims (9)
- 気体の反応物質から、液体の生成物と、任意に気体の生成物とを生成する方法であって、
少なくともCOおよびH2を含む気体反応物質材料を、懸濁液体中に懸濁する固体で非シフト型の炭化水素合成用触媒粒子からなる膨張するスラリー床内に、低い高さから給送するステップであって、前記スラリー床は、容器に収容され、膨張するスラリー床は、アスペクト比が5未満である給送ステップと、
任意に、再循環ガス流を前記スラリー床内へ給送するステップと、
液体の生成物と、任意に気体の生成物とが形成されるように、前記気体反応物質と種々の再循環ガスとを、少なくとも35cm/秒の入口空塔速度で前記スラリー床の中を上方に通過させて、CO+H2の1回通過あたりの転化率を少なくとも60%で反応させ得るステップであって、前記気体反応物質および種々の再循環ガスと、前記種々の気体生成物とによって、前記固体の触媒粒子を懸濁状態で前記懸濁液体中に維持し、また、前記液体生成物は、前記懸濁液体とともに前記スラリー床の液相を形成する反応ステップと、
種々の気体生成物および反応しなかった気体反応物質と、反応しなかった種々の再循環ガスとを、前記スラリー床から、気体成分として、前記スラリー床上方のヘッドスペース内へ遊離させ得るステップと、
前記気体成分を前記ヘッドスペースから引き出すステップと、
前記スラリー床を所望の高さに維持するために液相を前記スラリー床から引き出すステップと、
前記再循環ガス流を提供するように、任意に、前記ヘッドスペースから前記気体成分のいくらかを再循環させるステップと、
を含む方法。 - 前記膨張するスラリー床は、高さが40m未満、直径が少なくとも6mである請求項1に記載の方法。
- 前記触媒粒子は、少なくとも14体積%の平均濃度で前記スラリー床中に存在する請求項1または2に記載の方法。
- 一段プロセスである請求項1から3のいずれかに記載の方法。
- 前記再循環ガス流は、少なくとも0.4の、再循環ガス流/気体反応物質材料の体積比で、存在し、前記スラリー床内に給送される請求項1から4のいずれかに記載の方法。
- フィッシャートロプシュ炭化水素合成プロセスである請求項1から5のいずれかに記載の方法。
- 前記再循環ガス流が存在し、少なくとも前記再循環ガス流の一部分を、追加のガス材料として、前記気体反応物質材料が前記スラリー床内へ給送される高さよりも上において、前記スラリー床内へ給送するステップを含む請求項1から6のいずれかに記載の方法。
- 気体反応物質材料に対する再循環ガス流の再循環比は、CO+H2の全ての転化率が80%よりも高い転化率で前記スラリー床が作動するのに十分大きい請求項1から7のいずれかに記載の方法。
- 前記スラリー床内において熱、液相、および触媒粒子を再分配するために、スラリー再分配手段またはスラリー再分配器を使用して、スラリーを、前記スラリー床内の高い所から下向きに低い所へ通過させ得るステップを含む請求項1から8のいずれかに記載の方法。
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ZA2004/3548 | 2004-05-10 | ||
ZA200403548 | 2004-05-10 | ||
PCT/IB2005/051382 WO2005107935A1 (en) | 2004-05-10 | 2005-04-28 | The production of liquid and, optionally, gaseous hydrocarbons from gaseous reactants into an expanded slurry bed |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2007536376A JP2007536376A (ja) | 2007-12-13 |
JP4731553B2 true JP4731553B2 (ja) | 2011-07-27 |
Family
ID=34965457
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2007512614A Expired - Fee Related JP4731553B2 (ja) | 2004-05-10 | 2005-04-28 | 膨張するスラリー床内への気体の反応物質からの液体のまた任意に気体の炭化水素の生成 |
Country Status (9)
Country | Link |
---|---|
US (1) | US7772291B2 (ja) |
JP (1) | JP4731553B2 (ja) |
AU (1) | AU2005240425B2 (ja) |
BR (1) | BRPI0510932B1 (ja) |
GB (1) | GB2429714B (ja) |
NL (1) | NL1028949C2 (ja) |
NO (1) | NO20065691L (ja) |
WO (1) | WO2005107935A1 (ja) |
ZA (1) | ZA200609313B (ja) |
Families Citing this family (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ITMI20062466A1 (it) * | 2006-12-21 | 2008-06-22 | Eni Spa | Reattore modulare per reazioni chimiche esotermiche-endotermiche |
US20090062166A1 (en) | 2007-08-28 | 2009-03-05 | Chevron U.S.A. Inc. | Slideway Lubricant Compositions, Methods of Making and Using Thereof |
US7956018B2 (en) | 2007-12-10 | 2011-06-07 | Chevron U.S.A. Inc. | Lubricant composition |
US8394154B2 (en) | 2007-12-28 | 2013-03-12 | Texaco Inc. | Counter-current oxidation and steam methane reforming process and reactor therefor |
US7989511B2 (en) | 2008-05-21 | 2011-08-02 | Texaco Inc. | Process and apparatus for synthesis gas and hydrocarbon production |
US8586685B2 (en) * | 2009-07-23 | 2013-11-19 | Univation Technologies, Llc | Polymerization reaction system |
US8349776B2 (en) | 2009-09-29 | 2013-01-08 | Chevron Oronite Company Llc | Trunk piston engine lubricating oil compositions |
US8455406B2 (en) | 2010-10-28 | 2013-06-04 | Chevron U.S.A. Inc. | Compressor oils having improved oxidation resistance |
CN103459572A (zh) | 2011-04-05 | 2013-12-18 | 雪佛龙奥伦耐有限责任公司 | 低粘度船用气缸润滑油组合物 |
AU2012265887B2 (en) | 2011-06-07 | 2016-12-22 | Sasol Technology (Proprietary) Limited | Process for producing at least one product from at least one gaseous reactant in a slurry bed |
CA2838462C (en) | 2011-06-07 | 2020-04-21 | Sasol Technology (Proprietary) Limited | Process for producing at least one product from at least one gaseous reactant in a slurry bed |
CN103765986B (zh) | 2011-08-04 | 2017-03-29 | S·L·坎宁安 | 等离子电弧炉和应用 |
US9206374B2 (en) | 2011-12-16 | 2015-12-08 | Chevron Oronite Sas | Trunk piston engine lubricating oil compositions |
US10364403B2 (en) | 2013-11-06 | 2019-07-30 | Chevron Oronite Technology B.V. | Marine diesel cylinder lubricant oil compositions |
SG11201603378WA (en) | 2013-11-06 | 2016-05-30 | Chevron Oronite Technology Bv | Marine diesel cylinder lubricant oil compositions |
EP3140601A4 (en) | 2014-05-09 | 2017-11-08 | Stephen Lee Cunningham | Arc furnace smeltering system & method |
JP6518480B2 (ja) * | 2015-03-30 | 2019-05-22 | 株式会社クボタ | 気泡塔型スラリー床反応装置 |
CN107849481B (zh) | 2015-07-22 | 2021-09-03 | 雪佛龙奥伦耐技术有限责任公司 | 船用柴油机汽缸润滑油组合物 |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20020035163A1 (en) * | 1999-02-05 | 2002-03-21 | Sasol Technology (Proprietary) Limited | Process for producing liquid and, optionally, gaseous products from gaseous reactants |
JP2002510246A (ja) * | 1997-07-15 | 2002-04-02 | サソール テクノロジー(プロプライエタリー)リミテッド | ガス状反応物から液体生成物及び場合によりガス状生成物を製造する方法 |
US20030114543A1 (en) * | 2001-12-14 | 2003-06-19 | Jianping Zhang | Slurry bed reactor |
WO2003068715A1 (en) * | 2002-02-13 | 2003-08-21 | Sasol Technology (Proprietary) Limited | Process for starting up a fischer-tropsch reactor |
WO2003084906A1 (en) * | 2002-04-04 | 2003-10-16 | Chevron U.S.A. Inc. | Condensation of olefins in fischer tropsch tail gas |
JP2007501121A (ja) * | 2003-05-16 | 2007-01-25 | サソル テクノロジー (プロプリエタリ) リミテッド | ガス状反応物から液状生成物を生成し、任意でガス状生成物を生成する方法 |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2276274A (en) | 1937-08-04 | 1942-03-17 | Kellogg M W Co | Method of synthesizing hydrocarbons |
US2463912A (en) * | 1946-12-12 | 1949-03-08 | Standard Oil Dev Co | Synthesis of hydrocarbons |
CA2038774C (en) | 1990-04-04 | 2001-09-25 | Eric Herbolzheimer | Slurry bubble column |
JP3613486B2 (ja) | 1995-02-23 | 2005-01-26 | 大倉工業株式会社 | 炭化珪素ウイスカーの製造方法 |
DZ2013A1 (fr) | 1995-04-07 | 2002-10-23 | Sastech Ltd | Catalyseurs. |
FR2751564B1 (fr) | 1996-07-26 | 2001-10-12 | Inst Francais Du Petrole | Procede et dispositif pour le fonctionnement d'une colonne a bulles triphasique avec application en synthese fischer-tropsch |
FR2806736B1 (fr) | 2000-03-27 | 2002-05-10 | Inst Francais Du Petrole | Procede de production d'hydrocarbures a partir de gaz de synthese dans un reacteur triphasique |
CA2454237C (en) | 2001-07-25 | 2008-05-27 | Conocophillips Company | Optimizing the production rate of slurry bubble reactors by using large gas flow rates and moderate single pass conversion |
-
2005
- 2005-04-28 JP JP2007512614A patent/JP4731553B2/ja not_active Expired - Fee Related
- 2005-04-28 WO PCT/IB2005/051382 patent/WO2005107935A1/en active Application Filing
- 2005-04-28 AU AU2005240425A patent/AU2005240425B2/en not_active Ceased
- 2005-04-28 BR BRPI0510932-9A patent/BRPI0510932B1/pt active IP Right Grant
- 2005-04-28 GB GB0622803A patent/GB2429714B/en not_active Expired - Fee Related
- 2005-04-28 US US11/596,253 patent/US7772291B2/en active Active
- 2005-05-03 NL NL1028949A patent/NL1028949C2/nl not_active IP Right Cessation
-
2006
- 2006-11-08 ZA ZA200609313A patent/ZA200609313B/xx unknown
- 2006-12-11 NO NO20065691A patent/NO20065691L/no not_active Application Discontinuation
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002510246A (ja) * | 1997-07-15 | 2002-04-02 | サソール テクノロジー(プロプライエタリー)リミテッド | ガス状反応物から液体生成物及び場合によりガス状生成物を製造する方法 |
US20020035163A1 (en) * | 1999-02-05 | 2002-03-21 | Sasol Technology (Proprietary) Limited | Process for producing liquid and, optionally, gaseous products from gaseous reactants |
US20030114543A1 (en) * | 2001-12-14 | 2003-06-19 | Jianping Zhang | Slurry bed reactor |
WO2003068715A1 (en) * | 2002-02-13 | 2003-08-21 | Sasol Technology (Proprietary) Limited | Process for starting up a fischer-tropsch reactor |
WO2003084906A1 (en) * | 2002-04-04 | 2003-10-16 | Chevron U.S.A. Inc. | Condensation of olefins in fischer tropsch tail gas |
JP2007501121A (ja) * | 2003-05-16 | 2007-01-25 | サソル テクノロジー (プロプリエタリ) リミテッド | ガス状反応物から液状生成物を生成し、任意でガス状生成物を生成する方法 |
Also Published As
Publication number | Publication date |
---|---|
NL1028949A1 (nl) | 2005-11-11 |
GB2429714A (en) | 2007-03-07 |
US20080293834A1 (en) | 2008-11-27 |
GB2429714B (en) | 2008-12-17 |
BRPI0510932A (pt) | 2008-07-15 |
BRPI0510932B1 (pt) | 2015-05-05 |
NL1028949C2 (nl) | 2006-02-24 |
NO20065691L (no) | 2007-02-02 |
US7772291B2 (en) | 2010-08-10 |
JP2007536376A (ja) | 2007-12-13 |
AU2005240425B2 (en) | 2010-12-02 |
WO2005107935A1 (en) | 2005-11-17 |
ZA200609313B (en) | 2008-04-30 |
GB0622803D0 (en) | 2006-12-27 |
AU2005240425A1 (en) | 2005-11-17 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP4731553B2 (ja) | 膨張するスラリー床内への気体の反応物質からの液体のまた任意に気体の炭化水素の生成 | |
US20080299022A1 (en) | Process for producing liquid and, optionally, gaseous products from gaseous reactants | |
WO2007069317A1 (ja) | 気泡塔型フィッシャー・トロプシュ合成スラリー床反応システム | |
JP4203129B2 (ja) | ガス状反応物から液体生成物及び場合によりガス状生成物を製造する方法 | |
JP4456947B2 (ja) | 気泡塔型フィッシャー・トロプシュ合成スラリー床反応システム | |
US20080146682A1 (en) | Production of Liquid and, Optionally, Gaseous Products from Gaseous Reactants | |
US9080108B2 (en) | Process for producing at least one product from at least one gaseous reactant in a slurry bed | |
US9487710B2 (en) | Process for producing at least one product from at least one gaseous reactant in a slurry bed | |
NZ618388B2 (en) | Process for producing at least one product from at least one gaseous reactant in a slurry bed | |
NZ618392B2 (en) | Process for producing at least one product from at least one gaseous reactant in a slurry bed |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20080222 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20101102 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20110202 |
|
TRDD | Decision of grant or rejection written | ||
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20110329 |
|
A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20110419 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20140428 Year of fee payment: 3 |
|
R150 | Certificate of patent or registration of utility model |
Free format text: JAPANESE INTERMEDIATE CODE: R150 Ref document number: 4731553 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
LAPS | Cancellation because of no payment of annual fees |