NO317282B1 - Fremgangsmate for drift av en kolonne av trefasebobler under anvendelse av Fischer-Tropsch-syntesen - Google Patents
Fremgangsmate for drift av en kolonne av trefasebobler under anvendelse av Fischer-Tropsch-syntesen Download PDFInfo
- Publication number
- NO317282B1 NO317282B1 NO19973457A NO973457A NO317282B1 NO 317282 B1 NO317282 B1 NO 317282B1 NO 19973457 A NO19973457 A NO 19973457A NO 973457 A NO973457 A NO 973457A NO 317282 B1 NO317282 B1 NO 317282B1
- Authority
- NO
- Norway
- Prior art keywords
- reactor
- suspension
- recirculation
- liquid
- reaction
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims description 37
- 230000008569 process Effects 0.000 title claims description 13
- 230000015572 biosynthetic process Effects 0.000 title description 22
- 238000003786 synthesis reaction Methods 0.000 title description 22
- 239000000725 suspension Substances 0.000 claims description 48
- 238000006243 chemical reaction Methods 0.000 claims description 37
- 239000007788 liquid Substances 0.000 claims description 37
- 239000003054 catalyst Substances 0.000 claims description 34
- 239000007787 solid Substances 0.000 claims description 27
- 239000002245 particle Substances 0.000 claims description 22
- 239000002002 slurry Substances 0.000 claims description 19
- 239000000376 reactant Substances 0.000 claims description 13
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 11
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 11
- 229930195733 hydrocarbon Natural products 0.000 claims description 8
- 150000002430 hydrocarbons Chemical class 0.000 claims description 8
- 238000005984 hydrogenation reaction Methods 0.000 claims description 4
- 238000004062 sedimentation Methods 0.000 claims description 4
- 238000000926 separation method Methods 0.000 claims description 3
- 238000005899 aromatization reaction Methods 0.000 claims description 2
- 238000001914 filtration Methods 0.000 claims description 2
- 238000007037 hydroformylation reaction Methods 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 claims description 2
- 239000007789 gas Substances 0.000 description 45
- 239000012071 phase Substances 0.000 description 17
- 239000007791 liquid phase Substances 0.000 description 14
- 229910017052 cobalt Inorganic materials 0.000 description 10
- 239000010941 cobalt Substances 0.000 description 10
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 10
- 238000004064 recycling Methods 0.000 description 9
- 239000000047 product Substances 0.000 description 7
- 229910052739 hydrogen Inorganic materials 0.000 description 6
- 239000001257 hydrogen Substances 0.000 description 6
- 238000012546 transfer Methods 0.000 description 6
- 239000004215 Carbon black (E152) Substances 0.000 description 5
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 239000012190 activator Substances 0.000 description 4
- 239000006185 dispersion Substances 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 229910052707 ruthenium Inorganic materials 0.000 description 4
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 3
- 230000033228 biological regulation Effects 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 3
- 238000013461 design Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000012263 liquid product Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 229910052750 molybdenum Inorganic materials 0.000 description 3
- 239000011733 molybdenum Substances 0.000 description 3
- 239000012188 paraffin wax Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 2
- 229910052770 Uranium Inorganic materials 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 125000004432 carbon atom Chemical group C* 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 239000003085 diluting agent Substances 0.000 description 2
- 239000013529 heat transfer fluid Substances 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 235000012239 silicon dioxide Nutrition 0.000 description 2
- DNYWZCXLKNTFFI-UHFFFAOYSA-N uranium Chemical compound [U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U] DNYWZCXLKNTFFI-UHFFFAOYSA-N 0.000 description 2
- 229910052684 Cerium Inorganic materials 0.000 description 1
- 229910052779 Neodymium Inorganic materials 0.000 description 1
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 1
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 1
- 150000001342 alkaline earth metals Chemical class 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000010531 catalytic reduction reaction Methods 0.000 description 1
- ZMIGMASIKSOYAM-UHFFFAOYSA-N cerium Chemical compound [Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce] ZMIGMASIKSOYAM-UHFFFAOYSA-N 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000007809 chemical reaction catalyst Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- QUQFTIVBFKLPCL-UHFFFAOYSA-L copper;2-amino-3-[(2-amino-2-carboxylatoethyl)disulfanyl]propanoate Chemical compound [Cu+2].[O-]C(=O)C(N)CSSCC(N)C([O-])=O QUQFTIVBFKLPCL-UHFFFAOYSA-L 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 229910052735 hafnium Inorganic materials 0.000 description 1
- VBJZVLUMGGDVMO-UHFFFAOYSA-N hafnium atom Chemical compound [Hf] VBJZVLUMGGDVMO-UHFFFAOYSA-N 0.000 description 1
- 238000007210 heterogeneous catalysis Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- QEFYFXOXNSNQGX-UHFFFAOYSA-N neodymium atom Chemical compound [Nd] QEFYFXOXNSNQGX-UHFFFAOYSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- -1 prase-dymium Chemical compound 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 229910052761 rare earth metal Inorganic materials 0.000 description 1
- 150000002910 rare earth metals Chemical class 0.000 description 1
- 230000007420 reactivation Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 229910052702 rhenium Inorganic materials 0.000 description 1
- WUAPFZMCVAUBPE-UHFFFAOYSA-N rhenium atom Chemical compound [Re] WUAPFZMCVAUBPE-UHFFFAOYSA-N 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 229930195734 saturated hydrocarbon Natural products 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 1
- 229910052721 tungsten Inorganic materials 0.000 description 1
- 239000010937 tungsten Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
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
- B01J8/0005—Catalytic processes under superatmospheric pressure
-
- 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
- B01J8/1836—Heating and cooling the reactor
-
- 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
- B01J8/224—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 the particles being subject to a circulatory movement
- B01J8/226—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 the particles being subject to a circulatory movement internally, i.e. the particles rotate within the vessel
-
- 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
- B01J8/224—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 the particles being subject to a circulatory movement
- B01J8/228—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 the particles being subject to a circulatory movement externally, i.e. the particles leaving the vessel and subsequently re-entering it
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
- B01J2208/00123—Fingers
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
- B01J2208/00132—Tubes
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
- B01J2208/0015—Plates; Cylinders
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00265—Part of all of the reactants being heated or cooled outside the reactor while recycling
- B01J2208/00283—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant liquids
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR9609552A FR2751564B1 (fr) | 1996-07-26 | 1996-07-26 | Procede et dispositif pour le fonctionnement d'une colonne a bulles triphasique avec application en synthese fischer-tropsch |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| NO973457D0 NO973457D0 (no) | 1997-07-25 |
| NO973457L NO973457L (no) | 1998-01-27 |
| NO317282B1 true NO317282B1 (no) | 2004-10-04 |
Family
ID=9494611
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| NO19973457A NO317282B1 (no) | 1996-07-26 | 1997-07-25 | Fremgangsmate for drift av en kolonne av trefasebobler under anvendelse av Fischer-Tropsch-syntesen |
Country Status (14)
| Country | Link |
|---|---|
| US (2) | US5961933A (ja) |
| EP (1) | EP0820806B1 (ja) |
| JP (1) | JP4517180B2 (ja) |
| CA (1) | CA2210850C (ja) |
| DZ (1) | DZ2278A1 (ja) |
| EG (1) | EG21201A (ja) |
| FR (1) | FR2751564B1 (ja) |
| ID (1) | ID18660A (ja) |
| MY (2) | MY116126A (ja) |
| NO (1) | NO317282B1 (ja) |
| RU (1) | RU2189857C2 (ja) |
| SA (1) | SA97180363B1 (ja) |
| TN (1) | TNSN97131A1 (ja) |
| ZA (1) | ZA976537B (ja) |
Families Citing this family (57)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| IT1292422B1 (it) * | 1997-06-26 | 1999-02-08 | Agip Petroli | Reattore a bolle con draft tube e procedimento per la rigenerazione del catalizzatore in esso contenuto |
| US6080301A (en) | 1998-09-04 | 2000-06-27 | Exxonmobil Research And Engineering Company | Premium synthetic lubricant base stock having at least 95% non-cyclic isoparaffins |
| US6475960B1 (en) | 1998-09-04 | 2002-11-05 | Exxonmobil Research And Engineering Co. | Premium synthetic lubricants |
| TW518609B (en) * | 2000-03-15 | 2003-01-21 | Hitachi Ltd | Chemical decontamination liquid decomposition device provided with catalyst tower and catalyst tower therefor |
| FR2806642B1 (fr) | 2000-03-27 | 2002-08-23 | Inst Francais Du Petrole | Procede de conversion d'hydrocarbures dans un reacteur triphasique |
| JP3864669B2 (ja) * | 2000-05-08 | 2007-01-10 | 三菱化学株式会社 | ヒドロホルミル化方法 |
| GB0023781D0 (en) * | 2000-09-28 | 2000-11-08 | Kvaerner Process Tech Ltd | Process |
| US20020137805A1 (en) * | 2001-01-26 | 2002-09-26 | Huang Jui-Hsin Ray | Process for operating a fischer-tropsch reactor |
| GB0112796D0 (en) * | 2001-05-25 | 2001-07-18 | Bp Exploration Operating | Process |
| AU2002310583A1 (en) * | 2001-05-25 | 2002-12-09 | Bp Exploration Operating Company Limited | Fischer-tropsch synthesis process |
| JP2004536173A (ja) * | 2001-05-25 | 2004-12-02 | ビーピー エクスプロレーション オペレーティング カンパニー リミテッド | フィッシャートロプシュ法 |
| GB0112789D0 (en) * | 2001-05-25 | 2001-07-18 | Bp Exploration Operating | Process |
| GB0112791D0 (en) * | 2001-05-25 | 2001-07-18 | Bp Exploration Operating | Process |
| GB0112806D0 (en) * | 2001-05-25 | 2001-07-18 | Bp Exploration Operating | Process |
| EP1414774A4 (en) * | 2001-07-25 | 2007-05-30 | Conoco Inc | OPTIMIZATION OF BUBBLE SUSPENSION FUEL REACTORS USING HIGH GAS RATE AND CONVERSION WITH SIMPLE MODERATE PASSAGE |
| US6914082B2 (en) | 2001-12-14 | 2005-07-05 | Conocophillips Company | Slurry bubble reactor operated in well-mixed gas flow regime |
| US6720358B2 (en) | 2001-12-28 | 2004-04-13 | Conocophillips Company | Water stripping and catalyst/liquid product separation system |
| US7001927B2 (en) * | 2001-12-28 | 2006-02-21 | Conocophillips Company | Water removal in Fischer-Tropsch processes |
| US6809122B2 (en) * | 2001-12-28 | 2004-10-26 | Conocophillips Company | Method for reducing the maximum water concentration in a multi-phase column reactor |
| US6956063B2 (en) | 2001-12-28 | 2005-10-18 | Conocophillips Company | Method for reducing water concentration in a multi-phase column reactor |
| GB0203182D0 (en) * | 2002-02-11 | 2002-03-27 | Davy Process Techn Ltd | Apparatus |
| US20040000474A1 (en) * | 2002-02-22 | 2004-01-01 | Catalytic Distillation Technologies | Liquid-continuous column distillation |
| US7232848B2 (en) * | 2002-09-09 | 2007-06-19 | Conocophillips Company | Gas agitated multiphase reactor with stationary catalyst solid phase |
| US6897246B2 (en) * | 2002-11-12 | 2005-05-24 | Conocophillips Company | Recycling light olefins in multistage Fischer Tropsch processes |
| US7230035B2 (en) * | 2002-12-30 | 2007-06-12 | Conocophillips Company | Catalysts for the conversion of methane to synthesis gas |
| US20040175663A1 (en) * | 2003-03-06 | 2004-09-09 | M. Shannon Melton | Method for combusting fuel in a fired heater |
| US7019038B2 (en) * | 2003-05-23 | 2006-03-28 | Conocophillips Company | Recycle of low boiling point products to a Fischer-Tropsch reactor |
| US7163963B2 (en) * | 2003-09-08 | 2007-01-16 | Conocophillips Company | Chemically and thermally stabilized alumina for Fischer-Tropsch catalysts |
| DE10354311B4 (de) * | 2003-11-20 | 2009-09-17 | Lurgi Gmbh | Reaktor zur kontinuierlichen Durchführung einer chemischen Mehrphasenreaktion |
| US7087653B2 (en) * | 2003-12-23 | 2006-08-08 | World Gtl, Inc. | Modification of a methanol plant for converting natural gas to liquid hydrocarbons |
| JP4731553B2 (ja) * | 2004-05-10 | 2011-07-27 | サソール テクノロジー（プロプライエタリー）リミテッド | 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 |
| JP2006073271A (ja) * | 2004-08-31 | 2006-03-16 | Tyco Electronics Amp Kk | 電気コネクタ |
| US20080167391A1 (en) * | 2004-12-31 | 2008-07-10 | Shell Oil Company | Reactor for Solid/Liquid/Gas Reactions |
| US8013025B2 (en) * | 2005-03-17 | 2011-09-06 | Sasol Technology (Proprietary) Limited | Method of operating a three-phase slurry reactor |
| NL2000030C2 (nl) * | 2005-03-17 | 2007-06-14 | Sasol Tech Pty Ltd | Werkwijze voor het bedienen van een gefluïdiseerd-bedreactor en gefluïdiseerd-bedreactor. |
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| US8969236B2 (en) | 2006-04-27 | 2015-03-03 | University Of Wyoming Research Corporation | Process and catalyst for production of mixed alcohols from synthesis gas |
| US7666366B2 (en) * | 2006-07-10 | 2010-02-23 | Exxonmobil Chemical Patents Inc. | Internal loop reactor and Oxo process using same |
| FR2910488B1 (fr) | 2006-12-20 | 2010-06-04 | Inst Francais Du Petrole | Procede de conversion de biomasse pour la production de gaz de synthese. |
| US20080260631A1 (en) | 2007-04-18 | 2008-10-23 | H2Gen Innovations, Inc. | Hydrogen production process |
| CN101396647B (zh) * | 2007-09-29 | 2011-03-16 | 中科合成油技术有限公司 | 用于费-托合成的气-液-固三相悬浮床反应器及其应用 |
| US8278363B2 (en) * | 2009-03-23 | 2012-10-02 | Thomas Charles Holcombe | Fischer-tropsch reactions using heat transfer tubes with a catalyst layer on the outside surfaces |
| WO2011109567A1 (en) | 2010-03-02 | 2011-09-09 | Thomas Yuschak | Welded, laminated apparatus, methods of making, and methods of using the apparatus |
| CN103285780B (zh) * | 2012-02-24 | 2015-07-08 | 北京低碳清洁能源研究所 | 一种浆态鼓泡床磁感反应器 |
| CA2866306A1 (en) * | 2012-03-03 | 2013-09-12 | Viceroy Chemical Inc. | Electrolytic cell including a three-phase interface to react carbon-based gases in an aqueous electrolyte |
| FR2991991B1 (fr) | 2012-06-18 | 2014-06-13 | IFP Energies Nouvelles | Procede de synthese d'hydrocarbures a partir de gaz de synthese avec controle de la temperature de la boucle externe |
| FR2998812B1 (fr) | 2012-12-05 | 2014-11-21 | IFP Energies Nouvelles | Injection d'additif dans une unite de synthese d'hydrocarbures a partir de gaz de synthese permettant de controler et maintenir une concentration homogene en catalyseur |
| JP2014136767A (ja) * | 2013-01-17 | 2014-07-28 | Japan Oil Gas & Metals National Corp | 炭化水素合成反応装置 |
| ES2548426B1 (es) * | 2014-04-15 | 2016-07-26 | Fundacion Imdea Agua | Proceso para el tratamiento de aguas procedentes de lodos bentoníticos |
| US10710043B2 (en) | 2014-09-24 | 2020-07-14 | Raven Sr, Llc | Compact and maintainable waste reformation apparatus |
| RU2637922C2 (ru) * | 2016-06-02 | 2017-12-08 | Публичное акционерное общество "Электрогорский институт нефтепереработки" (ПАО "ЭлИНП") | Способ алкилирования изобутана в трехфазном реакторе с неподвижным слоем катализатора |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2662091A (en) * | 1950-09-25 | 1953-12-08 | William W Odell | Process and means of promoting chemical reactions |
| JPS501700B1 (ja) * | 1969-06-21 | 1975-01-21 | ||
| BE759284A (fr) * | 1969-11-24 | 1971-05-24 | Shell Int Research | Procede et appareil pour la mise en contact d'un liquide avec des particules solides |
| US3901660A (en) * | 1970-10-29 | 1975-08-26 | Hoechst Ag | Apparatus for the continuous carrying out heterogeneous catalytic reaction in liquid phase |
| NL175790C (nl) * | 1977-03-01 | 1985-01-02 | Shell Int Research | Inrichting voor het scheiden van gas en vloeistof, alsmede slurriereactor voorzien van een dergelijke inrichting. |
| US4139352A (en) * | 1978-03-14 | 1979-02-13 | Shell Oil Company | Gas liquid separator |
| US4589927A (en) * | 1984-05-29 | 1986-05-20 | Battelle Development Corporation | Liquid multisolid fluidized bed processing |
| US5527473A (en) * | 1993-07-15 | 1996-06-18 | Ackerman; Carl D. | Process for performing reactions in a liquid-solid catalyst slurry |
-
1996
- 1996-07-26 FR FR9609552A patent/FR2751564B1/fr not_active Expired - Fee Related
-
1997
- 1997-07-08 EP EP97401637A patent/EP0820806B1/fr not_active Revoked
- 1997-07-23 DZ DZ970128A patent/DZ2278A1/fr active
- 1997-07-23 ZA ZA976537A patent/ZA976537B/xx unknown
- 1997-07-24 JP JP19836597A patent/JP4517180B2/ja not_active Expired - Fee Related
- 1997-07-24 TN TNTNSN97131A patent/TNSN97131A1/fr unknown
- 1997-07-24 ID IDP972575A patent/ID18660A/id unknown
- 1997-07-25 RU RU97113256/12A patent/RU2189857C2/ru not_active IP Right Cessation
- 1997-07-25 MY MYPI97003413A patent/MY116126A/en unknown
- 1997-07-25 MY MYPI20013402A patent/MY127602A/en unknown
- 1997-07-25 NO NO19973457A patent/NO317282B1/no not_active IP Right Cessation
- 1997-07-25 CA CA002210850A patent/CA2210850C/fr not_active Expired - Fee Related
- 1997-07-26 EG EG72897A patent/EG21201A/xx active
- 1997-07-28 US US08/901,521 patent/US5961933A/en not_active Expired - Lifetime
- 1997-09-02 SA SA97180363A patent/SA97180363B1/ar unknown
-
1999
- 1999-01-11 US US09/227,837 patent/US6060524A/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| EG21201A (en) | 2001-01-31 |
| EP0820806B1 (fr) | 2003-05-14 |
| US5961933A (en) | 1999-10-05 |
| EP0820806A1 (fr) | 1998-01-28 |
| SA97180363B1 (ar) | 2006-07-30 |
| TNSN97131A1 (fr) | 1999-12-31 |
| FR2751564A1 (fr) | 1998-01-30 |
| RU2189857C2 (ru) | 2002-09-27 |
| JP4517180B2 (ja) | 2010-08-04 |
| MY116126A (en) | 2003-11-28 |
| ZA976537B (en) | 1999-01-25 |
| MY127602A (en) | 2006-12-29 |
| CA2210850C (fr) | 2006-10-17 |
| JPH1066859A (ja) | 1998-03-10 |
| ID18660A (id) | 1998-04-30 |
| FR2751564B1 (fr) | 2001-10-12 |
| US6060524A (en) | 2000-05-09 |
| NO973457L (no) | 1998-01-27 |
| CA2210850A1 (fr) | 1998-01-26 |
| NO973457D0 (no) | 1997-07-25 |
| DZ2278A1 (fr) | 2002-12-18 |
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