NO319909B1 - Fremgangsmate for separering av vaeske fra slam og prosess for bearbeiding av tunge hydrokarboner. - Google Patents
Fremgangsmate for separering av vaeske fra slam og prosess for bearbeiding av tunge hydrokarboner. Download PDFInfo
- Publication number
- NO319909B1 NO319909B1 NO19983975A NO983975A NO319909B1 NO 319909 B1 NO319909 B1 NO 319909B1 NO 19983975 A NO19983975 A NO 19983975A NO 983975 A NO983975 A NO 983975A NO 319909 B1 NO319909 B1 NO 319909B1
- Authority
- NO
- Norway
- Prior art keywords
- sludge
- liquid
- filter
- vessel
- gas
- Prior art date
Links
- 239000010802 sludge Substances 0.000 title claims description 108
- 239000007788 liquid Substances 0.000 title claims description 47
- 238000000034 method Methods 0.000 title claims description 42
- 229930195733 hydrocarbon Natural products 0.000 title claims description 36
- 150000002430 hydrocarbons Chemical class 0.000 title claims description 36
- 239000002245 particle Substances 0.000 claims description 51
- 239000003054 catalyst Substances 0.000 claims description 47
- 238000003786 synthesis reaction Methods 0.000 claims description 22
- 230000015572 biosynthetic process Effects 0.000 claims description 20
- 239000007787 solid Substances 0.000 claims description 16
- 238000006243 chemical reaction Methods 0.000 claims description 11
- 238000007872 degassing Methods 0.000 claims description 9
- 238000001311 chemical methods and process Methods 0.000 claims description 6
- 239000011949 solid catalyst Substances 0.000 claims description 6
- 238000009434 installation Methods 0.000 claims description 4
- 239000000376 reactant Substances 0.000 claims description 4
- 239000002002 slurry Substances 0.000 claims description 3
- 238000011144 upstream manufacturing Methods 0.000 claims description 3
- 239000007789 gas Substances 0.000 description 25
- 238000000926 separation method Methods 0.000 description 18
- 239000012190 activator Substances 0.000 description 13
- 229910052751 metal Inorganic materials 0.000 description 13
- 239000002184 metal Substances 0.000 description 13
- 238000001914 filtration Methods 0.000 description 10
- 239000004215 Carbon black (E152) Substances 0.000 description 8
- 229910017052 cobalt Inorganic materials 0.000 description 8
- 239000010941 cobalt Substances 0.000 description 8
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 8
- 229910052739 hydrogen Inorganic materials 0.000 description 7
- 239000001257 hydrogen Substances 0.000 description 7
- 239000000047 product Substances 0.000 description 7
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 6
- 229910002091 carbon monoxide Inorganic materials 0.000 description 6
- 238000009295 crossflow filtration Methods 0.000 description 6
- 239000000725 suspension Substances 0.000 description 6
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 4
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 4
- 238000001816 cooling Methods 0.000 description 4
- 239000000706 filtrate Substances 0.000 description 4
- 229910052748 manganese Inorganic materials 0.000 description 4
- 239000011572 manganese Substances 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 229910052720 vanadium Inorganic materials 0.000 description 4
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 description 4
- 229910052726 zirconium Inorganic materials 0.000 description 4
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 3
- 239000012876 carrier material Substances 0.000 description 3
- 239000007795 chemical reaction product Substances 0.000 description 3
- 238000005520 cutting process Methods 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 206010016256 fatigue Diseases 0.000 description 3
- 238000007327 hydrogenolysis reaction Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 150000002739 metals Chemical class 0.000 description 3
- 230000000737 periodic effect Effects 0.000 description 3
- 229910052719 titanium Inorganic materials 0.000 description 3
- 239000010936 titanium Substances 0.000 description 3
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 230000004907 flux Effects 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000012263 liquid product Substances 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229910044991 metal oxide Inorganic materials 0.000 description 2
- 150000004706 metal oxides Chemical class 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 229920000098 polyolefin Polymers 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 1
- 229910052768 actinide Inorganic materials 0.000 description 1
- 150000001255 actinides Chemical class 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- -1 aromatic urethanes Chemical class 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012065 filter cake Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000022244 formylation Effects 0.000 description 1
- 238000006170 formylation reaction Methods 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 229910052747 lanthanoid Inorganic materials 0.000 description 1
- 150000002602 lanthanoids Chemical class 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000006213 oxygenation reaction Methods 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 239000012465 retentate Substances 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
- 229910052707 ruthenium Inorganic materials 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
-
- 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
- C10G53/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more refining processes
- C10G53/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more refining processes plural serial stages only
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/0068—General arrangements, e.g. flowsheets
-
- 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
-
- 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
- B01J8/005—Separating solid material from the gas/liquid stream
- B01J8/0055—Separating solid material from the gas/liquid stream using cyclones
-
- 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
- B01J8/005—Separating solid material from the gas/liquid stream
- B01J8/006—Separating solid material from the gas/liquid stream by filtration
-
- 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
-
- 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
- C10G31/00—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for
- C10G31/09—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for by filtration
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Combustion & Propulsion (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)
- Catalysts (AREA)
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP96200532 | 1996-02-29 | ||
| PCT/EP1997/001002 WO1997031693A1 (en) | 1996-02-29 | 1997-02-27 | Method for separating liquid from a slurry and process for the preparation of hydrocarbons |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| NO983975D0 NO983975D0 (no) | 1998-08-28 |
| NO983975L NO983975L (no) | 1998-10-28 |
| NO319909B1 true NO319909B1 (no) | 2005-09-26 |
Family
ID=8223733
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| NO19983975A NO319909B1 (no) | 1996-02-29 | 1998-08-28 | Fremgangsmate for separering av vaeske fra slam og prosess for bearbeiding av tunge hydrokarboner. |
Country Status (21)
| Country | Link |
|---|---|
| US (1) | US5900159A (da) |
| EP (1) | EP0956126B1 (da) |
| JP (1) | JP2000506061A (da) |
| KR (1) | KR19990082121A (da) |
| CN (1) | CN1104925C (da) |
| AU (1) | AU713933B2 (da) |
| BR (1) | BR9707717A (da) |
| CA (1) | CA2242779C (da) |
| DE (1) | DE69712521T2 (da) |
| DK (1) | DK0956126T3 (da) |
| DZ (1) | DZ2185A1 (da) |
| EA (1) | EA001233B1 (da) |
| ES (1) | ES2176696T3 (da) |
| ID (1) | ID16054A (da) |
| MY (1) | MY118981A (da) |
| NO (1) | NO319909B1 (da) |
| NZ (1) | NZ332055A (da) |
| PE (1) | PE46498A1 (da) |
| SA (1) | SA97170707B1 (da) |
| WO (1) | WO1997031693A1 (da) |
| ZA (1) | ZA971644B (da) |
Families Citing this family (62)
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| EP0996491B1 (en) * | 1997-06-06 | 2005-10-12 | Texaco Development Corporation | Process and apparatus for treating black water from syngas scrubbers by vacuum flash and for recovering vapour |
| ITMI980865A1 (it) * | 1998-04-23 | 1999-10-23 | Eniricerche S P A Ora Enitecno | Procedimento per la preparazione di idrocarburi da gas di sintesi |
| US6365544B2 (en) * | 1998-05-22 | 2002-04-02 | Conoco Inc. | Fischer-Tropsch processes and catalysts using fluorided alumina supports |
| US6368997B2 (en) * | 1998-05-22 | 2002-04-09 | Conoco Inc. | Fischer-Tropsch processes and catalysts using fluorided supports |
| FR2802832B1 (fr) * | 1999-12-22 | 2002-01-18 | Inst Francais Du Petrole | Installation et procede de production d'hydrocarbures par synthese fischer-tropsch dans un reacteur comportant sur la boucle de recirculation des moyens de limitation de l'attrition du solide |
| FR2802828B1 (fr) * | 1999-12-22 | 2002-05-03 | Inst Francais Du Petrole | Dispositif et procede de separation de produits liquides a partir d'une suspension issue d'un reacteur fischer-tropsch et en presence d'un diluant |
| FR2802831B1 (fr) * | 1999-12-22 | 2002-02-08 | Inst Francais Du Petrole | Installation et procede de conversion chimique dans un reacteur triphasique comportant sur la boucle de recirculation des moyens de limitation de l'attrition du solide |
| FR2802827B1 (fr) * | 1999-12-22 | 2002-05-10 | Inst Francais Du Petrole | Dispositif et procede de separation de produits liquides a partir d'une suspension contenant un solide et en presence d'un diluant |
| GB0023781D0 (en) * | 2000-09-28 | 2000-11-08 | Kvaerner Process Tech Ltd | Process |
| EP1328607A2 (en) * | 2000-10-13 | 2003-07-23 | Bp Exploration Operating Company Limited | Fischer-tropsch synthesis process |
| US6359018B1 (en) | 2000-10-27 | 2002-03-19 | Chevron U.S.A. Inc | Process for upflow fixed-bed hydroprocessing of fischer-tropsch wax |
| FR2826294B1 (fr) * | 2001-06-25 | 2003-09-26 | Inst Francais Du Petrole | Dispositif et procede optimisant la circulation d'une suspension dans une installation comprenant un reacteur fischer-tropsch |
| FR2826295B1 (fr) * | 2001-06-25 | 2003-09-26 | Inst Francais Du Petrole | Dispositif et procede optimisant la circulation d'une suspension dans une installation comprenant un reacteur triphasique |
| US6762209B1 (en) | 2001-08-31 | 2004-07-13 | University Of Kentucky Research Foundation | Bubble column apparatus for separating wax from catalyst slurry |
| EP1447133B1 (en) * | 2001-10-24 | 2012-04-04 | Daikin Industries, Ltd. | Method for the recovery of catalysts in a process for the production of perfluoroalkyl iodide telomers |
| US6720358B2 (en) | 2001-12-28 | 2004-04-13 | Conocophillips Company | Water stripping and catalyst/liquid product separation system |
| US6809122B2 (en) * | 2001-12-28 | 2004-10-26 | Conocophillips Company | Method for reducing the maximum water concentration in a multi-phase column reactor |
| US7001927B2 (en) * | 2001-12-28 | 2006-02-21 | Conocophillips Company | Water removal in Fischer-Tropsch processes |
| US6956063B2 (en) * | 2001-12-28 | 2005-10-18 | Conocophillips Company | Method for reducing water concentration in a multi-phase column reactor |
| CA2482057A1 (en) * | 2002-04-16 | 2003-10-30 | Conocophillips Company | Solid/liquid separation system for multiphase converters |
| US6866779B1 (en) | 2002-07-22 | 2005-03-15 | Western Environmental Engineering Company | Nitrogen recovery system and method |
| US7153427B2 (en) * | 2002-07-22 | 2006-12-26 | Environmental Energy & Engineering Co. | Nitrogen recovery system and method using heated air as stripping gas |
| US6833078B2 (en) * | 2002-09-13 | 2004-12-21 | Conocophillips Company | Solid-liquid separation system |
| ITMI20030969A1 (it) * | 2003-05-15 | 2004-11-16 | Enitecnologie Spa | Procedimento per la produzione in continuo di idrocarburi da gas di sintesi in reattori a sospensione e per la separazione della fase liquida prodotta dalla fase solida. |
| ITMI20031029A1 (it) * | 2003-05-22 | 2004-11-23 | Enitecnologie Spa | Procedimenti per la produzione in continuo di idrocarburi da gas di sintesi. |
| US7488601B2 (en) | 2003-06-20 | 2009-02-10 | Roche Diagnostic Operations, Inc. | System and method for determining an abused sensor during analyte measurement |
| ITMI20031288A1 (it) * | 2003-06-25 | 2004-12-26 | Enitecnologie Spa | Processo per la produzione in continuo di idrocarburi da gas di sintesi in reattori a sospensione e per la separazione della fase liquida prodotta dalla fase solida. |
| US7150823B2 (en) * | 2003-07-02 | 2006-12-19 | Chevron U.S.A. Inc. | Catalytic filtering of a Fischer-Tropsch derived hydrocarbon stream |
| US20050004412A1 (en) * | 2003-07-02 | 2005-01-06 | Chevron U.S.A. Inc, | Distillation of a Fischer-Tropsch derived hydrocarbon stream |
| RU2341323C2 (ru) * | 2003-07-03 | 2008-12-20 | Шелл Интернэшнл Рисерч Маатсхаппий Б.В. | Способ отделения твердой фазы от потока газа, содержащего твердую фазу |
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| US9834730B2 (en) | 2014-01-23 | 2017-12-05 | Ecolab Usa Inc. | Use of emulsion polymers to flocculate solids in organic liquids |
| CN105194910B (zh) * | 2015-10-26 | 2017-08-15 | 杭州鼎流科技有限公司 | 一种液体脱气输送系统 |
| US11607634B2 (en) * | 2018-05-25 | 2023-03-21 | Sustainable Energy Solutions, Inc. | Method for concentrating solids and removing solids from a filter medium |
Family Cites Families (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3245318C3 (de) * | 1982-12-08 | 1996-06-20 | Bayer Ag | Verfahren zur Durchführung von Druckreaktionen mit suspendierten Katalysatoren |
| CH667373A5 (de) * | 1985-05-22 | 1988-10-14 | Bucher Guyer Ag Masch | Verfahren zur klaerung von fluessigkeiten und anlage zur durchfuehrung desselben. |
| FR2586439B1 (fr) * | 1985-08-22 | 1987-10-23 | Cegedur | Dispositif d'assemblage et de fixation de panneaux rectangulaires |
| IL79985A0 (en) * | 1985-09-13 | 1986-12-31 | Ausimont Spa | Purification of oils containing solid matter in suspension |
| JPH01148318A (ja) * | 1987-12-04 | 1989-06-09 | Toshiba Ceramics Co Ltd | 固液分離装置 |
| JPH01296972A (ja) * | 1988-05-25 | 1989-11-30 | Ngk Insulators Ltd | 膜型反応装置 |
| US5035799A (en) * | 1989-08-21 | 1991-07-30 | Clear Flow, Inc. | Filter assembly |
| JP3018449B2 (ja) * | 1990-09-21 | 2000-03-13 | 味の素株式会社 | アミノ酸の発酵方法およびその装置 |
| BR9102288A (pt) * | 1991-05-28 | 1993-01-05 | Brasileira S A Embraco Empresa | Conjunto abafador de succao para compressor hermetico |
| JPH07143873A (ja) * | 1993-11-24 | 1995-06-06 | Miura Co Ltd | 酒造用濾過装置 |
-
1997
- 1997-02-25 US US08/806,879 patent/US5900159A/en not_active Expired - Lifetime
- 1997-02-26 DZ DZ970031A patent/DZ2185A1/fr active
- 1997-02-26 PE PE1997000138A patent/PE46498A1/es not_active Application Discontinuation
- 1997-02-26 ZA ZA9701644A patent/ZA971644B/xx unknown
- 1997-02-27 DE DE69712521T patent/DE69712521T2/de not_active Expired - Fee Related
- 1997-02-27 WO PCT/EP1997/001002 patent/WO1997031693A1/en not_active Application Discontinuation
- 1997-02-27 KR KR1019980705843A patent/KR19990082121A/ko not_active Application Discontinuation
- 1997-02-27 NZ NZ332055A patent/NZ332055A/xx unknown
- 1997-02-27 EP EP97907056A patent/EP0956126B1/en not_active Expired - Lifetime
- 1997-02-27 CN CN97192638A patent/CN1104925C/zh not_active Expired - Fee Related
- 1997-02-27 BR BR9707717A patent/BR9707717A/pt active Search and Examination
- 1997-02-27 AU AU19246/97A patent/AU713933B2/en not_active Ceased
- 1997-02-27 EA EA199800777A patent/EA001233B1/ru not_active IP Right Cessation
- 1997-02-27 CA CA002242779A patent/CA2242779C/en not_active Expired - Fee Related
- 1997-02-27 JP JP9530627A patent/JP2000506061A/ja not_active Ceased
- 1997-02-27 ID IDP970582A patent/ID16054A/id unknown
- 1997-02-27 DK DK97907056T patent/DK0956126T3/da active
- 1997-02-27 MY MYPI97000754A patent/MY118981A/en unknown
- 1997-02-27 ES ES97907056T patent/ES2176696T3/es not_active Expired - Lifetime
- 1997-03-11 SA SA97170707A patent/SA97170707B1/ar unknown
-
1998
- 1998-08-28 NO NO19983975A patent/NO319909B1/no not_active IP Right Cessation
Also Published As
| Publication number | Publication date |
|---|---|
| NO983975D0 (no) | 1998-08-28 |
| ES2176696T3 (es) | 2002-12-01 |
| MY118981A (en) | 2005-02-28 |
| CN1104925C (zh) | 2003-04-09 |
| CA2242779C (en) | 2005-05-10 |
| ZA971644B (en) | 1997-08-29 |
| EA199800777A1 (ru) | 1999-02-25 |
| SA97170707B1 (ar) | 2006-03-25 |
| BR9707717A (pt) | 1999-04-06 |
| CA2242779A1 (en) | 1997-09-04 |
| JP2000506061A (ja) | 2000-05-23 |
| EP0956126A1 (en) | 1999-11-17 |
| DZ2185A1 (fr) | 2002-12-02 |
| PE46498A1 (es) | 1998-08-26 |
| KR19990082121A (ko) | 1999-11-15 |
| NZ332055A (en) | 1999-03-29 |
| DE69712521D1 (de) | 2002-06-13 |
| US5900159A (en) | 1999-05-04 |
| CN1212635A (zh) | 1999-03-31 |
| EA001233B1 (ru) | 2000-12-25 |
| WO1997031693A1 (en) | 1997-09-04 |
| AU713933B2 (en) | 1999-12-16 |
| AU1924697A (en) | 1997-09-16 |
| DE69712521T2 (de) | 2002-09-12 |
| ID16054A (id) | 1997-08-28 |
| NO983975L (no) | 1998-10-28 |
| EP0956126B1 (en) | 2002-05-08 |
| DK0956126T3 (da) | 2002-09-02 |
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| MM1K | Lapsed by not paying the annual fees |