WO1998030322A1 - Fluid mixer and process using the same - Google Patents
Fluid mixer and process using the same Download PDFInfo
- Publication number
- WO1998030322A1 WO1998030322A1 PCT/EP1998/000141 EP9800141W WO9830322A1 WO 1998030322 A1 WO1998030322 A1 WO 1998030322A1 EP 9800141 W EP9800141 W EP 9800141W WO 9830322 A1 WO9830322 A1 WO 9830322A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- expander
- sectional area
- downstream
- upstream
- cross
- 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.)
- Ceased
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen; Reversible storage of hydrogen
- C01B3/02—Production of hydrogen; Production of gaseous mixtures containing hydrogen
- C01B3/32—Production of hydrogen; Production of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide or air
- C01B3/34—Production of hydrogen; Production of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide or air by reaction of hydrocarbons with gasifying agents
- C01B3/38—Production of hydrogen; Production of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide or air by reaction of hydrocarbons with gasifying agents using catalysts
- C01B3/386—Catalytic partial combustion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
-
- 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
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/0278—Feeding reactive fluids
-
- 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
- B01J2208/00504—Controlling the temperature by means of a burner
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/02—Processes for making hydrogen or synthesis gas
- C01B2203/025—Processes for making hydrogen or synthesis gas containing a partial oxidation step
- C01B2203/0261—Processes for making hydrogen or synthesis gas containing a partial oxidation step containing a catalytic partial oxidation step [CPO]
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/06—Integration with other chemical processes
- C01B2203/061—Methanol production
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/06—Integration with other chemical processes
- C01B2203/062—Hydrocarbon production, e.g. Fischer-Tropsch process
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/10—Catalysts for performing the hydrogen forming reactions
- C01B2203/1005—Arrangement or shape of catalyst
- C01B2203/1029—Catalysts in the form of a foam
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/10—Catalysts for performing the hydrogen forming reactions
- C01B2203/1041—Composition of the catalyst
- C01B2203/1047—Group VIII metal catalysts
- C01B2203/1064—Platinum group metal catalysts
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/10—Catalysts for performing the hydrogen forming reactions
- C01B2203/1041—Composition of the catalyst
- C01B2203/1082—Composition of support materials
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/12—Feeding the process for making hydrogen or synthesis gas
- C01B2203/1205—Composition of the feed
- C01B2203/1211—Organic compounds or organic mixtures used in the process for making hydrogen or synthesis gas
- C01B2203/1235—Hydrocarbons
- C01B2203/1241—Natural gas or methane
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/12—Feeding the process for making hydrogen or synthesis gas
- C01B2203/1276—Mixing of different feed components
Definitions
- the apparatus of the invention enables the mixing and diffusion of fluids by initial expansion of fluid stream in terms of greatest cross-sectional dimension (i.e. by increasing the internal cross-sectional area) without significant increase, i.e. up to 5 times, especially up to 3 times, preferably up to 2 times, of fluid-stream cross-sectional area (i.e. available cross-sectional area), and by subsequent divergence of fluid-stream cross-sectional area in manner to meet the hereinbefore mentioned obj ectives .
- References herein to cross-sectional area of stream or apparatus is to the area of the cross-section taken through a plane perpendicular to the stream or apparatus longitudinal axis.
- the carbon monoxide and hydrogen produced by the process of this invention may be used in any process employing either one or both of these compounds.
- the mixture of carbon monoxide and hydrogen prepared by the process is particularly suitable for use m the synthesis of hydrocarbons, for example by means of the Fischer- Tropsch process, or for the synthesis of oxygenates, for example methanol. Processes for the conversion of carbon monoxide and hydrogen into such products are well known in the art.
- the gaseous fluids enter the apparatus (1) and are mixed.
- the mixed fluids enter the expander (5) at its upstream end and are equally divided about axially mounted insert (6) .
- the annular mixed fluid stream merges by radial inward re-entry about the convex surface of insert (6) .
- the diffuser (7) is suitably profiled to provide radial inward momentum component to the mixed fluid stream for the avoidance of flow separation (for example from the wall) .
- the diffused mixed fluid stream passes through porous shield (8) and advances for a sufficient distance for the desired conditioning of feed prior to contacting catalyst (12) .
- the fluids comprising oxygen and natural gas are pre-heated prior to entering the apparatus (1) .
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- General Health & Medical Sciences (AREA)
- Health & Medical Sciences (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Feeding And Controlling Fuel (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Hydrogen, Water And Hydrids (AREA)
- Detergent Compositions (AREA)
Priority Applications (8)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AU60935/98A AU720655B2 (en) | 1997-01-07 | 1998-01-06 | Fluid mixer and process using the same |
| NZ336399A NZ336399A (en) | 1997-01-07 | 1998-01-06 | Fluid mixer for mixing reactive fluids at elevated temperatures and pressures having an expander with an insert and process using the same |
| DE69812585T DE69812585T2 (de) | 1997-01-07 | 1998-01-06 | Fluidmischer und verfahren für seine verwendung |
| CA002276464A CA2276464C (en) | 1997-01-07 | 1998-01-06 | Fluid mixer and process using the same |
| PL98334445A PL334445A1 (en) | 1997-01-07 | 1998-01-06 | Apparatus for and method of agitating fluids |
| EP98905287A EP0951345B1 (en) | 1997-01-07 | 1998-01-06 | Fluid mixer and process using the same |
| JP53056498A JP4156036B2 (ja) | 1997-01-07 | 1998-01-06 | 流体ミキサー及びそれを用いる方法 |
| NO993339A NO993339L (no) | 1997-01-07 | 1999-07-06 | Fluidblander og tilhörende prosess |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP97200033.5 | 1997-01-07 | ||
| EP97200033 | 1997-01-07 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO1998030322A1 true WO1998030322A1 (en) | 1998-07-16 |
Family
ID=8227915
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/EP1998/000141 Ceased WO1998030322A1 (en) | 1997-01-07 | 1998-01-06 | Fluid mixer and process using the same |
Country Status (12)
| Country | Link |
|---|---|
| US (1) | US6092921A (https=) |
| EP (1) | EP0951345B1 (https=) |
| JP (1) | JP4156036B2 (https=) |
| KR (1) | KR20000069909A (https=) |
| AU (1) | AU720655B2 (https=) |
| CA (1) | CA2276464C (https=) |
| DE (1) | DE69812585T2 (https=) |
| ID (1) | ID21814A (https=) |
| NO (1) | NO993339L (https=) |
| NZ (1) | NZ336399A (https=) |
| PL (1) | PL334445A1 (https=) |
| WO (1) | WO1998030322A1 (https=) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1043271A1 (en) * | 1999-03-30 | 2000-10-11 | Shell Internationale Researchmaatschappij B.V. | Apparatus for the catalytic partial oxidation of hydrocarbons |
| WO2001018451A1 (en) * | 1999-09-06 | 2001-03-15 | Shell Internationale Research Maatschappij B.V. | Mixing device |
| JP2004505754A (ja) * | 2000-08-08 | 2004-02-26 | シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ | 流れ分配器 |
| US7108838B2 (en) | 2003-10-30 | 2006-09-19 | Conocophillips Company | Feed mixer for a partial oxidation reactor |
| US7416571B2 (en) | 2005-03-09 | 2008-08-26 | Conocophillips Company | Compact mixer for the mixing of gaseous hydrocarbon and gaseous oxidants |
| WO2018007912A3 (en) * | 2016-07-07 | 2018-04-12 | Nova Chemicals (International) S.A. | Inherently safe oxygen/hydrocarbon gas mixer |
| CN111964052A (zh) * | 2019-05-19 | 2020-11-20 | 宁波方太厨具有限公司 | 一种用于燃气灶的引射管 |
Families Citing this family (34)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7654728B2 (en) | 1997-10-24 | 2010-02-02 | Revalesio Corporation | System and method for therapeutic application of dissolved oxygen |
| US7128278B2 (en) | 1997-10-24 | 2006-10-31 | Microdiffusion, Inc. | System and method for irritating with aerated water |
| US6702949B2 (en) | 1997-10-24 | 2004-03-09 | Microdiffusion, Inc. | Diffuser/emulsifier for aquaculture applications |
| US6386751B1 (en) | 1997-10-24 | 2002-05-14 | Diffusion Dynamics, Inc. | Diffuser/emulsifier |
| EP0953842A1 (de) * | 1998-05-01 | 1999-11-03 | F. Hoffmann-La Roche Ag | Analysenautomat mit an der Unterseite verjüngter Mischkammer und mit dieser dichtend verbundener Sockeleinheit |
| DE10049327A1 (de) * | 2000-10-05 | 2002-04-18 | Honeywell Specialty Chemicals | Verfahren und Vorrichtung zur Herstellung von Nickelsulfamat |
| US20070080189A1 (en) * | 2001-06-21 | 2007-04-12 | Jozef Smit Jacobus A | Catalytic reactor |
| US6514316B1 (en) | 2001-08-22 | 2003-02-04 | Mt Systems, Llc | System for improving the maximum operating temperature and lifetime of chromatographic columns |
| US7357820B2 (en) * | 2001-09-05 | 2008-04-15 | Webasto Ag | System for converting fuel and air into reformate |
| DE10219747B4 (de) * | 2002-05-02 | 2005-06-23 | Daimlerchrysler Ag | Verfahren zur Vermeidung einer Rückzündung in einem einen Reaktionsraum anströmenden Gemisch und Reaktor zur Durchführung des Verfahrens |
| US6783749B2 (en) * | 2002-05-13 | 2004-08-31 | The Boc Group, Inc. | Gas recovery process |
| US7255848B2 (en) * | 2002-10-01 | 2007-08-14 | Regents Of The Univeristy Of Minnesota | Production of hydrogen from alcohols |
| US7262334B2 (en) * | 2002-11-13 | 2007-08-28 | Regents Of The University Of Minnesota | Catalytic partial oxidation of hydrocarbons |
| US20040133057A1 (en) * | 2003-01-02 | 2004-07-08 | Conocophillips Company | Gaseous hydrocarbon-oxygen bubble tank mixer |
| US7683232B2 (en) | 2004-05-25 | 2010-03-23 | Regents Of The University Of Minnesota | Production of olefins having a functional group |
| DE602007008896D1 (de) * | 2006-07-03 | 2010-10-14 | Hardi Int As | Vorrichtung zum lösen von festen teilchen und flüssigen substanzen in einer flüssigkeit |
| US8784898B2 (en) | 2006-10-25 | 2014-07-22 | Revalesio Corporation | Methods of wound care and treatment |
| US8445546B2 (en) | 2006-10-25 | 2013-05-21 | Revalesio Corporation | Electrokinetically-altered fluids comprising charge-stabilized gas-containing nanostructures |
| US8609148B2 (en) | 2006-10-25 | 2013-12-17 | Revalesio Corporation | Methods of therapeutic treatment of eyes |
| AU2007308838B2 (en) | 2006-10-25 | 2014-03-13 | Revalesio Corporation | Mixing device and output fluids of same |
| US8597689B2 (en) | 2006-10-25 | 2013-12-03 | Revalesio Corporation | Methods of wound care and treatment |
| US8784897B2 (en) | 2006-10-25 | 2014-07-22 | Revalesio Corporation | Methods of therapeutic treatment of eyes |
| JP5491185B2 (ja) | 2006-10-25 | 2014-05-14 | リバルシオ コーポレイション | 傷のケアおよび処置の方法 |
| WO2008052361A1 (en) * | 2006-11-03 | 2008-05-08 | Nxtgen Emission Controls Inc. | Fuel processor |
| DE602007009175D1 (de) * | 2006-12-09 | 2010-10-28 | Haldor Topsoe As | Verfahren und Vorrichtung zum Mischen zweier oder mehrerer Fluidströme |
| US9523090B2 (en) | 2007-10-25 | 2016-12-20 | Revalesio Corporation | Compositions and methods for treating inflammation |
| US9745567B2 (en) | 2008-04-28 | 2017-08-29 | Revalesio Corporation | Compositions and methods for treating multiple sclerosis |
| US10125359B2 (en) | 2007-10-25 | 2018-11-13 | Revalesio Corporation | Compositions and methods for treating inflammation |
| US8980325B2 (en) | 2008-05-01 | 2015-03-17 | Revalesio Corporation | Compositions and methods for treating digestive disorders |
| US8815292B2 (en) | 2009-04-27 | 2014-08-26 | Revalesio Corporation | Compositions and methods for treating insulin resistance and diabetes mellitus |
| BR112012028540A2 (pt) | 2010-05-07 | 2016-07-26 | Revalesio Corp | composições e métodos para melhorar desempenho fisiológico e tempo de recuperação |
| JP2013533320A (ja) | 2010-08-12 | 2013-08-22 | レバレジオ コーポレイション | タウオパチーを治療するための組成物および方法 |
| FR3008626B1 (fr) * | 2013-07-19 | 2015-08-07 | Arkema France | Reacteur pour preparer du cyanure d'hydrogene par le procede d'andrussow, equipement comprenant ledit reacteur et procede utilisant un tel equipement |
| JP6291903B2 (ja) * | 2014-02-26 | 2018-03-14 | 株式会社ジェイテクト | 混練装置 |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2115978A1 (de) * | 1970-04-03 | 1971-10-21 | Shell Int Research | Mischvorrichtung fur Gase |
| DE2203648A1 (de) * | 1971-01-28 | 1972-08-10 | Shell Int Research | Mischvorrichtung für Gase |
| EP0254395A2 (en) * | 1986-05-27 | 1988-01-27 | Imperial Chemical Industries Plc | Method of starting a process for the production of a gas stream containing hydrogen and carbon oxides |
| US5112527A (en) * | 1991-04-02 | 1992-05-12 | Amoco Corporation | Process for converting natural gas to synthesis gas |
| EP0656317A1 (en) * | 1993-11-29 | 1995-06-07 | Shell Internationale Researchmaatschappij B.V. | Process for the catalytic partial oxidation of hydrocarbons |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2021092A (en) * | 1931-02-09 | 1935-11-12 | Teliet Jean Antoine Marcel | Improved method and means for incorporating a fluid to a stream of a fluid or of a pulverulent solid |
| US3020234A (en) * | 1959-10-06 | 1962-02-06 | Union Carbide Corp | Method and apparatus for producing a homogeneous thermal insulation mixture |
| DE1258835B (de) * | 1964-08-28 | 1968-01-18 | James R Lage Dr | Mischeinrichtung |
| US4008580A (en) * | 1974-12-04 | 1977-02-22 | Frigoscandia Contracting, Inc. | Initial quick freeze pan for direct refrigerant contact cooler |
| US4299655A (en) * | 1978-03-13 | 1981-11-10 | Beloit Corporation | Foam generator for papermaking machine |
| JPS60137425A (ja) * | 1983-12-26 | 1985-07-22 | Hitachi Ltd | 流体混合装置 |
-
1998
- 1998-01-06 ID IDW990651A patent/ID21814A/id unknown
- 1998-01-06 JP JP53056498A patent/JP4156036B2/ja not_active Expired - Fee Related
- 1998-01-06 AU AU60935/98A patent/AU720655B2/en not_active Ceased
- 1998-01-06 EP EP98905287A patent/EP0951345B1/en not_active Expired - Lifetime
- 1998-01-06 NZ NZ336399A patent/NZ336399A/xx unknown
- 1998-01-06 DE DE69812585T patent/DE69812585T2/de not_active Expired - Fee Related
- 1998-01-06 WO PCT/EP1998/000141 patent/WO1998030322A1/en not_active Ceased
- 1998-01-06 PL PL98334445A patent/PL334445A1/xx unknown
- 1998-01-06 KR KR1019997006121A patent/KR20000069909A/ko not_active Withdrawn
- 1998-01-06 CA CA002276464A patent/CA2276464C/en not_active Expired - Fee Related
- 1998-01-07 US US09/004,072 patent/US6092921A/en not_active Expired - Fee Related
-
1999
- 1999-07-06 NO NO993339A patent/NO993339L/no not_active Application Discontinuation
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2115978A1 (de) * | 1970-04-03 | 1971-10-21 | Shell Int Research | Mischvorrichtung fur Gase |
| DE2203648A1 (de) * | 1971-01-28 | 1972-08-10 | Shell Int Research | Mischvorrichtung für Gase |
| EP0254395A2 (en) * | 1986-05-27 | 1988-01-27 | Imperial Chemical Industries Plc | Method of starting a process for the production of a gas stream containing hydrogen and carbon oxides |
| US5112527A (en) * | 1991-04-02 | 1992-05-12 | Amoco Corporation | Process for converting natural gas to synthesis gas |
| EP0656317A1 (en) * | 1993-11-29 | 1995-06-07 | Shell Internationale Researchmaatschappij B.V. | Process for the catalytic partial oxidation of hydrocarbons |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1043271A1 (en) * | 1999-03-30 | 2000-10-11 | Shell Internationale Researchmaatschappij B.V. | Apparatus for the catalytic partial oxidation of hydrocarbons |
| WO2001018451A1 (en) * | 1999-09-06 | 2001-03-15 | Shell Internationale Research Maatschappij B.V. | Mixing device |
| US7018435B1 (en) | 1999-09-06 | 2006-03-28 | Shell Oil Company | Mixing device |
| JP2004505754A (ja) * | 2000-08-08 | 2004-02-26 | シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ | 流れ分配器 |
| US7018436B2 (en) | 2000-08-08 | 2006-03-28 | Shell Oil Company | Catalytic reactor with tangential flow distribution |
| US7108838B2 (en) | 2003-10-30 | 2006-09-19 | Conocophillips Company | Feed mixer for a partial oxidation reactor |
| US7416571B2 (en) | 2005-03-09 | 2008-08-26 | Conocophillips Company | Compact mixer for the mixing of gaseous hydrocarbon and gaseous oxidants |
| WO2018007912A3 (en) * | 2016-07-07 | 2018-04-12 | Nova Chemicals (International) S.A. | Inherently safe oxygen/hydrocarbon gas mixer |
| CN111964052A (zh) * | 2019-05-19 | 2020-11-20 | 宁波方太厨具有限公司 | 一种用于燃气灶的引射管 |
| CN111964052B (zh) * | 2019-05-19 | 2021-11-26 | 宁波方太厨具有限公司 | 一种用于燃气灶的引射管 |
Also Published As
| Publication number | Publication date |
|---|---|
| US6092921A (en) | 2000-07-25 |
| NO993339D0 (no) | 1999-07-06 |
| AU6093598A (en) | 1998-08-03 |
| NZ336399A (en) | 2000-03-27 |
| AU720655B2 (en) | 2000-06-08 |
| DE69812585D1 (de) | 2003-04-30 |
| JP2001506183A (ja) | 2001-05-15 |
| KR20000069909A (ko) | 2000-11-25 |
| CA2276464A1 (en) | 1998-07-16 |
| EP0951345A1 (en) | 1999-10-27 |
| JP4156036B2 (ja) | 2008-09-24 |
| EP0951345B1 (en) | 2003-03-26 |
| PL334445A1 (en) | 2000-02-28 |
| NO993339L (no) | 1999-09-02 |
| CA2276464C (en) | 2007-05-08 |
| ID21814A (id) | 1999-07-29 |
| DE69812585T2 (de) | 2004-01-08 |
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Legal Events
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| AK | Designated states |
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