EP1125626A1 - Mélangeur statique - Google Patents

Mélangeur statique Download PDF

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Publication number
EP1125626A1
EP1125626A1 EP01810047A EP01810047A EP1125626A1 EP 1125626 A1 EP1125626 A1 EP 1125626A1 EP 01810047 A EP01810047 A EP 01810047A EP 01810047 A EP01810047 A EP 01810047A EP 1125626 A1 EP1125626 A1 EP 1125626A1
Authority
EP
European Patent Office
Prior art keywords
chambers
mixer
static mixer
mixing
basic structure
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.)
Granted
Application number
EP01810047A
Other languages
German (de)
English (en)
Other versions
EP1125626B1 (fr
Inventor
Rolf Heusser
Markus Fleischli
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sulzer Chemtech AG
Original Assignee
Sulzer Chemtech AG
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Sulzer Chemtech AG filed Critical Sulzer Chemtech AG
Priority to EP01810047A priority Critical patent/EP1125626B1/fr
Publication of EP1125626A1 publication Critical patent/EP1125626A1/fr
Application granted granted Critical
Publication of EP1125626B1 publication Critical patent/EP1125626B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/40Mixing liquids with liquids; Emulsifying
    • B01F23/47Mixing liquids with liquids; Emulsifying involving high-viscosity liquids, e.g. asphalt
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40Static mixers
    • B01F25/42Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/432Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction with means for dividing the material flow into separate sub-flows and for repositioning and recombining these sub-flows; Cross-mixing, e.g. conducting the outer layer of the material nearer to the axis of the tube or vice-versa
    • B01F25/4321Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction with means for dividing the material flow into separate sub-flows and for repositioning and recombining these sub-flows; Cross-mixing, e.g. conducting the outer layer of the material nearer to the axis of the tube or vice-versa the subflows consisting of at least two flat layers which are recombined, e.g. using means having restriction or expansion zones
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F2101/00Mixing characterised by the nature of the mixed materials or by the application field
    • B01F2101/2305Mixers of the two-component package type, i.e. where at least two components are separately stored, and are mixed in the moment of application
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00Other mixers; Mixing plants; Combinations of mixers
    • B01F33/50Movable or transportable mixing devices or plants
    • B01F33/501Movable mixing devices, i.e. readily shifted or displaced from one place to another, e.g. portable during use
    • B01F33/5011Movable mixing devices, i.e. readily shifted or displaced from one place to another, e.g. portable during use portable during use, e.g. hand-held

Definitions

  • the invention relates to a static mixer, a device with a such mixer and use of the mixer.
  • the mixing results of the mixers mentioned are for individual applications insufficient, especially in cases where components are mixed that have different values of their viscosity. On insufficient mixed result manifests itself in the fact that at least one Flow thread that only consists of one of the components to be mixed exists, the mixer structure passes through and practically no or one to experiences slow mixing with adjacent flow threads. On such flow threads are referred to here as "mix-resistant”. Mixing-resistant flow threads come mainly in static mixers before, whose mixer structure consists of a periodic sequence of similar elementary mixing chambers. But also for non-periodic ones Mixer-resistant flow threads can be observed in mixer structures.
  • the object of the invention is to provide a static mixer, the Mixing result compared to the known mixers is improved. This The object is achieved by the static mixer defined in claim 1.
  • the static mixer includes a plurality of mixing chambers, one Form mixer structure.
  • the mixing chambers are in a tube along one Pipe axis arranged behind and next to each other. They are for mixing usable from at least two flowable components.
  • the Mixer structure represents a modification of a basic structure. In this Basic structure are the mixing chambers through radial, in the direction of Pipe axis oriented walls and through walls that are transverse to the pipe axis Walls separated from each other. Breakthroughs between neighboring Chambers in the radial walls form entrances and exits for the mixing components.
  • the modification consists of structural changes at individual points in the basic structure. It is designed in such a way that Flow of the components to be mixed is a transversal Dislocation of mix-resistant flow threads results, this Flow threads are resistant to mixing with respect to the basic structure.
  • the impurities have flow areas outside of the mix-resistant flow thread are usually a disadvantage Effect on the mixing process. If this is the case, only as many should be used Impurities are provided, such as for a sufficient number of Dislocation of the mix-resistant flow threads is necessary.
  • the defects can be designed so that they are not directly on the mix resistant flow threads, but indirectly by acting in their direct sphere of influence cause diversions, which in turn then influence the mix-resistant flow thread.
  • An arrangement suitable defects can be found empirically.
  • a device 100 is indicated by dash-dotted lines in FIG. 1.
  • This contains a static mixer 1, the mixer structure 1 'of which is a regular, unmodified basic structure 1 "forms.
  • the mixer structure 1 ' is as Side view shown. It is known from EP-A-0 749 776 and EP-A- 0 815 929, in which the basic structure 1 "on two different Wise is described:
  • the basic structure 1 consists of a multitude of Mixing elements together, arranged in a tube 10 one behind the other are; or it consists of a bundle of four chambered strands, whose mixing chambers 8 (“mixing chambers”) each between extend two closed ends 4a and 4b.
  • the mixing chambers 8 of the basic structure 1 "are of the same size without any installation and staggered.
  • Two side Reinforcement walls 5 extend over the entire length of the mixer 1.
  • the device 100 comprises a two-chambered container 100a, namely a cartridge with chambers 101 and 102. These are used for separate Inclusion of two flowable components A and B.
  • a and B can be inserted into the tube by means of pistons 111 and 112 10 are pressed in (arrows A ', B').
  • static mixer 1 which consists of the tube 10 and the mixer structure 1 ' the mixture exits the device through a nozzle 120 100 out.
  • the cartridge 100a can comprise more than two chambers.
  • the Tube 10 can be a tube part that can be placed on the cartridge 100a be trained.
  • FIG. 2 A section along the line II - II is shown in Fig. 2.
  • the mixer structure 1 ' is flowed through by the two components A and B, the same values for the Have viscosity.
  • Arrows in the mixing chamber 8 indicate the flow pattern (with the symbols 'circle with cross' and 'circle with point' arrows following below or above - in relation to the image plane - mean).
  • the Flow pattern is based on results of a numerical simulation drawn. As you can see, the flow threads appear to be of similar thickness Layers; this means good mixing.
  • Fig. 3 shows a corresponding representation as in Fig. 2, here for two Components A and B, their viscosity values by a factor of 100 are different.
  • the less viscous component B is much narrower Layers because this component flows faster.
  • the flow threads spread unevenly. Another unevenness is particularly strong over a cross section perpendicular to shown section stands. These irregularities are bad Mixing results.
  • Web 91 is formed in the mixing chamber 8 'to the tube axis 11 or axis the mixer structure 1 'is inclined.
  • the web 91 connects on a radial Wall 2 has an entrance 6b with an exit 7a such that the Flow through the web 91 from the tube wall 10 in the direction of the tube axis 11 is deflected (arrow 91 ').
  • the reverse is also possible: one Flow deflection through the web 91 from the tube axis 11 in the direction Pipe wall 10.
  • the modification 9 according to FIGS. 5 and 8 is shortened by the Lengths of three adjacent chambers 81, 82 and 83 with simultaneous Reduced number of inputs or outputs.
  • the pair is the the chambers 81 and 82 which lie one behind the other along the tube axis 11, arranged laterally from the third chamber 83.
  • Two breakthroughs 7c and 92 make a connection (arrow 92 ') between the two chambers of the pair 81, 82 ago.
  • a modification 9 advantageously includes several defects Modification elements 91 (first modification) or 81, 82, 83, 92 (second Modification), which is preferably carried out regularly over the entire length of the static mixer 1 can be positioned.
  • Modification elements 91 first modification
  • second Modification second Modification
  • the mixer structures 11 'of the described embodiments are included Advantage each monolithic; you can in particular from one Injection molded thermoplastic.
  • the mixer structure 11 ' has one rectangular cross-section and includes four arranged side by side Chamber strands. Each line forms a series of 5 to 15 mixing chambers 8.
  • Each chamber 8 of the basic structure has a length that is 1.5 to 2.5 times is longer than a chamber width, this width being greater than 1 mm and is less than 10 mm, preferably at least 2 mm and at most 5 mm.
  • the device 100 is suitable for mixing a highly viscous Components A with at least one further component B, one around can have a factor 10 to 1000 lower viscosity.
  • the Mass flow of the other component can be for example, by a factor of 10, less than the mass flow of highly viscous components.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Civil Engineering (AREA)
  • Structural Engineering (AREA)
EP01810047A 2000-02-17 2001-01-18 Mélangeur statique Expired - Lifetime EP1125626B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP01810047A EP1125626B1 (fr) 2000-02-17 2001-01-18 Mélangeur statique

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
EP00810133 2000-02-17
EP00810133 2000-02-17
EP01810047A EP1125626B1 (fr) 2000-02-17 2001-01-18 Mélangeur statique

Publications (2)

Publication Number Publication Date
EP1125626A1 true EP1125626A1 (fr) 2001-08-22
EP1125626B1 EP1125626B1 (fr) 2005-11-02

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Family Applications (1)

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EP01810047A Expired - Lifetime EP1125626B1 (fr) 2000-02-17 2001-01-18 Mélangeur statique

Country Status (1)

Country Link
EP (1) EP1125626B1 (fr)

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1312409A1 (fr) * 2002-03-22 2003-05-21 Sulzer Chemtech AG Mélangeur de tube avec un élément longitudinal
EP1837070A1 (fr) 2006-03-24 2007-09-26 StaMixCo Technology AG Mélangeur statique, et procédé de fabrication correspondant
US7645843B2 (en) 2004-12-17 2010-01-12 Borealis Technology Oy Process for polymerising olefins in the presence of an olefin polymerisation catalyst
EP2335817A3 (fr) * 2009-12-15 2012-06-13 HILTI Aktiengesellschaft Mélangeur statique
CN1720094B (zh) * 2002-12-06 2012-08-29 苏尔寿混合技术有限公司 静态混合器
DE202015105397U1 (de) 2015-10-13 2017-01-17 Nikolaus Brugner Statischer Mischer und Mischvorrichtung mit einem derartigen Mischer
WO2017027275A3 (fr) * 2015-08-07 2017-03-30 Nordson Corporation Éléments de mélange d'entrée ainsi que mélangeurs statiques et procédés de mélange associés
CN106659992A (zh) * 2014-06-12 2017-05-10 黄嘉豪 混合器
EP3241611A1 (fr) 2016-05-02 2017-11-08 Borealis AG Procédé d'alimentation d'un catalyseur de polymérisation
EP3338882A1 (fr) * 2016-12-14 2018-06-27 Felix Streiff Élément mélangeur à résistance et à action de mélange élevés
DE202018106654U1 (de) 2018-11-22 2019-02-06 Sulzer Mixpac Ag Statischer Mischer
US10245565B2 (en) 2015-08-07 2019-04-02 Nordson Corporation Double wall flow shifter baffles and associated static mixer and methods of mixing
CN111189759A (zh) * 2020-01-14 2020-05-22 安徽奇书生物科技有限公司 一种灌流显微镜
DE202023106686U1 (de) 2022-11-18 2024-04-02 Medmix Switzerland Ag Statischer Mischer
EP4371656A1 (fr) 2022-11-18 2024-05-22 medmix Switzerland AG Mélangeur statique avec moyens de séparation

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE202011050465U1 (de) 2011-06-16 2011-08-17 Vosschemie Gmbh Statischer Mischer zum Mischen von mindestens zwei fließfähigen Komponenten
US10898872B2 (en) 2015-11-13 2021-01-26 Re Mixers, Inc. Static mixer
DE102017117198A1 (de) 2017-07-28 2019-01-31 3lmed GmbH Mischer
WO2019020764A1 (fr) 2017-07-28 2019-01-31 Kettenbach Gmbh & Co. Kg Mélangeur

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1265659A (fr) * 1960-08-19 1961-06-30 Du Pont égaliseur d'écoulement pour liquides
US3239197A (en) * 1960-05-31 1966-03-08 Dow Chemical Co Interfacial surface generator
DE2343352A1 (de) * 1973-08-28 1975-03-13 Worcester Valve Co Ltd Vorrichtung zum mischen von fluden
US3893654A (en) * 1972-03-18 1975-07-08 Harunobu Miura Mixing apparatus
US4632568A (en) * 1984-05-30 1986-12-30 Ritter-Plastic Gmbh Static mixing column
US5944419A (en) * 1995-06-21 1999-08-31 Sulzer Chemtech Ag Mixing device

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3239197A (en) * 1960-05-31 1966-03-08 Dow Chemical Co Interfacial surface generator
FR1265659A (fr) * 1960-08-19 1961-06-30 Du Pont égaliseur d'écoulement pour liquides
US3893654A (en) * 1972-03-18 1975-07-08 Harunobu Miura Mixing apparatus
DE2343352A1 (de) * 1973-08-28 1975-03-13 Worcester Valve Co Ltd Vorrichtung zum mischen von fluden
US4632568A (en) * 1984-05-30 1986-12-30 Ritter-Plastic Gmbh Static mixing column
US5944419A (en) * 1995-06-21 1999-08-31 Sulzer Chemtech Ag Mixing device

Cited By (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1312409A1 (fr) * 2002-03-22 2003-05-21 Sulzer Chemtech AG Mélangeur de tube avec un élément longitudinal
CN1720094B (zh) * 2002-12-06 2012-08-29 苏尔寿混合技术有限公司 静态混合器
US7645843B2 (en) 2004-12-17 2010-01-12 Borealis Technology Oy Process for polymerising olefins in the presence of an olefin polymerisation catalyst
EP1837070A1 (fr) 2006-03-24 2007-09-26 StaMixCo Technology AG Mélangeur statique, et procédé de fabrication correspondant
EP2335817A3 (fr) * 2009-12-15 2012-06-13 HILTI Aktiengesellschaft Mélangeur statique
CN106659992B (zh) * 2014-06-12 2019-03-29 黄嘉豪 混合器
CN106659992A (zh) * 2014-06-12 2017-05-10 黄嘉豪 混合器
EP3156121A4 (fr) * 2014-06-12 2018-01-24 HUANG, Chia-Hao Mélangeur
US10427114B2 (en) 2015-08-07 2019-10-01 Nordson Corporation Double wall flow shifter baffles and associated static mixer and methods of mixing
US10363526B2 (en) 2015-08-07 2019-07-30 Nordson Corporation Entry mixing elements and related static mixers and methods of mixing
WO2017027275A3 (fr) * 2015-08-07 2017-03-30 Nordson Corporation Éléments de mélange d'entrée ainsi que mélangeurs statiques et procédés de mélange associés
US10245565B2 (en) 2015-08-07 2019-04-02 Nordson Corporation Double wall flow shifter baffles and associated static mixer and methods of mixing
DE202015105397U1 (de) 2015-10-13 2017-01-17 Nikolaus Brugner Statischer Mischer und Mischvorrichtung mit einem derartigen Mischer
WO2017191054A1 (fr) 2016-05-02 2017-11-09 Borealis Ag Procédé d'alimentation de catalyseur de polymérisation
EP3241611A1 (fr) 2016-05-02 2017-11-08 Borealis AG Procédé d'alimentation d'un catalyseur de polymérisation
US10946357B2 (en) 2016-05-02 2021-03-16 Borealis Ag Process for feeding a polymerisation catalyst
EP3338882A1 (fr) * 2016-12-14 2018-06-27 Felix Streiff Élément mélangeur à résistance et à action de mélange élevés
DE202018106654U1 (de) 2018-11-22 2019-02-06 Sulzer Mixpac Ag Statischer Mischer
WO2020104473A2 (fr) 2018-11-22 2020-05-28 Sulzer Mixpac Ag Melangeur statique
CN111189759A (zh) * 2020-01-14 2020-05-22 安徽奇书生物科技有限公司 一种灌流显微镜
DE202023106686U1 (de) 2022-11-18 2024-04-02 Medmix Switzerland Ag Statischer Mischer
EP4371657A1 (fr) 2022-11-18 2024-05-22 medmix Switzerland AG Mélangeur statique
EP4371656A1 (fr) 2022-11-18 2024-05-22 medmix Switzerland AG Mélangeur statique avec moyens de séparation
WO2024104789A1 (fr) 2022-11-18 2024-05-23 Medmix Switzerland Ag Mélangeur statique avec moyens de séparation

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Publication number Publication date
EP1125626B1 (fr) 2005-11-02

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