KR102047431B1 - 유동이 가역적인 균질화 공정 및 장치 - Google Patents

유동이 가역적인 균질화 공정 및 장치 Download PDF

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KR102047431B1
KR102047431B1 KR1020157019873A KR20157019873A KR102047431B1 KR 102047431 B1 KR102047431 B1 KR 102047431B1 KR 1020157019873 A KR1020157019873 A KR 1020157019873A KR 20157019873 A KR20157019873 A KR 20157019873A KR 102047431 B1 KR102047431 B1 KR 102047431B1
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South Korea
Prior art keywords
deflection
homogenization
interaction element
fluid
plugs
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KR1020157019873A
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Korean (ko)
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KR20150096803A (ko
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알프레도 리치
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게아 미케니컬 이큅먼트 이탈리아 에스.피.에이.
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/421—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions by moving the components in a convoluted or labyrinthine path
    • B01F25/423—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions by moving the components in a convoluted or labyrinthine path by means of elements placed in the receptacle for moving or guiding the components
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/44—Mixers in which the components are pressed through slits
    • B01F25/441—Mixers in which the components are pressed through slits characterised by the configuration of the surfaces forming the slits
    • B01F25/4412—Mixers in which the components are pressed through slits characterised by the configuration of the surfaces forming the slits the slits being formed between opposed planar surfaces, e.g. pushed again each other by springs
    • B01F5/0663—
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/44—Mixers in which the components are pressed through slits
    • B01F25/442—Mixers in which the components are pressed through slits characterised by the relative position of the surfaces during operation
    • B01F25/4422—Mixers in which the components are pressed through slits characterised by the relative position of the surfaces during operation the surfaces being maintained in a fixed but adjustable position, spaced from each other, therefore allowing the slit spacing to be varied
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/44—Mixers in which the components are pressed through slits
    • B01F25/442—Mixers in which the components are pressed through slits characterised by the relative position of the surfaces during operation
    • B01F25/4423—Mixers in which the components are pressed through slits characterised by the relative position of the surfaces during operation the surfaces being part of a valve construction, formed by opposed members in contact, e.g. automatic positioning caused by spring pressure
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71—Feed mechanisms
    • B01F35/717—Feed mechanisms characterised by the means for feeding the components to the mixer
    • B01F35/71805—Feed mechanisms characterised by the means for feeding the components to the mixer using valves, gates, orifices or openings
    • B01F5/068—
    • B01F5/0681—
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Disintegrating Or Milling (AREA)
  • General Preparation And Processing Of Foods (AREA)
  • Seeds, Soups, And Other Foods (AREA)
  • Beans For Foods Or Fodder (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Detergent Compositions (AREA)
  • Fats And Perfumes (AREA)
  • Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
  • Soy Sauces And Products Related Thereto (AREA)
KR1020157019873A 2012-12-21 2013-12-20 유동이 가역적인 균질화 공정 및 장치 Active KR102047431B1 (ko)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
IT000090A ITPR20120090A1 (it) 2012-12-21 2012-12-21 Procedimento e apparato di omogeneizzazione con inversione flusso
ITPR2012A000090 2012-12-21
PCT/IB2013/061179 WO2014097234A2 (en) 2012-12-21 2013-12-20 Homogenising process and apparatus with flow reversal

Publications (2)

Publication Number Publication Date
KR20150096803A KR20150096803A (ko) 2015-08-25
KR102047431B1 true KR102047431B1 (ko) 2019-12-02

Family

ID=47605665

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1020157019873A Active KR102047431B1 (ko) 2012-12-21 2013-12-20 유동이 가역적인 균질화 공정 및 장치

Country Status (12)

Country Link
US (1) US10159946B2 (enExample)
EP (1) EP2934733B1 (enExample)
JP (1) JP2016501720A (enExample)
KR (1) KR102047431B1 (enExample)
CN (1) CN104884153B (enExample)
BR (1) BR112015014958B1 (enExample)
CA (1) CA2895182C (enExample)
DK (1) DK2934733T3 (enExample)
ES (1) ES2607486T3 (enExample)
IT (1) ITPR20120090A1 (enExample)
RU (1) RU2621768C2 (enExample)
WO (1) WO2014097234A2 (enExample)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DK3291684T3 (en) * 2015-04-30 2019-04-15 Gea Mech Equipment Italia S P A PROCEDURE FOR YOGURT MANUFACTURING OR ANOTHER FERMENTED MILK BASED PRODUCT
US11332375B2 (en) 2015-09-25 2022-05-17 Lg Chem, Ltd. Peeling device of sheet material including optimized outlet
JP6614554B2 (ja) * 2016-11-15 2019-12-04 株式会社スギノマシン ノズル洗浄方法及び微粒化装置のノズル洗浄構造
CN109395666B (zh) * 2018-12-20 2023-09-26 中原工学院 一体化的对射流型反应器
IT202000007159A1 (it) * 2020-04-03 2021-10-03 Gea Mech Equipment Italia S P A Metodo di validazione di una valvola omogeneizzante
CN115614484B (zh) * 2022-10-28 2025-05-23 上海申鹿均质机有限公司 一种对撞式均质阀结构

Family Cites Families (29)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE361642C (de) * 1922-10-17 Bergedorfer Eisenwerk Akt Ges Homogenisiervorrichtung
DE271432C (enExample) *
FR17429E (fr) * 1913-08-30 John Henry Exshaw Cessionnaire Obturateur pour conduites et appareils dans lesquels circulent tous fluides, gaz, vapeurs ou liquides
NL48062C (enExample) 1938-03-11 1939-10-16
US2236013A (en) * 1939-07-17 1941-03-25 American Marsh Pumps Inc Homogenizer
US2274720A (en) * 1939-07-29 1942-03-03 Marco Company Inc Combinator head or homogenizer
US2662590A (en) * 1947-07-14 1953-12-15 Julius Vignati Gas burner and flow restrictor
US3164167A (en) * 1961-01-19 1965-01-05 Albina Ets Apparatus for homogenizing liquids and pulps
DE1258835B (de) 1964-08-28 1968-01-18 James R Lage Dr Mischeinrichtung
DD122649A1 (enExample) * 1975-09-10 1976-10-20
US4135829A (en) * 1977-08-24 1979-01-23 International Telephone And Telegraph Corporation Homogenizer
US4340311A (en) 1980-09-26 1982-07-20 Zebron Corporation Interfacial surface generator mixer
DE8711740U1 (de) * 1987-08-29 1987-12-23 Bran & Lübbe GmbH, 22844 Norderstedt Homogenisiervorrichtung
DE3818237A1 (de) * 1988-05-28 1989-11-30 Bran & Luebbe Hochdruckhomogenisator
US4860959A (en) * 1988-06-23 1989-08-29 Semi-Bulk Systems, Inc. Apparatus for subjecting particles dispersed in a fluid to a shearing action
US5217037A (en) * 1991-11-26 1993-06-08 Apv Gaulin, Inc. Homogenizing apparatus having magnetostrictive actuator assembly
US5273407A (en) * 1992-04-30 1993-12-28 Apv Gaulin Gmbh Homogenizing system having improved fluid flow path
CH685366A5 (fr) * 1992-12-09 1995-06-30 Nestle Sa Dispositif de traitement d'un produit fluide par injection de vapeur.
US5482369A (en) * 1993-02-08 1996-01-09 Verstallen; Adrian Process for homogenizing essentially immiscible liquids for forming an emulsion
GB9419520D0 (en) 1994-09-28 1994-11-16 Ic Consultants Limited A mixer and apparatus for analysing fluid flow
IT1282765B1 (it) 1996-05-30 1998-03-31 Niro Soavi Spa Valvola di omogeneizzazione
JP3149371B2 (ja) * 1996-12-26 2001-03-26 株式会社ジーナス 微粒化方法及びその装置
JPH10180069A (ja) * 1996-12-26 1998-07-07 Jiinasu:Kk 微粒化方法及びその装置
US5984519A (en) 1996-12-26 1999-11-16 Genus Corporation Fine particle producing devices
JPH1142428A (ja) 1997-07-25 1999-02-16 Jiinasu:Kk 微粒化方法
TW536425B (en) * 2001-05-30 2003-06-11 Cam Tecnologie S P A A static mixer and a process for producing dispersions, in particular dispersions of liquid fuel with water
CA2584955C (en) 2006-05-15 2014-12-02 Sulzer Chemtech Ag A static mixer
JP4893365B2 (ja) * 2007-02-27 2012-03-07 株式会社明電舎 マイクロバブル発生装置及びマイクロバブル発生システム
JP2010017623A (ja) * 2008-07-09 2010-01-28 Sanmaru Kikai Kogyo Kk ホモジナイザー

Also Published As

Publication number Publication date
US10159946B2 (en) 2018-12-25
RU2621768C2 (ru) 2017-06-07
CA2895182C (en) 2020-01-21
CN104884153B (zh) 2017-06-06
DK2934733T3 (en) 2017-01-30
WO2014097234A2 (en) 2014-06-26
CA2895182A1 (en) 2014-06-26
JP2016501720A (ja) 2016-01-21
EP2934733B1 (en) 2016-11-09
KR20150096803A (ko) 2015-08-25
ITPR20120090A1 (it) 2014-06-22
ES2607486T3 (es) 2017-03-31
EP2934733A2 (en) 2015-10-28
CN104884153A (zh) 2015-09-02
US20150298074A1 (en) 2015-10-22
BR112015014958B1 (pt) 2021-07-20
WO2014097234A3 (en) 2014-10-16
RU2015129450A (ru) 2017-01-26
BR112015014958A2 (pt) 2017-07-11

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Lieberman Ultrasonic homogenizing systems are able to produce particle-size and droplet-size distributions that approach those of piston homogenizers with a lower power re-quirement. In order to work, they must be fed a well-blended premix or a metered feed of the liquid components. The vibrating element is an extra maintenance item, espe-cially in heavy or abrasive service. Overall, they offer an attractive option when fixed-gap rotor/stator devices do not produce the required size distributions. 5. Homogenizer/Extruder Another high-pressure homogenizer/extruder with an adjustable valve having produc-tion capacities from 8 mL/hr to 12,000 LL/hr is available. A positive displacement pump produces pressures up to 30,000 psig. The manufacturer claims that no O-ring is used in the product pass and pump seal, and this homogenizer/extruder was approved by the US Food and Drug Administration for pharmaceutical use [36]. At this writing, in-formation concerning the internal structure is not available. The apparatus is capable of producing fine emulsions and liposomal dispersions. Figure 36 shows a laboratory unit. 6. Microfluidizer Technologies A more recent invention to find wide use in specialized forms of dispersed system dosage forms is the microfluidizer. This device uses a high-pressure positive-displacement pump operating at a pressure of 500-20,000 psig, which accelerates the process flow to up to 500 m/min through the interaction chamber. The interaction chamber consists of small channels known as microchannels. The microchannel diameters can be as narrow as 50 urn and cause the flow of product to occur as very thin sheets. The configuration of these microchannels within the interaction chamber resembles Y-shaped flow streams in which the process stream divides into these microchannels, creating two separate microstreams. The sum of cross-sectional areas of these two microstreams is less than the cross-sectional area of the pipe before division to two separate streams. This nar-rowing of the flow pass creates an (axisymmetric) elongational flow to generate high Fig. 36 Emulsiflex-C5, a high-pressure homogenizer.(From Ref. 36.)
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