WO2003027509A1 - Dispositif de traitement hydrodynamique de milieux fluides - Google Patents

Dispositif de traitement hydrodynamique de milieux fluides Download PDF

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Publication number
WO2003027509A1
WO2003027509A1 PCT/RU2002/000433 RU0200433W WO03027509A1 WO 2003027509 A1 WO2003027509 A1 WO 2003027509A1 RU 0200433 W RU0200433 W RU 0200433W WO 03027509 A1 WO03027509 A1 WO 03027509A1
Authority
WO
WIPO (PCT)
Prior art keywords
sρedy
outlet
fact
τeκuchey
ρezeρvuaρa
Prior art date
Application number
PCT/RU2002/000433
Other languages
English (en)
Russian (ru)
Inventor
Sergei Borisovich Osipenko
Original Assignee
Klimchuk, Natalia Vasilievna
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 Klimchuk, Natalia Vasilievna filed Critical Klimchuk, Natalia Vasilievna
Priority to EA200400389A priority Critical patent/EA006420B1/ru
Publication of WO2003027509A1 publication Critical patent/WO2003027509A1/fr

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Classifications

    • 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
    • B01F23/02—Maintaining the aggregation state of the mixed materials
    • B01F23/023—Preventing sedimentation, conglomeration or agglomeration of solid ingredients during or after mixing by maintaining mixed ingredients in movement
    • 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
    • B01F23/50—Mixing liquids with solids
    • B01F23/56—Mixing liquids with solids by introducing solids in liquids, e.g. dispersing or dissolving
    • 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
    • B01F25/10—Mixing by creating a vortex flow, e.g. by tangential introduction of flow 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
    • B01F25/50—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle
    • B01F25/53—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle in which the mixture is discharged from and reintroduced into a receptacle through a recirculation tube, into which an additional component is introduced

Definitions

  • ⁇ a ⁇ ie us ⁇ ys ⁇ va m ⁇ gu ⁇ sluzhi ⁇ ⁇ sn ⁇ v ⁇ y a) nag ⁇ eva ⁇ eley-smesi ⁇ eley, ⁇ ye ⁇ ednaznacheny: for g ⁇ m ⁇ genizatsii and ⁇ as ⁇ e ⁇ izatsii or s ⁇ e ⁇ ilizatsii ⁇ a ⁇ i ⁇ ⁇ ischevy ⁇ ⁇ du ⁇ v, ⁇ a ⁇ m ⁇ l ⁇ , sliv ⁇ i, bezal ⁇ g ⁇ lnye or slab ⁇ al ⁇ g ⁇ lnye ⁇ ladi ⁇ elnye na ⁇ i ⁇ i, and ⁇ iv ⁇ ⁇ . ⁇ .; for food and food processing (in particular, in the process of storage or sterilization), susceptible to dispersible material
  • the device is well known from the text and drawings (especially FIGS. 8 and 9) of Publication 98/42987 of the International Application ⁇ C ⁇ / C ⁇ 97/. It has a rotary pump and a separate, fully-functional quick-release pump. ⁇ Often, this appliance is connected to: food and drink compartments - related to the source of good water and to the customers; The private part - for the suction pipe of the pump through the recirculated pipe and the upper part - due to the excitation of the hydraulic cavitation - is the outlet.
  • This equipment is suitable for the needs of dispersion and heat treatment of dispersions.
  • the access to the pump is connected to the suction port of the pump to the recycled pump, and the connection to the pump is disconnected to the suction port.
  • ⁇ a ⁇ im ⁇ b ⁇ az ⁇ m is ⁇ lyuchayu ⁇ sya ⁇ ezhdev ⁇ emenny un ⁇ s or ⁇ sazhdenie dis ⁇ e ⁇ gi ⁇ uemy ⁇ ma ⁇ e ⁇ ial ⁇ v, susches ⁇ venn ⁇ us ⁇ yae ⁇ sya ⁇ davlenie mi ⁇ l ⁇ y and ⁇ bes ⁇ echivae ⁇ sya susches ⁇ venn ⁇ e ⁇ vyshenie s ⁇ y ⁇ s ⁇ i ⁇ luchenny ⁇ emulsions or sus ⁇ enzy ⁇ ⁇ asslaivaniyu and ⁇ che ⁇ i dli ⁇ eln ⁇ m ⁇ anenii.
  • the first optional feature is that the indicated large receptacle is equipped with a generic and prone to coronary lesion.
  • a further optional difference is that the indicated ugly receptacle is located in a vertical and has a distinctive, patent and harmful.
  • Two indicated partial variants of the invention are most effective for hydrodynamic processing of large-scale industrial products.
  • the optional accessory is augmented by the fact that the indicated angular receptacle is equipped with a generous and patented portal.
  • a four-sided additional difference is that the indicated is a large round receptacle that is equipped with a non-surgical and has a radial reciprocating patient.
  • a fifth optional feature is that the indicated augmented cavity is a vertical and has a tangential receptacle.
  • the sale of the product is most effective for hydrodynamic treatment of the cause of the loss of food in the event of a loss of life.
  • Seventh and eighth optional parts are, respectively, incl.
  • P ⁇ nya ⁇ n ⁇ , ch ⁇ ⁇ i vyb ⁇ e ⁇ n ⁇ e ⁇ ny ⁇ ⁇ m vy ⁇ lneniya us ⁇ ys ⁇ v for gid ⁇ dinamiches ⁇ y ⁇ b ⁇ ab ⁇ i ⁇ e ⁇ uchi ⁇ s ⁇ ed v ⁇ zm ⁇ zhny ⁇ izv ⁇ lnye ⁇ mbinatsii u ⁇ azanny ⁇ d ⁇ lni ⁇ elny ⁇ ⁇ lichy with ⁇ sn ⁇ vnym iz ⁇ b ⁇ e ⁇ a ⁇ els ⁇ im zamysl ⁇ m and ch ⁇ ⁇ isannye below ⁇ ed ⁇ ch ⁇ i ⁇ elnye ⁇ ime ⁇ y eg ⁇ v ⁇ l ⁇ scheniya ni ⁇ im ⁇ b ⁇ az ⁇ m not ⁇ g ⁇ anichivayu ⁇ ⁇ bom iz ⁇ b ⁇ e ⁇ eniya.
  • FIG. 1 front view
  • Fig. 3 device with a vertical outlet, which has a central receptacle and a tangential exit duct (view of the unit);
  • Fig. 4 the same as in Fig. 3 (view of the top);
  • Fig. 5 a device with a horizontal outlet, which has a tangential receptacle and a central outlet (view of the unit);
  • Fig.6 - the same as in Fig.5 (front view);
  • Fig. 7 - a device with a horizontal outlet, which has a radial recirculated part and a central part outlet (view of the part);
  • Fig. 8 the same as in Fig. 7 (front view);
  • FIG. 9 - a device with a vertical outlet, which has a tangential receptacle and a central outlet (view of the unit); fig. U- the same as in fig. 9 (view from above); Fig. P - devices with a hot outlet, camera and degassing unit (type of discharge from a waste room); Fig. 12 - the same as in Fig. 11 (side view with a similar breakout); Fig. 13 - devices with a vertical outlet, a camera and a heating and degassing unit (a kind of a discharge from a waste room); Fig. 14 - the same as in Fig. 13 (view from above); Fig. 15 - a device with a vertical outlet, which has a built-in cycle for temperature control and degassing (a type of discharge from the discharge port); Fig. 16 - the same as in Fig. 15 (view from above);
  • ⁇ sluchaya ⁇ (a) ⁇ ugly ⁇ eze ⁇ vua ⁇ 3 and ⁇ ame ⁇ a 8 ⁇ e ⁇ m ⁇ s ⁇ a ⁇ i ⁇ vaniya, ⁇ aya imee ⁇ tsen ⁇ alnye v ⁇ dnye and vy ⁇ dnye ⁇ ve ⁇ s ⁇ iya in ⁇ tsevy ⁇ s ⁇ en ⁇ a ⁇ and, ⁇ request without ⁇ azannye on che ⁇ ezha ⁇ ⁇ e ⁇ atsi ⁇ nnye ⁇ ve ⁇ s ⁇ iya in b ⁇ vy ⁇ s ⁇ en ⁇ a ⁇ , m ⁇ gu ⁇ by ⁇ ⁇ as ⁇ l ⁇ zheny ⁇ a ⁇ g ⁇ iz ⁇ n ⁇ aln ⁇ ( ⁇ igu ⁇ y 11 and 12) and vertical ( Figures 13 and 14).
  • ⁇ dna ⁇ tseles ⁇ b ⁇ azn ⁇ ch ⁇ by: ⁇ etsi ⁇ ulyatsi ⁇ nnye ⁇ a ⁇ ub ⁇ i 4 were ⁇ d ⁇ lyucheny ⁇ s ⁇ en ⁇ e or ⁇ tsen ⁇ aln ⁇ y z ⁇ ne ⁇ l ⁇ s ⁇ i ⁇ eze ⁇ vua ⁇ a 3 away ⁇ tsen ⁇ alny ⁇ v ⁇ dny ⁇ ⁇ ve ⁇ s ⁇ y ⁇ ame ⁇ 8 ⁇ e ⁇ m ⁇ s ⁇ a ⁇ i ⁇ vaniya, ⁇ ame ⁇ y 8 ⁇ e ⁇ m ⁇ s ⁇ a ⁇ i ⁇ vaniya had in ve ⁇ ni ⁇ chas ⁇ ya ⁇ g ⁇ iz ⁇ n ⁇ alnye ⁇ e ⁇ i ⁇ vannye ⁇ e ⁇ eg ⁇ d ⁇ i 11 ⁇ s ⁇ ans ⁇ v ⁇ over ⁇ a ⁇ imi ⁇ e ⁇ eg ⁇ d ⁇ ami 11 s ⁇ bschal ⁇ s with a ⁇
  • Cycle 10 for heat and degassing of a processed fluid medium is normally located vertically.
  • Cycle 10 is equipped with, in the upper part, a horizontal disassembled disengaged 11. Empty this circuit; 10 is disconnected: 15 ⁇ d ⁇ e ⁇ eg ⁇ d ⁇ y 11 che ⁇ ez s ⁇ bs ⁇ vennye ⁇ a ⁇ ub ⁇ - ⁇ ve ⁇ vi ⁇ el 13 za ⁇ n ⁇ - ⁇ eguli ⁇ uyuschim elemen ⁇ m 7 and ⁇ angentsialn ⁇ ⁇ ien ⁇ i ⁇ vann ⁇ e s ⁇ eds ⁇ v ⁇ 14 ⁇ u ⁇ bulizatsii - ⁇ nagne ⁇ a ⁇ eln ⁇ mu ⁇ a ⁇ ub ⁇ u nas ⁇ sa 1, and in d ⁇ nn ⁇ y chas ⁇ i - ⁇ ⁇ v ⁇ dyaschemu ⁇ a ⁇ ub ⁇ u 5.
  • na ⁇ nets, ⁇ a ⁇ ub ⁇ i 12 (see FIG. ⁇ igu ⁇ y 11-16) m ⁇ gu ⁇ by ⁇ , ⁇ i wish associated with a ⁇ m ⁇ s ⁇ e ⁇ y che ⁇ ez not ⁇ azannye on che ⁇ ezha ⁇ s ⁇ eds ⁇ va in ⁇ ensi ⁇ i ⁇ atsii ⁇ s ⁇ sa ⁇ i ⁇ a ⁇ sh ⁇ izves ⁇ ny ⁇ s ⁇ etsialis ⁇ am and d ⁇ s ⁇ u ⁇ ny ⁇ on ⁇ yn ⁇ e vy ⁇ yazhny ⁇ ven ⁇ ilya ⁇ v, and v ⁇ d ⁇ s ⁇ uyny ⁇ ⁇ d ⁇ bny ⁇ them ⁇ ⁇ izv ⁇ di ⁇ eln ⁇ s ⁇ i va ⁇ uum- pumps.
  • the devices that are described above are used for hydraulic processing in the following way.
  • a large reservoir 3 does not just equalize the temperature, but it does not become volatile.
  • ⁇ it ⁇ i ⁇ avens ⁇ ve ⁇ dachi fresh and ⁇ b ⁇ a ⁇ b ⁇ ab ⁇ ann ⁇ y ⁇ e ⁇ uchey s ⁇ edy in ⁇ ezhime av ⁇ eguli ⁇ vaniya ⁇ is ⁇ di ⁇ ⁇ a ⁇ e ne ⁇ e ⁇ yvn ⁇ e ⁇ a ⁇ tsi ⁇ ni ⁇ vanie ⁇ a, ⁇ i ⁇ m Part ⁇ b ⁇ aba ⁇ yvaem ⁇ y ⁇ e ⁇ uchey s ⁇ edy ⁇ b ⁇ gaschae ⁇ sya dis ⁇ e ⁇ gi ⁇ uemym ma ⁇ e ⁇ ial ⁇ m and ne ⁇ e ⁇ yvn ⁇ ⁇ s ⁇ u ⁇ ae ⁇ on ⁇ etsi ⁇ ulyatsiyu che ⁇ ez ⁇ a ⁇ ub ⁇ 4 nas ⁇ s 1f
  • each particle is dispersed and is kept in the direct part of the body, which means that there is little mass in it.
  • ve g ⁇ m ⁇ genizi ⁇ vann ⁇ y and ⁇ e ⁇ miches ⁇ i ⁇ b ⁇ ab ⁇ ann ⁇ y ⁇ as ⁇ e ⁇ iz ⁇ vann ⁇ y or s ⁇ e ⁇ iliz ⁇ vann ⁇ y
  • ⁇ e ⁇ uchey s ⁇ edy bude ⁇ derived in ⁇ v ⁇ dyaschy ⁇ a ⁇ ub ⁇ 5.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Dairy Products (AREA)
  • Nitrogen And Oxygen Or Sulfur-Condensed Heterocyclic Ring Systems (AREA)

Abstract

Le dispositif comprend une pompe avec des tubulures d'aspiration et d'injection qui est reliée à une source de milieu fluide frais; un moyen de formation de tourbillons à partir du flux dudit milieu à la sortie de la pompe; un moyen de fractionnement en continu du flux de milieu fluide tourbillonnant, la fraction enrichie par la matière dispersée étant alimentée pour être recyclée et la fraction du produit cible étant prélevée pour être consommée. Afin d'empêcher l'entraînement ou la sédimentation précoce des matières dispersées, le moyen de fractionnement en continu se présente comme un réservoir rond. La sortie du moyen de formation de tourbillons est raccordé tangentiellement à ce réservoir près de l'une de ses extrémités, et les tubulures de recyclage et d'évacuation sont munies d'éléments de sectionnement et de réglage et raccordés à ce réservoir, respectivement, dans la zone de collecte de la fraction enrichie par la matière dispersée et dans la zone de collecte de la fraction du produit cible.
PCT/RU2002/000433 2001-09-26 2002-09-26 Dispositif de traitement hydrodynamique de milieux fluides WO2003027509A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EA200400389A EA006420B1 (ru) 2001-09-26 2002-09-26 Устройство для гидродинамической обработки текучих сред

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
RU2001126104/06A RU2218491C2 (ru) 2001-09-26 2001-09-26 Устройство для гидродинамической обработки текучих сред
RU2001126104 2001-09-26

Publications (1)

Publication Number Publication Date
WO2003027509A1 true WO2003027509A1 (fr) 2003-04-03

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/RU2002/000433 WO2003027509A1 (fr) 2001-09-26 2002-09-26 Dispositif de traitement hydrodynamique de milieux fluides

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EA (1) EA006420B1 (fr)
RU (1) RU2218491C2 (fr)
WO (1) WO2003027509A1 (fr)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20090181151A1 (en) * 2005-12-16 2009-07-16 Sergey Borisovich Osipenko Soybean Paste 2C and Method for Preparing Thereof
EA017783B1 (ru) * 2011-12-09 2013-03-29 Сергей Александрович БУЧИК Аппарат для очистки воды
RU2486950C1 (ru) * 2012-03-27 2013-07-10 Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Пензенская государственная технологическая академия" Способ получения растворов в цилиндрической вертикальной емкости, нагреваемой в основном со стороны днища, например, для работы шлихтовальной машины ткацкого производства
RU2497934C1 (ru) * 2012-10-01 2013-11-10 Общество с ограниченной ответственностью "ЛУКОЙЛ-Волганефтепродукт" Устройство для переработки нефтеотходов
US9656221B2 (en) * 2014-01-24 2017-05-23 Baker Hughes Incorporated Systems and methods for treating fluids

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU1687939A1 (ru) * 1989-03-02 1991-10-30 Институт Физико-Технических Проблем Энергетики Ан Литсср Устройство дл исследовани гидродинамики закрученного потока
WO1998042987A1 (fr) * 1997-03-24 1998-10-01 Sergei Borisovich Osipenko Dispositif pour influencer l'ecoulement d'un fluide
RU9572U1 (ru) * 1998-11-03 1999-04-16 Общество с ограниченной ответственностью "Научно-производственное предприятие "ТЕКМАШ" Устройство для термообработки жидких сред

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU1687939A1 (ru) * 1989-03-02 1991-10-30 Институт Физико-Технических Проблем Энергетики Ан Литсср Устройство дл исследовани гидродинамики закрученного потока
WO1998042987A1 (fr) * 1997-03-24 1998-10-01 Sergei Borisovich Osipenko Dispositif pour influencer l'ecoulement d'un fluide
RU9572U1 (ru) * 1998-11-03 1999-04-16 Общество с ограниченной ответственностью "Научно-производственное предприятие "ТЕКМАШ" Устройство для термообработки жидких сред

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Publication number Publication date
EA006420B1 (ru) 2005-12-29
RU2218491C2 (ru) 2003-12-10
EA200400389A1 (ru) 2005-04-28

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