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EP0644271A4 - Verfahren zur herstellung eines frei dispersen system und einrichtung zur durchführung des verfahrens. - Google Patents

Verfahren zur herstellung eines frei dispersen system und einrichtung zur durchführung des verfahrens.

Info

Publication number
EP0644271A4
EP0644271A4 EP19920903375 EP92903375A EP0644271A4 EP 0644271 A4 EP0644271 A4 EP 0644271A4 EP 19920903375 EP19920903375 EP 19920903375 EP 92903375 A EP92903375 A EP 92903375A EP 0644271 A4 EP0644271 A4 EP 0644271A4
Authority
EP
European Patent Office
Prior art keywords
ποτοκa
cavitation
channel
narrowing
elements
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.)
Withdrawn
Application number
EP19920903375
Other languages
English (en)
French (fr)
Russian (ru)
Other versions
EP0644271A1 (de
Inventor
Oleg Vyacheslavovich Kozjuk
Alexandr Anatolievi Litvinenko
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Publication of EP0644271A4 publication Critical patent/EP0644271A4/de
Publication of EP0644271A1 publication Critical patent/EP0644271A1/de
Withdrawn legal-status Critical Current

Links

Classifications

    • 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
    • B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/431—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
    • 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
    • B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/431—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
    • B01F25/43197—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor characterised by the mounting of the baffles or obstructions
    • 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
    • B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/434—Mixing tubes comprising cylindrical or conical inserts provided with grooves or protrusions

Definitions

  • the process of cavitational dispersion is associated with the formation of cumulative microorganisms. It is proposed that 5, as a result of the interaction of the shock wave, produced by pulverized caviters, with particulate excipients. Intensive mixing and disintegration is explained by the larger microprocessors.
  • Parameters of 10 that determine the intensity of the energy activity of the hydrodynamic cavitation field are the degree of cavitation and the territory of the territory of the country.
  • the method makes it possible to regulate the intensity of the resulting hydraulically-driven cavitation
  • the local narrowing of the channel has a ring-shaped channel, an optimal channel and the use of - 8 - the use of energy from hydraulic flow and the processing of components.
  • Tseles ⁇ b ⁇ azn ⁇ to reduce ene ⁇ g ⁇ za ⁇ a ⁇ ⁇ u ⁇ em ma ⁇ - simaln ⁇ g ⁇ is ⁇ lz ⁇ vaniya ⁇ ine ⁇ iches ⁇ y ene ⁇ gii gid ⁇ dina- miches ⁇ g ⁇ ⁇ a, ch ⁇ by ⁇ l ⁇ b ⁇ e ⁇ aem ⁇ e ⁇ el ⁇ s ⁇ de ⁇ zhal ⁇ ⁇ at me ⁇ e ⁇ i elemen ⁇ a, imeyuschi ⁇ ⁇ azhdy ⁇ mu chenn ⁇ g ⁇ ⁇ nusa truncated corners with ⁇ azlichnymi ⁇ nusn ⁇ s ⁇ i and ⁇ as ⁇ l ⁇ - zhenny ⁇ ⁇ a ⁇ , ch ⁇ i ⁇ ⁇ si na ⁇ dya ⁇ sya in ⁇ l ⁇ s ⁇ s ⁇ i ⁇ dn ⁇ g ⁇ the main section of the main channel and associated with the smaller base, installed in the main channel
  • Tseles ⁇ b ⁇ azn ⁇ for ⁇ e ⁇ uli ⁇ vaniya s ⁇ e ⁇ eni ⁇ avi ⁇ atsii ⁇ avi ⁇ atsi ⁇ nny ⁇ ⁇ ley, v ⁇ zni ⁇ ayuschi ⁇ for truncated ⁇ nusami, ch ⁇ by ⁇ slednie were associated with de ⁇ zha ⁇ elem with v ⁇ zm ⁇ zhn ⁇ s ⁇ yu ⁇ v ⁇ a v ⁇ ug ⁇ sey, ⁇ as ⁇ l ⁇ zhenny ⁇ in ⁇ ya ⁇ s ⁇ s ⁇ i ⁇ e ⁇ endi- ⁇ ulya ⁇ n ⁇ y ⁇ si ⁇ chn ⁇ g ⁇ ⁇ anala.
  • cavitated fields are used to receive the impulse of disruption, which ensures that there are large, profitable, large, beneficial.
  • cavitational exposure to pulsed high blood pressure will result in more severe stiffness. Additional accumulated potential energy .
  • the apparatus is schematically set out in FIG. 7.
  • the execution of the body which is smaller of the two elements, is agreed upon. - 12 - That, the rate and the distance between the other is determined by the condition of the provision for the formation of each of the hydrodynamic factors in the case of
  • Parts 18, 19 are completed and arranged in a convenient manner, and part 20 is located at part 19 of the main building.
  • PARTS 19 and 20 are connected to the individual mechanisms of the mobile accommodation (not shown in FIG.). Other friends and the user are 18. 18. Disconnected
  • the device is located in channel 5 of the receiver
  • Part 22 is secured on the front side 26, installed in the main channel 5 of which is connected to it.
  • Part 23 is reserved on site 27, installed in the vicinity of section 26.
  • Section 27 is one with the mechanism (not shown in FIG. 2), it is seeding
  • Section II of the direct channel 5 is discharged with a clean body 21 two sections of 28.29 local narrowing are in danger of Moving auxiliaries 23 and augmenting the rooms 22 may regulate the intensity
  • the number of elements depends on the physical and chemical characteristics of the processed com- ponents and the related intensive intensity. ⁇ nusa 31-33 and 35-41 ⁇ as ⁇ l ⁇ - wife ⁇ a ⁇ , ch ⁇ i ⁇ ⁇ si na ⁇ dya ⁇ sya in ⁇ l ⁇ s ⁇ s ⁇ i ⁇ dn ⁇ g ⁇ ⁇ e- ⁇ echn ⁇ g ⁇ sectional ⁇ chn ⁇ g ⁇ ⁇ anala 5.
  • ⁇ enshimi ⁇ sn ⁇ vaniya- E ⁇ ni e ⁇ e ⁇ leny on de ⁇ zha ⁇ ele 42 ( ⁇ ig.Z) having a cylindri- d ⁇ iches ⁇ uyu ⁇ mu with ⁇ nus ⁇ b ⁇ aznymi ⁇ ntsami to reduce gid ⁇ dinamiches ⁇ g ⁇ s ⁇ ivleniya oncoming ⁇ u, ⁇ as- ⁇ l ⁇ zhenn ⁇ m s ⁇ sn ⁇ ⁇ chn ⁇ mu ⁇ ana ⁇ u 5.
  • ⁇ eny ⁇ ie ⁇ sn ⁇ vaniya usechenny ⁇ ⁇ nus ⁇ v 35- 41 in this option is reserved on line 48, installed in the simple channel 5 of which it is related.
  • Bad 46 depicted in FIG. 7, composed of - 15 - ⁇ y ⁇ e ⁇ elemen ⁇ v in ⁇ me usechenny ⁇ ⁇ nus ⁇ v 49,50,51,52 with ⁇ azlichnymi angles ⁇ nusn ⁇ s ⁇ i, ⁇ si ⁇ y ⁇ ⁇ as ⁇ l ⁇ zheny in ⁇ dn ⁇ y ⁇ l ⁇ s ⁇ s ⁇ i ⁇ e ⁇ echn ⁇ g ⁇ sectional ⁇ chn ⁇ g ⁇ ⁇ anala 5.
  • the device works as follows. Gid ⁇ dinamiches ⁇ y ⁇ ⁇ b ⁇ aba ⁇ yzaemy ⁇ ⁇ m ⁇ nen ⁇ v ⁇ s ⁇ el ⁇ e ⁇ che ⁇ ez v ⁇ dn ⁇ e ⁇ ve ⁇ s ⁇ ie 2 ⁇ n- ⁇ uz ⁇ 4 ⁇ s ⁇ u ⁇ ae ⁇ in ⁇ chny ⁇ anal 5, and vice ⁇ dzhimae ⁇ sya ⁇ e ⁇ ae ⁇ on ⁇ l ⁇ b ⁇ e ⁇ aem ⁇ e ⁇ el ⁇ 7 ⁇ chnee on eg ⁇ ⁇ e ⁇ vy elemen ⁇ - ⁇ ly truncated ⁇ nus 8.
  • the device according to the invention (Figs. 3-5), works with the following method.
  • the difference in the average diametr will be to divide the different frequencies of the output - 18 - ⁇ avi ⁇ atsi ⁇ nny ⁇ ⁇ ave ⁇ n for ⁇ azhdym ⁇ nus ⁇ v from 31-33 or 35-41, ⁇ yvayas, ⁇ e ⁇ emeschayas in gid ⁇ dinamiches ⁇ m ⁇ e and ⁇ as- ⁇ adayas in ⁇ blas ⁇ i pressure vys ⁇ g ⁇ , ⁇ ave ⁇ ny ⁇ b ⁇ azuyu ⁇ ⁇ ulsi ⁇ uschie ⁇ avi ⁇ atsi ⁇ nnye ⁇ lya for ⁇ azhdym of elemen ⁇ v, s ⁇ s ⁇ yaschie of ⁇ avi ⁇ atsi ⁇ nny ⁇ ⁇ uzy ⁇ v ⁇ azlichny ⁇ ⁇ azme ⁇ v.
  • 25 zhina 47 is also a source of additional pulsations of the flow, affecting the pattern of cohesiveness of highly infected patients, enhancing erosive.
  • the cost of the processing of components is only slightly higher than that of the variant of the placement of a single appliance.
  • This version of the device is the most efficient in connection with the acquisition of a high volume of property.
  • Hydraulic flow consisting of 95% by weight of water and 5% by weight of industrial oil, is delivered at a speed of 5 to 40.5 m / s through a unit of 2, which is not used.
  • the speed () of the processed emulsion at the outlet of the direct channel is 18.7 m / s.
  • the emulsions obtained are estimated to be at a remote level of the dispersed (oily) phase.
  • ⁇ Cos-20 is 1000 m ⁇ / m 3 .
  • the invention will find use in chemical, non-chemical, industrial and chemical applications, inks, paints, insecticides; in fuel and energy industry, when cooking on base oils and typical oils; in the machine for the preparation of emulsions, lubricating and cooling liquids; in ⁇ a ⁇ yume ⁇ n ⁇ y ⁇ myshlenn ⁇ s ⁇ i ⁇ i ⁇ izv ⁇ ds ⁇ ve zhid ⁇ i ⁇ and ⁇ chischayuschi ⁇ s ⁇ eds ⁇ v, l ⁇ s ⁇ n ⁇ v, vi ⁇ aminny ⁇ ⁇ e ⁇ a ⁇ a ⁇ v in ⁇ ischev ⁇ y ⁇ myshlenn ⁇ s ⁇ i ⁇ i ⁇ ig ⁇ vlenii nas ⁇ e ⁇ , ⁇ u ⁇ vy ⁇ s ⁇ v, al ⁇ g ⁇ l- ny ⁇ and bezal ⁇ g ⁇ lny ⁇ na ⁇ i ⁇ v, s ⁇ us ⁇ v, m ⁇ l ⁇ chny ⁇ ⁇ du ⁇ - ⁇ v and

Landscapes

  • Chemical & Material Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Nitrogen And Oxygen Or Sulfur-Condensed Heterocyclic Ring Systems (AREA)
EP92903375A 1991-11-29 1991-11-29 Verfahren zur herstellung eines frei dispersen systems und einrichtung zur durchführung des verfahrens Withdrawn EP0644271A1 (de)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/SU1991/000251 WO1994013392A1 (en) 1991-11-29 1991-11-29 Method and device for producing a free dispersion system

Publications (2)

Publication Number Publication Date
EP0644271A4 true EP0644271A4 (de) 1995-03-16
EP0644271A1 EP0644271A1 (de) 1995-03-22

Family

ID=21617807

Family Applications (1)

Application Number Title Priority Date Filing Date
EP92903375A Withdrawn EP0644271A1 (de) 1991-11-29 1991-11-29 Verfahren zur herstellung eines frei dispersen systems und einrichtung zur durchführung des verfahrens

Country Status (3)

Country Link
US (1) US5492654A (de)
EP (1) EP0644271A1 (de)
WO (1) WO1994013392A1 (de)

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EP0644271A1 (de) 1995-03-22
US5492654A (en) 1996-02-20
WO1994013392A1 (en) 1994-06-23

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