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WO2002016783A1 - Dispositif pour agir sur un flux de milieu fluide - Google Patents

Dispositif pour agir sur un flux de milieu fluide Download PDF

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Publication number
WO2002016783A1
WO2002016783A1 PCT/UA2001/000027 UA0100027W WO0216783A1 WO 2002016783 A1 WO2002016783 A1 WO 2002016783A1 UA 0100027 W UA0100027 W UA 0100027W WO 0216783 A1 WO0216783 A1 WO 0216783A1
Authority
WO
WIPO (PCT)
Prior art keywords
gas
fluid
degassing
sρedy
channel
Prior art date
Application number
PCT/UA2001/000027
Other languages
English (en)
Russian (ru)
Other versions
WO2002016783A9 (fr
WO2002016783A8 (fr
Inventor
Sergey Borisovich Osypenko
Original Assignee
Osipenko Sergey Borisovich
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 Osipenko Sergey Borisovich filed Critical Osipenko Sergey Borisovich
Priority to AU2001280425A priority Critical patent/AU2001280425A1/en
Publication of WO2002016783A1 publication Critical patent/WO2002016783A1/fr
Publication of WO2002016783A9 publication Critical patent/WO2002016783A9/fr
Publication of WO2002016783A8 publication Critical patent/WO2002016783A8/fr

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F15—FLUID-PRESSURE ACTUATORS; HYDRAULICS OR PNEUMATICS IN GENERAL
    • F15D—FLUID DYNAMICS, i.e. METHODS OR MEANS FOR INFLUENCING THE FLOW OF GASES OR LIQUIDS
    • F15D1/00—Influencing flow of fluids
    • F15D1/02—Influencing flow of fluids in pipes or conduits
    • 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
    • B01F25/432—Mixing 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
    • 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
    • B01F25/432—Mixing 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
    • B01F25/4321—Mixing 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
    • B01F25/43211—Mixing 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 using a simple by-pass for separating and recombining the flow, e.g. by using branches of different length
    • 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
    • B01F25/433—Mixing tubes wherein the shape of the tube influences the mixing, e.g. mixing tubes with varying cross-section or provided with inwardly extending profiles
    • 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
    • B01F25/433—Mixing tubes wherein the shape of the tube influences the mixing, e.g. mixing tubes with varying cross-section or provided with inwardly extending profiles
    • B01F25/4335—Mixers with a converging-diverging cross-section
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17D—PIPE-LINE SYSTEMS; PIPE-LINES
    • F17D1/00—Pipe-line systems
    • F17D1/08—Pipe-line systems for liquids or viscous products
    • F17D1/14—Conveying liquids or viscous products by pumping
    • 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
    • B01F2025/91—Direction of flow or arrangement of feed and discharge openings
    • B01F2025/916—Turbulent flow, i.e. every point of the flow moves in a random direction and intermixes
    • 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
    • B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids

Definitions

  • the invention does not have access to equipment for the flow of fluid, and more than that, it is not intended to be damaged.
  • perfumery products such as lilacs, food creams and ⁇ . ⁇ .;
  • 35 c) such as operating in the intensive turbulent mode as in the cavitational mode 2-g ⁇ eva ⁇ eley a ⁇ iva ⁇ v with ⁇ chnysh or ⁇ etsm ⁇ ulyatsm ⁇ nnymm ⁇ n ⁇ u ⁇ amm, ⁇ ye ⁇ ednaznacheny for ⁇ e ⁇ m ⁇ me ⁇ an ⁇ imiches ⁇ y ⁇ b ⁇ ab ⁇ i ⁇ ea ⁇ tsm ⁇ nny ⁇ mixture v ⁇ lyu- chayuschm ⁇ ⁇ smaller me ⁇ e ⁇ din ⁇ vo ⁇ dy ine ⁇ ny ma ⁇ e ⁇ ial ⁇ i ⁇ a ⁇ ezin ⁇ v ⁇ y ⁇ sh ⁇ m, ⁇ e ⁇ ed zag ⁇ uz ⁇ y e ⁇ m ⁇ mixtures in (me ⁇ an ⁇ ) ⁇ mmiches ⁇ ie a ⁇ a ⁇ a ⁇ y (na ⁇ mme ⁇ , e ⁇ s ⁇ ude ⁇ y and 5 vul ⁇ anizatsi ⁇ nnye
  • This generator works in close proximity to the laminate mode, which excludes cavitation, and is very reliable in operation. However, for obvious reasons, there is a low specific power and low heat output for specialists.
  • ⁇ edn ⁇ e influence ⁇ egulya ⁇ ny ⁇ vib ⁇ atsy ⁇ i dli ⁇ eln ⁇ y ⁇ ab ⁇ e and ⁇ a ⁇ v ⁇ emen- ny ⁇ m ⁇ egulya ⁇ ny ⁇ vib ⁇ atsy ⁇ i za ⁇ us ⁇ e- ⁇ s ⁇ an ⁇ v ⁇ e on nadozhn ⁇ s ⁇ ne ⁇ udn ⁇ uches ⁇ ⁇ i ⁇ e ⁇ i ⁇ vanii m izg ⁇ vlenii us ⁇ ys ⁇ v for v ⁇ zdeys ⁇ viya on ⁇ i ⁇ e ⁇ uchi ⁇ s ⁇ ed u ⁇ - ⁇ chneniem ⁇ s ⁇ b ⁇ nag ⁇ uzhenny ⁇ chas ⁇ ey and ⁇ imeneniem ⁇ d ⁇ dyaschi ⁇ am ⁇ iza ⁇ v and shum ⁇ gl ⁇ i ⁇ eley.
  • An investigation of the pleasures in the course of a bullet-proof fluid environment results in large cavities (cavities) and a loss of development.
  • This phenomenon of specialism means the term “surgery”.
  • the pump is equipped with a pump for the immediate transfer of a working fluid, a channel for pumping a processed fluid, a pump.
  • a pump for the immediate transfer of a working fluid, a channel for pumping a processed fluid, a pump.
  • P ⁇ s ⁇ avlennaya task ⁇ eshena ⁇ em, ch ⁇ in us ⁇ ys ⁇ ve for v ⁇ zdeys ⁇ vmya on ⁇ ⁇ e ⁇ uchey s ⁇ edy, myeyuschesh nas ⁇ s for ne ⁇ e ⁇ yvn ⁇ y ⁇ dachi ⁇ e ⁇ uchey s ⁇ edy on ⁇ b ⁇ ab ⁇ u, ⁇ anal for ⁇ ⁇ achivansh ⁇ a ⁇ b ⁇ aba ⁇ yvaem ⁇ y ⁇ e ⁇ uchey s ⁇ edy, ⁇ d ⁇ lyuchonny ⁇ HA z ⁇ gne ⁇ a ⁇ eln ⁇ mu ⁇ a ⁇ ub ⁇ u nas ⁇ sa, s ⁇ eds ⁇ v ⁇ ⁇ u ⁇ bulizatsii ⁇ a ⁇ b ⁇ aba ⁇ yvaem ⁇ y ⁇ e ⁇ u - whose s ⁇ edy in e ⁇ m ⁇ ana
  • ne ⁇ e ⁇ yvnaya ⁇ eguli ⁇ ue maya degassing ⁇ u ⁇ buliz ⁇ vann ⁇ g ⁇ ⁇ a m ⁇ smaller me ⁇ e ⁇ e ⁇ i ⁇ diches ⁇ e removal izby ⁇ a gas na ⁇ ime ⁇ in a ⁇ m ⁇ - s ⁇ e ⁇ u or sb ⁇ ni ⁇ -na ⁇ i ⁇ el, susches ⁇ venn ⁇ snizhayu ⁇ ⁇ asn ⁇ s ⁇ su ⁇ e ⁇ avi ⁇ atsii m ⁇ busl ⁇ vlenny ⁇ it a ⁇ e ⁇ i ⁇ diches ⁇ i ⁇ uda ⁇ v and even e ⁇ zii ⁇ i ⁇ i ⁇ anii nas ⁇ sa ⁇ a ⁇ y HA 5 syschenn ⁇ y air and other pollutants, such as liquid and other volatile gases, as well
  • the first option is that the device, in addition, has a cheap connection for the sake of mediation. At first glance, it may be shown that this
  • thermo-generator shown in Fig. 98/829. Indeed, in this case, the known heat-generating part of the tank-accumulator is in charge;
  • a positive feedback is indicated as a first condition, and it is advantageous to use it in general.
  • Equipped with it facilities for driving on a flow of fluid are suitable when heated, or in the case of a fluid product. It is valid, good or cold, which is usually used to decontaminate water, as opposed to being heavily contaminated with water. Their complete removal from water, which is usedlessly used for hot water supply for other intensive and economical needs, is economically unsuitable. Therefore, the exclusion of the pump from the recirculating contact significantly weakens its wear and tear.
  • the ⁇ chn ⁇ g ⁇ ilm for ⁇ d ⁇ m ⁇ i ⁇ etsi ⁇ ulyatsi ⁇ nn ⁇ g ⁇ ⁇ u ⁇ a is ⁇ lzuyu ⁇ fresh ⁇ e ⁇ uchuyu s ⁇ edu, zaved ⁇ m ⁇ s ⁇ de ⁇ zhaschuyu ⁇ imesi ⁇ as ⁇ v ⁇ on- ny ⁇ gaz ⁇ v.
  • the ⁇ chn ⁇ g ⁇ or ⁇ d ⁇ i ⁇ i ⁇ etsi ⁇ ulyatsi ⁇ nn ⁇ g ⁇ ⁇ u ⁇ a is ⁇ lzuyu ⁇ degazi ⁇ vannuga fresh ⁇ e ⁇ uchuyu s ⁇ edu.
  • a ten-year-old third is more likely to be conveniently coupled with the use of a non-lenght connection. Possessing a gaseous fluid pump reduces the noise in the pump and the load on it.
  • a large format of the device is agreed upon by the invention and it is preferable to use the equipment of the autonomous supply system of the hot / cold water supply.
  • FIG. 1 the circuitry of such a simple device for the use of a torrent of fluid, the device is supplied with a non-removable device 5 ⁇ ig.2 - bl ⁇ -s ⁇ ema ⁇ a ⁇ g ⁇ ⁇ s ⁇ eysheg ⁇ us ⁇ ys ⁇ va for v ⁇ zdeys ⁇ viya on ⁇ ⁇ e ⁇ uchey s ⁇ edy, ⁇ e mmee ⁇ ⁇ b ⁇ a ⁇ nuyu link for v ⁇ zv ⁇ a ⁇ a chas ⁇ i ⁇ e ⁇ uchey s ⁇ edy with you ⁇ ⁇ da s ⁇ eds ⁇ va degassing v ⁇ d nas ⁇ sa; ⁇ ig.Z - bl ⁇ -s ⁇ ema ⁇ a ⁇ g ⁇ ⁇
  • FIG. 6 a block diagram of such a more complex device for arrears on the receipt of a death, but has a connection to you for a limited service
  • Fig. 7 is a block diagram of a more convenient device for entering into a flow of a liquid medium, which has a by-product for the treatment of a by-product of a by-product
  • Fig. 8 - a block diagram of such a more complex device for driving at a flow of 25 fluid mediums, which means that it is in case of loss of public life;
  • fmg. 9 flow chart of a simpler device for the participation in the sale of a fluid; Referring to Fig.
  • this is a block diagram of a more convenient device for the operation of a fluid medium; ⁇ ig.11 - bl ⁇ -c ⁇ EMA ⁇ a ⁇ g ⁇ b ⁇ lee sl ⁇ zhn ⁇ g ⁇ us ⁇ ms ⁇ va for v ⁇ zdems ⁇ viya on ⁇ ⁇ e ⁇ uchey s ⁇ edy, ⁇ e imee ⁇ ⁇ b ⁇ a ⁇ nuyu communication for v ⁇ zv ⁇ a ⁇ a chas ⁇ i ⁇ e ⁇ uchey s ⁇ edy with You are a 35 ⁇ da s ⁇ eds ⁇ va d ⁇ zi ⁇ vann ⁇ y ⁇ dachi gas in channel v ⁇ d nas ⁇ sa; 18 Fig. 12 - The main circuit of such a device is used for the operation of a fluid medium; Fig. 13 - the channel with the well-located access to the input channel
  • Fig. 16 is a schematic view of a recirculating heat generating unit with an active gas system of 20 gasification of a processed fluid medium at the primary outlet.
  • the throttle can be made in the form of 21 ⁇ chn ⁇ g ⁇ ⁇ n ⁇ uz ⁇ a 19, y ⁇ g ⁇ diame ⁇ v ⁇ dn ⁇ g ⁇ ⁇ ve ⁇ s ⁇ mya ⁇ evyshae ⁇ diame ⁇
  • 26 Located on the front side of the 27th part of the exhaust system, 26 lives in the throttle, which facilitates the release of gas from the gas-fired unit,
  • pump 1 through suction of the unit 2 is continuously supplied with a flowing medium from the source.
  • Consumption 1 forces this medium into channel 4, in which its kinetic energy comes under the influence of medium 3, and the process of transformation into thermal energy.
  • a median of 5 degassing, which is not immediately obsolete after 3 injuries, emits and, after an accidentally regulating element is 6, is less In this way, “emptiness” is significantly reduced, and the danger of acute and severe eruptions was significantly reduced, and the risk of acute erosion was increased.
  • Bay ⁇ asny ⁇ ub ⁇ v ⁇ d 8 (see. ⁇ ig.Z) ⁇ y ⁇ bes ⁇ echivae ⁇ ⁇ b ⁇ a ⁇ nuyu Me- forward link gid ⁇ avliches ⁇ im vy ⁇ d ⁇ m s ⁇ eds ⁇ va 5 degassing and v ⁇ d ⁇ m in s ⁇ eds ⁇ v ⁇ 3 ⁇ u ⁇ buliza- tion, ⁇ zv ⁇ lyae ⁇ is ⁇ lz ⁇ va ⁇ for za ⁇ av ⁇ i zam ⁇ nu ⁇ y ⁇ sis ⁇ em ⁇ e ⁇ l ⁇ snabzheniya v ⁇ d ⁇ - 24 natural water, which has been decontaminated by such gases as acid or liquid or its dispersive substances. Indeed, when starting the power supply system, such gases do not recycle through pump 1, and subsequently dissipate the exhausted air and consume the exhausted gas.
  • Bay ⁇ asny ⁇ ub ⁇ v ⁇ d 9 (see Fig. ⁇ ig.4) ⁇ y ⁇ bes ⁇ echivae ⁇ ⁇ b ⁇ a ⁇ nuyu Me- forward link v ⁇ d ⁇ m in s ⁇ eds ⁇ v ⁇ 5 degassing and v ⁇ d ⁇ m nas ⁇ sa 1 ⁇ zv ⁇ lyae ⁇ e ⁇ e ⁇ ivn ⁇ ⁇ eguli- ⁇ va ⁇ ⁇ ntsen ⁇ atsiyu gas even ⁇ a ⁇ m ⁇ ⁇ e ⁇ uchi ⁇ s ⁇ eda ⁇ , k ⁇ ye glub ⁇ were degassed ⁇ vany d ⁇ them za ⁇ av ⁇ i close the power supply systems.
  • a medium of 10 gas supply to the channel 4 before 3 tank operation see Figures 5-12
  • Deys ⁇ vi ⁇ eln ⁇ is ⁇ lzuya ⁇ aznye le ⁇ uchie gases ( ⁇ s ⁇ benn ⁇ s ⁇ i ⁇ a ⁇ ie, ⁇ ye ⁇ sh ⁇ ⁇ as ⁇ v ⁇ imy in ⁇ e ⁇ uchem s ⁇ ede and sled ⁇ va ⁇ eln ⁇ , leg ⁇ usvaivayu ⁇ sya it ⁇ sle s ⁇ l ⁇ yvaniya ⁇ avi ⁇ atsm ⁇ nny ⁇ ⁇ ave ⁇ n) v ⁇ all ⁇ bome ⁇ a ⁇ m s ⁇ edy ⁇ i ⁇ u ⁇ bulizatsmm udao ⁇ sya ⁇ mi ⁇ va ⁇ ⁇ leblyuschiesya gaz ⁇ vye ⁇ uzy ⁇ i.
  • bay ⁇ asny ⁇ ub ⁇ v ⁇ d 7 us ⁇ ys ⁇ ve s ⁇ glasn ⁇ ⁇ ig.6 snizhae ⁇ ⁇ ntsen ⁇ a- tion le ⁇ uchi ⁇ gaz ⁇ v in ⁇ ekuchey s ⁇ ede on v ⁇ de in nas ⁇ s 1 and bay ⁇ asny ⁇ ub ⁇ v ⁇ d 12 us ⁇ ys ⁇ ve s ⁇ glasn ⁇ ⁇ ig.7 s ⁇ s ⁇ bs ⁇ vue ⁇ zaschi ⁇ e nas ⁇ sa 1 ⁇ k ⁇ zii ag ⁇ essivnymi gas-Zami, is ⁇ lzuemymi for ⁇ bezza ⁇ azhivaniya aquatic water, or volatile organic acids, which can be found in small raw materials used in the food industry
  • bay ⁇ asny ⁇ ub ⁇ v ⁇ d 9 us ⁇ ys ⁇ ve s ⁇ glasn ⁇ ⁇ ig.8, bay ⁇ asny ⁇ ub ⁇ v ⁇ d 13 us ⁇ ys ⁇ ve s ⁇ glasn ⁇ ⁇ mg.9 m bay ⁇ asny ⁇ ub ⁇ v ⁇ d 14 us ⁇ ys ⁇ ve s ⁇ glasn ⁇ ⁇ ig.10 ⁇ bes ⁇ echivayu ⁇ ⁇ chn ⁇ e ⁇ eguli ⁇ vanme ⁇ ntsen ⁇ atsmm gaz ⁇ vy ⁇ ⁇ mmesey in ⁇ ka ⁇ , k ⁇ ye ⁇ s ⁇ u ⁇ ayu ⁇ on v ⁇ d s ⁇ eds ⁇ va 3 consumerization, in the case when, for the purchase of a commercial or for the preparation of recycled products, a degassed fresh fluid medium is used.
  • the device is in accordance with the fig. 25 in the presence of high calcium oxide with the subsequent saturation of the reactive mixture as well as high carbon dioxide;
  • us ⁇ ys ⁇ v ⁇ s ⁇ glasn ⁇ ⁇ ig.9 ⁇ s ⁇ b ⁇ e ⁇ e ⁇ ivn ⁇ ⁇ i zaschi ⁇ e nas ⁇ sa 1 ⁇ ⁇ zim ⁇ mmiches ⁇ i a ⁇ mvnymi ⁇ eagen ⁇ ami is ⁇ lzuemymi for ⁇ e ⁇ m ⁇ imiches ⁇ y a ⁇ ivatsii ⁇ a- ⁇ i ⁇ ma ⁇ e ⁇ ial ⁇ v, ⁇ a ⁇ oil and ⁇ s ⁇ benn ⁇ , ⁇ islye gud ⁇ ny, is ⁇ lzuemye in ⁇ izv ⁇ d- s ⁇ ve bi ⁇ um ⁇ v and ⁇ ezin ⁇ vaya ⁇ sh ⁇ a, ⁇ luchennaya grinding ⁇ d ⁇ v ⁇ eziny ; and the device
  • the most efficient operation is 5 degassing, which is made in the form of a throttled fluid medium.
  • the volatile gas required for initiating a regulated hydraulic flow is sometimes supplied to the system through a (live) power supply. However, more often than not, it sends out through collector 25 to channel 4 in advance
  • ⁇ zam ⁇ nu ⁇ y ⁇ ⁇ etsi ⁇ kulyatsi ⁇ nny ⁇ sis ⁇ ema ⁇ ⁇ e ⁇ l ⁇ snabzheniya v ⁇ avoid gaz ⁇ vy ⁇ ⁇ b ⁇ k in ⁇ ub ⁇ v ⁇ da ⁇ and ⁇ i ⁇ elny ⁇ ba ⁇ a ⁇ eya ⁇ nag ⁇ e ⁇ uyu ⁇ ekuchuyu s ⁇ edu ⁇ bychn ⁇ ⁇ - bi ⁇ ayu ⁇ che ⁇ ez za ⁇ n ⁇ - ⁇ eguli ⁇ uyuschy elemen ⁇ 35 and 34 ⁇ a ⁇ ub ⁇ ⁇ sle ⁇ byaza ⁇ eln ⁇ m glub ⁇ y degassing d ⁇ lni ⁇ eln ⁇ m 29 se ⁇ a ⁇ a ⁇ e gas.
  • ⁇ sli same us ⁇ ys ⁇ v ⁇ s ⁇ glasn ⁇ ⁇ ig.16 is ⁇ lzuyu ⁇ ⁇ a ⁇ a ⁇ a ⁇ for ⁇ e ⁇ m ⁇ b ⁇ ab ⁇ m in ⁇ m including ⁇ dn ⁇ v ⁇ emennym gazi ⁇ vaniem, ⁇ ⁇ b ⁇ ab ⁇ annuyu ⁇ e ⁇ uchuyu s ⁇ edu ⁇ sle d ⁇ s ⁇ a ⁇ chn ⁇ m ⁇ etsm ⁇ ulyatsii che ⁇ ez ⁇ isannuyu sis ⁇ emu ⁇ bychn ⁇ ⁇ bi ⁇ ayu ⁇ with vy ⁇ da nas ⁇ - ca 1 che ⁇ ez d ⁇ lnm ⁇ elny ⁇ e ⁇ e ⁇ uskn ⁇ m ⁇ a ⁇ ub ⁇ 50 za ⁇ n ⁇ - ⁇ eguli ⁇ uyuschim elements ⁇ m 51 and the outlet 38 with the regulating elements 39 and 40, and the separation 29 is
  • the invention in any form of the invention, is practicable through the use of a conventional machine.
  • a clean regulation of gas impurities allows gas to be more efficient. 28 to exclude unrecoverable loss of operation in the process of the destruction of the environment due to the irregular vibrations and periodic impacts caused by it.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Dispersion Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Public Health (AREA)
  • Water Supply & Treatment (AREA)
  • Health & Medical Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • Degasification And Air Bubble Elimination (AREA)
  • Pipeline Systems (AREA)
  • Structures Of Non-Positive Displacement Pumps (AREA)
  • Nitrogen And Oxygen Or Sulfur-Condensed Heterocyclic Ring Systems (AREA)
  • Electric Connection Of Electric Components To Printed Circuits (AREA)
  • Physical Water Treatments (AREA)

Abstract

Le dispositif pour agir sur un flux de milieu fluide comprend une pompe destinée à l'alimentation continue d'un flux fluide destinée au traitement, un canal destiné à faire circuler un flux de milieu fluide à traiter, un moyen de formation d'un tourbillon du flux de milieu fluide à traiter dans ce canal et un moyen de dégazage du flux turbulent. Pour réguler la concentration des additifs gazeux dans les milieux fluides turbulents et afin de réduire le risque d'apparition de bouchons de gaz et de chocs dus à la 'super-cavitation', le moyen de dégazage a été disposé directement après le moyen de formation de tourbillons dans le flux; il est en outre muni d'un élément d'obturation et de régulation servant à l'évacuation contrôlée du gaz émis. Pour réguler avec plus de précision la concentration des additifs gazeux, on peut mettre en oeuvre différentes variantes de rétroaction entre le moyen de dégazage et l'entrée de la pompe ou le moyen de formation de tourbillons, ainsi que l'alimentation dosée du gaz dans le canal avant l'entrée dans le moyen de formation de tourbillons.
PCT/UA2001/000027 2000-08-23 2001-08-01 Dispositif pour agir sur un flux de milieu fluide WO2002016783A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU2001280425A AU2001280425A1 (en) 2000-08-23 2001-08-01 Device for effecting a flow of liquid medium

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
UA2000084987 2000-08-23
UA2000084987 2000-08-23

Publications (3)

Publication Number Publication Date
WO2002016783A1 true WO2002016783A1 (fr) 2002-02-28
WO2002016783A9 WO2002016783A9 (fr) 2003-07-24
WO2002016783A8 WO2002016783A8 (fr) 2003-10-02

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CN (1) CN1214192C (fr)
AU (1) AU2001280425A1 (fr)
RU (1) RU2207449C2 (fr)
WO (1) WO2002016783A1 (fr)

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NO326080B1 (no) 2005-11-11 2008-09-15 Norsk Hydro Produksjon As Arrangement for deling av bronnstrom og separasjonssystem
DE102010047782B3 (de) * 2010-10-08 2012-01-12 Itt Manufacturing Enterprises, Inc. Strömungsgleichrichter für geschlossene Rohrleitungen
CN102427286B (zh) * 2011-11-08 2016-01-20 中国神华能源股份有限公司 一种空心导线的吹扫方法和吹扫系统
EP3044508A4 (fr) 2013-09-13 2017-05-03 Services Pétroliers Schlumberger Procédé et système de combustion d'effluents
BR102015024683B1 (pt) * 2015-09-25 2022-04-26 Cylzer S.A Duto de carbonatação para mesclar um gás e uma bebida e processo de carbonatação
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US3866630A (en) * 1970-12-04 1975-02-18 Fowler Knobbe & Martens Ball canister and system for controlling cavitation in liquids
US4150696A (en) * 1974-03-04 1979-04-24 Max-Planck-Gesellschaft Zur Forderung Der Wissenschaften E.V. Arrangement for suppressing vibrations caused by the flow of a flowable medium
SU1657844A1 (ru) * 1988-12-19 1991-06-23 Куйбышевский политехнический институт им.В.В.Куйбышева Устройство дл перекачки высоков зких жидкостей
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WO1998042987A1 (fr) * 1997-03-24 1998-10-01 Sergei Borisovich Osipenko Dispositif pour influencer l'ecoulement d'un fluide

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RU2207449C2 (ru) 2003-06-27
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WO2002016783A9 (fr) 2003-07-24
CN1214192C (zh) 2005-08-10
WO2002016783A8 (fr) 2003-10-02

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