WO2013009207A1 - Procédé d'ionisation d'air et dispositif de sa mise en oeuvre - Google Patents
Procédé d'ionisation d'air et dispositif de sa mise en oeuvre Download PDFInfo
- Publication number
- WO2013009207A1 WO2013009207A1 PCT/RU2011/000502 RU2011000502W WO2013009207A1 WO 2013009207 A1 WO2013009207 A1 WO 2013009207A1 RU 2011000502 W RU2011000502 W RU 2011000502W WO 2013009207 A1 WO2013009207 A1 WO 2013009207A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- air
- cooled
- vortex tube
- stream
- outlet
- Prior art date
Links
Classifications
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L9/00—Disinfection, sterilisation or deodorisation of air
- A61L9/16—Disinfection, sterilisation or deodorisation of air using physical phenomena
- A61L9/22—Ionisation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C1/00—Magnetic separation
- B03C1/02—Magnetic separation acting directly on the substance being separated
- B03C1/025—High gradient magnetic separators
- B03C1/031—Component parts; Auxiliary operations
- B03C1/033—Component parts; Auxiliary operations characterised by the magnetic circuit
- B03C1/0332—Component parts; Auxiliary operations characterised by the magnetic circuit using permanent magnets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/01—Pretreatment of the gases prior to electrostatic precipitation
- B03C3/014—Addition of water; Heat exchange, e.g. by condensation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/019—Post-treatment of gases
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/02—Plant or installations having external electricity supply
- B03C3/04—Plant or installations having external electricity supply dry type
- B03C3/14—Plant or installations having external electricity supply dry type characterised by the additional use of mechanical effects, e.g. gravity
- B03C3/15—Centrifugal forces
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/34—Constructional details or accessories or operation thereof
- B03C3/36—Controlling flow of gases or vapour
- B03C3/368—Controlling flow of gases or vapour by other than static mechanical means, e.g. internal ventilator or recycler
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/34—Constructional details or accessories or operation thereof
- B03C3/40—Electrode constructions
- B03C3/45—Collecting-electrodes
- B03C3/455—Collecting-electrodes specially adapted for heat exchange with the gas stream
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C9/00—Combinations with other devices, e.g. fans, expansion chambers, diffusors, water locks
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C9/00—Combinations with other devices, e.g. fans, expansion chambers, diffusors, water locks
- B04C2009/001—Combinations with other devices, e.g. fans, expansion chambers, diffusors, water locks with means for electrostatic separation
Definitions
- the invention relates to the field of ionization, ozonation and conditioning of atmospheric air in order to improve its consumer properties and is intended for use in industrial and domestic premises for processing ambient air.
- the invention can also be used for aeroionotherapy of various diseases and the treatment of any gaseous media.
- Ionization of gases or liquids is the formation in the medium of positive and negative ions and free electrons from electrically neutral atoms and molecules by means of energy exposure to them.
- electric, thermal, shock, photon, laser, electrolytic and other types are distinguished.
- the disadvantages of the ionization method due to the balloelectric effect are the insufficiently high degree of ionization of the liquid, the low intensity of saturation of air with ions when mixing the ionized liquid with air, the inability to control the process and achieve the required unipolarity.
- the disadvantages of this method are the low degree of dispersion of the liquid, due to the mechanical dispersion method using the impeller, and the inefficiency of the passive system for mixing liquid with air by sucking air from the atmosphere.
- a low degree of dispersion of the liquid results in a coarsely dispersed liquid, including the presence of a large number of non-ionized medium and large particles that are not trapped by air and do not increase the ionization potential of air.
- the inefficiency of the system of mixing air and liquid leads to an uneven distribution of liquid ions in the air and a decrease in the general unipolarity of the air.
- the humidity of the mixture increases, which in some cases is an undesirable phenomenon.
- the disadvantages of this method are the design complexity, inefficiency of the system of mixing air and ionized liquid, increased air humidity, reduced degree of air ionization due to the neutralization of part of the charges on the walls of the vessel.
- the mixture of air with liquid particles is heterogeneous, which reduces the overall degree of ionization of the air.
- the closest in technical essence to the present invention is a device for treating moist air according to the copyright certificate SU 1483205. When this device is in operation, ionization is achieved by treating moist air using a vortex energy separator (vortex tube) and a high-voltage electric discharge ionizer.
- the high-voltage electric-discharge ionizer is made in the form of a casing placed around a cold flow outlet pipe and connected to a positive electrode and a needle negative electrode located along the axis of the cold stream pipe.
- a vortex tube air is divided into cooled and heated streams. Cooled air with the fog formed in it enters the region of a unipolar corona discharge, where the particles of fog and air molecules acquire a negative charge and under the action of electrostatic forces move to the positive ring electrode, dragging the cooled air along with them.
- ozone molecules are formed from excited oxygen molecules. Ionized and ozonized air is sent to cool the cutter in the metalworking zone.
- the noted drawbacks in the aggregate do not provide a high degree of ionization of the air and reduce its effectiveness.
- the invention is aimed at increasing the degree of ionization of air, providing control over the ionization process, increasing the intensity of air saturation with ions of a dispersed liquid and increasing the efficiency of the ionization process with the simplicity of the method and the device used.
- the problem is solved in the method of ionization of air, including the separation of air into cooled and heated flows in a vortex tube with the condensation of moisture contained in the cooled air stream, and the output of the vortex tube ionized due to the balloelectric effect of the flows of cooled and heated air.
- the cooled ionized stream is divided into several separate jets uniformly distributed along the vortex tube perimeter and directed diametrically opposite jets towards each other to ensure their shock-dynamic interaction, and the magnetic ion pre-acting on the stream of cooled ionized air at the exit of the vortex tube with the force magnetic lines along the air flow in opposite or passing directions.
- the method according to the invention can significantly increase the degree of ionization of air compared with known methods due to the presence of two stages of ionization: dispersion of the liquid in the vortex tube and additional dispersion of liquid droplets in the separator at counter shock dynamic interaction of air jets.
- An increase in the degree of ionization is promoted by a high degree of dispersion of the liquid and mixing of the components of the mixture.
- the intensity of air saturation by ions of a dispersed liquid increases due to intensive mixing of components due to counter shock dynamic interaction of air jets in the mixer with the formation of a finely dispersed ionized mixture with a uniform distribution of ions throughout the mixture.
- the problem is also solved in a device for ionizing air, containing a vortex tube, a pipe for tangential air supply, a swirl, outlet pipes for cooled and heated air flows and a throttle located in the outlet pipe for heated air.
- the vortex tube at the outlet of the cooled air is additionally equipped with a separator with channels evenly distributed along its perimeter, extending into a cylindrical mixer made in the form of a cavity on the outside of the separator, while the channel outlet openings are diametrically opposed in pairs.
- the channels are substantially L-shaped, with the ratio of the total area of the channels of the separator to the living area of the outlet pipe of the cooled air stream being 1 / 2.5-1 / 3.0.
- outlet pipe for the cooled air can be equipped with two annular permanent magnets covering the pipe, mounted on the end planes of the swirl with the possibility of their rearrangement to change the direction of the magnetic field relative to the flow of cooled air.
- FIG. 1 schematically shows a device for ionizing air according to the present invention, a view in longitudinal section;
- FIG. 2 is a section along AA in FIG. 1.
- a device for implementing the air ionization method in accordance with the present invention is a vortex tube consisting of a housing 1, a swirl 2, a throttle 3, a pipe 4 for tangential air supply to the swirl 2, a cooled air outlet 5 and a heated air outlet 6.
- the inner surface of the casing of the vortex tube 1 is made of non-porous material that does not conduct electric current, for example, fluoroplastic, polystyrene, polyvinyl, organic glass, etc. with a roughness of not more than Ra 0.8.
- the inner surfaces of other parts of the device are made of the same material. All other surfaces and other parts of the device can be made of any material.
- the housing has a cylindrical or conical shape.
- the swirl 2 is a cochlear supercharger that swirls the air flow and feeds it along a helical line into the vortex tube body.
- the throttle 3 is intended, firstly, for the selection of heated air and, secondly, for regulating its flow rate, and, accordingly, the flow rate of chilled air.
- the vortex tube provides energy separation of air into cooled and heated flows. Separation is due to the Rank-Hills effect.
- the heated stream moves along the periphery of the vortex tube, and the cooled stream moves along the pipe axis in the opposite direction.
- At the end of the pipe there is a reflector 7, which ensures the rotation of the flow and the outlet of heated air through the peripheral holes 8 into the pipe 6.
- the chilled air outlet pipe 5 is provided with two permanent ring magnets 9 and 10, covering said pipe.
- the magnets are mounted on the end planes of the swirl 2 on its outer sides.
- the magnets 9 and 10 are mounted with the possibility of their rearrangement, so that the direction of the magnetic field is either oncoming or passing relative to the flow of cooled air.
- Coercive magnetic field strength and dimensions magnets are determined by the parameters of the air flow (flow, pressure, speed), the size of the vortex tube and are selected experimentally.
- the device at the outlet of the cooled air is equipped with a separator 11, dividing the air flow into separate jets.
- channels 12 are made in the separator, for example, of an L-shaped shape uniformly distributed around the perimeter of the separator 1 1.
- the channels 12 exit into a cylindrical mixer 13, which is a cavity on the outside of the separator.
- the outlet openings of the channels 12 are arranged in pairs diametrically opposite (Fig. 2)
- F K is the total area of the channels
- F 0B is the living section area of the cooled outlet pipe air flow.
- the method is as follows.
- the pipe 4 and the swirl 2 in the casing 1 of the vortex tube serves moist air (humidity more than 30%) depending on the required output parameters of humidity and ionization potential.
- the air flow in the vortex tube is intensively swirled at high peripheral speed, turbulized and divided into two flows: heated (peripheral) and cooled (axial). Both flows move towards each other, which increases turbulization.
- the stream of chilled air at the exit of the vortex tube is treated with a magnetic field with the location of the magnetic lines of force along the air stream in the opposite or passing directions.
- One or another direction of the magnetic field is provided by the installation of magnets 9 and 10.
- FIG. 1 shows one of the options for installing magnets with an indication of their poles. With this arrangement of the poles of the magnets, the magnetic field will coincide in direction with the air flow. When the poles are reversed, the magnetic field will be directed towards the air flow.
- the cooled air After magnetic treatment, the cooled air enters the L-shaped channels 12 of the separator 1 1. Since the total area of the channels 12 is 2.5-3 times less than the living area of the chilled air outlet 5, the air velocity in the channels and at the outlet of them increases . High-speed jets of air enter the mixer 13, made in the form of a cavity on the outside of the separator.
- the remaining liquid droplets are additionally dispersed due to the kinetic shock-dynamic interaction of air jets.
- the number of ions increases (due to secondary impact ionization) and their density in the air stream, as a result of which the degree of air ionization increases.
- air and charged particles are actively mixed with the achievement of a high uniformity of the distribution of ionized particles in the air.
- a high degree of dispersion of liquid droplets and air ionization is provided due to the above optimal ratio of the total area of the channels in the separator and the living area of the chilled air pipe.
- the above ratio allows for a high speed of air jets without a significant increase in the resistance of the channels and the total pressure in the device. So, with a ratio of less than 2.5, the speed of the air jets decreases, the process of dispersing liquid droplets becomes ineffective due to a decrease in the kinetic energy of the air jets, and with a ratio of more than 3.0, the resistance of the channels and the pressure in the device increase, increasing the energy consumption for air ionization.
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- Health & Medical Sciences (AREA)
- Epidemiology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Animal Behavior & Ethology (AREA)
- General Health & Medical Sciences (AREA)
- Public Health (AREA)
- Veterinary Medicine (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
Le procédé d'ionisation d'air comprend la séparation de l'air en des flux d'air refroidi et chauffé dans le tube tourbillonnaire assurant la condensation de l'humidité contenue dans le flux d'air refroidi et l'évacuation hors le tube tourbillonnaire des flux d'air ionisés par l'effet balloélectrique. Le flux ionisé refroidi à la sortie provenant du tube tourbillonnaire est soumis à l'effet d'un champ magnétique puis séparé en plusieurs flux isolé, puis les flux opposés diamétralement sont dirigés les uns contre les autres en assurant leur impact de choc dynamique. Le dispositif pour mettre en oeuvre ce procédé comprend un tube tourbillonnaire, une tubulure d'amenée tangentielle d'air, un dispositif de formation de tourbillons, une tubulure de sortie des flux d'air refroidi et chauffé et le papillon disposé dans la tubulure de sortie d'air chauffé. A la sortie d'air refroidi le tube tourbillonnaire est doté d'un séparateur avec des canaux répartis régulièrement à sa périphérie et donnent sur un mélangeur cylindrique qui se présente comme des cavités à la surface externe du séparateur, les orifices de sortie des canaux étant disposés deux par deux et opposés diamétralement.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/RU2011/000502 WO2013009207A1 (fr) | 2011-07-08 | 2011-07-08 | Procédé d'ionisation d'air et dispositif de sa mise en oeuvre |
RU2013158077/15A RU2576513C2 (ru) | 2011-07-08 | 2011-07-08 | Способ ионизации воздуха и устройство для его осуществления |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/RU2011/000502 WO2013009207A1 (fr) | 2011-07-08 | 2011-07-08 | Procédé d'ionisation d'air et dispositif de sa mise en oeuvre |
Publications (1)
Publication Number | Publication Date |
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WO2013009207A1 true WO2013009207A1 (fr) | 2013-01-17 |
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ID=47506287
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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PCT/RU2011/000502 WO2013009207A1 (fr) | 2011-07-08 | 2011-07-08 | Procédé d'ionisation d'air et dispositif de sa mise en oeuvre |
Country Status (2)
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RU (1) | RU2576513C2 (fr) |
WO (1) | WO2013009207A1 (fr) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109737627A (zh) * | 2018-12-27 | 2019-05-10 | 西北工业大学 | 无热端阀门防堵塞高效涡流管 |
US11577192B2 (en) * | 2018-09-14 | 2023-02-14 | Washington State University | Vortex tube lined with magnets and uses thereof |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SU517191A1 (ru) * | 1974-09-12 | 1976-06-05 | Казанский ордена Трудового Красного Знамени авиационный институт им. А.Н.Туполева | Гидроаэроионизатор |
SU1084558A1 (ru) * | 1981-05-29 | 1984-04-07 | Gajdukov Aleksej A | Система кондиционировани воздуха |
SU1483205A1 (ru) * | 1987-06-27 | 1989-05-30 | Институт общей и неорганической химии им.Н.С.Курнакова | Устройство дл обработки влажного воздуха |
JP2000325727A (ja) * | 1999-05-18 | 2000-11-28 | Nikko Sohonsha:Kk | 負イオン発生方法および負イオン発生装置、並びに負イオン発生装置における給水タンクおよび自動給水装置 |
JP2001321625A (ja) * | 2000-05-19 | 2001-11-20 | Matsushita Seiko Co Ltd | 負イオン発生装置 |
-
2011
- 2011-07-08 RU RU2013158077/15A patent/RU2576513C2/ru not_active IP Right Cessation
- 2011-07-08 WO PCT/RU2011/000502 patent/WO2013009207A1/fr active Application Filing
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SU517191A1 (ru) * | 1974-09-12 | 1976-06-05 | Казанский ордена Трудового Красного Знамени авиационный институт им. А.Н.Туполева | Гидроаэроионизатор |
SU1084558A1 (ru) * | 1981-05-29 | 1984-04-07 | Gajdukov Aleksej A | Система кондиционировани воздуха |
SU1483205A1 (ru) * | 1987-06-27 | 1989-05-30 | Институт общей и неорганической химии им.Н.С.Курнакова | Устройство дл обработки влажного воздуха |
JP2000325727A (ja) * | 1999-05-18 | 2000-11-28 | Nikko Sohonsha:Kk | 負イオン発生方法および負イオン発生装置、並びに負イオン発生装置における給水タンクおよび自動給水装置 |
JP2001321625A (ja) * | 2000-05-19 | 2001-11-20 | Matsushita Seiko Co Ltd | 負イオン発生装置 |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US11577192B2 (en) * | 2018-09-14 | 2023-02-14 | Washington State University | Vortex tube lined with magnets and uses thereof |
CN109737627A (zh) * | 2018-12-27 | 2019-05-10 | 西北工业大学 | 无热端阀门防堵塞高效涡流管 |
Also Published As
Publication number | Publication date |
---|---|
RU2013158077A (ru) | 2015-08-20 |
RU2576513C2 (ru) | 2016-03-10 |
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