+

WO1993010404A1 - Ultrasonic atomising, cooling and air-conditioning - Google Patents

Ultrasonic atomising, cooling and air-conditioning Download PDF

Info

Publication number
WO1993010404A1
WO1993010404A1 PCT/AU1992/000619 AU9200619W WO9310404A1 WO 1993010404 A1 WO1993010404 A1 WO 1993010404A1 AU 9200619 W AU9200619 W AU 9200619W WO 9310404 A1 WO9310404 A1 WO 9310404A1
Authority
WO
WIPO (PCT)
Prior art keywords
air
atmosphere
liquid
ultrasonic energy
evaporation
Prior art date
Application number
PCT/AU1992/000619
Other languages
French (fr)
Inventor
Edison Miraziz
Jan Jeltes
Original Assignee
Edison Miraziz
Jan Jeltes
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 Edison Miraziz, Jan Jeltes filed Critical Edison Miraziz
Publication of WO1993010404A1 publication Critical patent/WO1993010404A1/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05BSPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B17/00Apparatus for spraying or atomising liquids or other fluent materials, not covered by the preceding groups
    • B05B17/04Apparatus for spraying or atomising liquids or other fluent materials, not covered by the preceding groups operating with special methods
    • B05B17/06Apparatus for spraying or atomising liquids or other fluent materials, not covered by the preceding groups operating with special methods using ultrasonic or other kinds of vibrations
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS 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
    • A61L9/00Disinfection, sterilisation or deodorisation of air
    • A61L9/015Disinfection, sterilisation or deodorisation of air using gaseous or vaporous substances, e.g. ozone
    • A61L9/04Disinfection, sterilisation or deodorisation of air using gaseous or vaporous substances, e.g. ozone using substances evaporated in the air without heating
    • A61L9/12Apparatus, e.g. holders, therefor
    • A61L9/122Apparatus, e.g. holders, therefor comprising a fan
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F3/00Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
    • F24F3/12Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
    • F24F3/14Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/70Efficient control or regulation technologies, e.g. for control of refrigerant flow, motor or heating
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency

Definitions

  • This invention relates to the control of the vapour content and temperature in various gaseous atmospheres, and although not limited to any particular application the invention is most particularly directed to air conditioning, medical and chemical processing procedures requiring such control.
  • Air may be cooled by evaporation which is known from the typical evaporative air conditioning apparatus .
  • the typical evaporative air conditioner provides a wanted cooling affect which is balanced against the generally unwanted increase in humidity (effectiveness of cooling being less as ambient relative humidity approaches 100%), while on the other hand, the wanted increase in humidity in a greenhouse environment provides unwanted reduction in temperature which typically is compensated by providing a further heating means and fan for dispersing the heated water vapour produced.
  • Cooling towers use evaporative cooling techniques and are found to operate more efficiently, when, rather than relying on air passing over the heat exchanger portion of the tower,, a fine spray of water is entrained into the inlet air stream.
  • This arrangement lowers the dry bulb temperature and enhances the air side heat transfer due to droplet vaporisation, without wetting the heat exchanger surface and reducing or eliminating problems with algae and other contaminate build-up on the air side heat exchanger surfaces. It is also known that heat transfer co-efficients increase with decreasing flow velocity and also decreasing temperature difference between the surface and the air flow.
  • Cavitation is known to have a nucleation phase, wherein, cavitation nuclei comprising gas pockets trapped in cracks/ crevices, hydrophobia impurities or icrobubbles stabilised in solution against total dissolution, are activated, and, a second growth phase, wherein microbubbles are formed and expand from the stabilised nuclei.
  • the uses of the phenomenon of cavitation are well known and include their use as a humidifier wherein an ultrasonic transducer submerged in a reservoir of water promotes the ejection of water molecules from the body of water at its surface interface.
  • Electro-aerodynamic atomisation is a similar means of ato isation to that of the action of an electrostatic field. These processes cause atomisation not vaporisation. Electro- aerodynamic atomisation results from the application of non- static electrical fields to a liquid droplet laden atmosphere. Atomisation results from the opposing effect of the cohesive surface tension forces and the disruptive forces created by the repulsive forces between like charges at molecular level, where it is known, that the electric field necessary to cause disruption in the liquid mass increases as the liquid surface tension increases. In electric fields a droplet of water forms at the crest of the electric waves and it is observed that there is preferential migration of charges to surface protuberances caused by the distortion of the droplets by the electric field. New smaller droplets are formed from the crest of the surface waves, since the maximum concentration of electric charges and minimum value of surface tension will occur at thes-e areas.
  • a further atomisation process results from vibrating an element over which a controlled depth of fluid is passed (so called sonicating thin film liquids) from which small droplets of liquid are projected.
  • the viscosity of the liquid, the depth of the film, the frequency and amplitude of the vibrating element all determine the size of the droplet produced.
  • the creation of an atmosphere using a working gas carrying water droplets past an ultrasonic energy emitter which imparts its energy thereon can very efficiently vaporise droplets in the working gas.
  • One of the very useful uses of this process is cooling and humidification effects, as described previously for evaporative air-conditioners.
  • the vaporisation, of water and other liquids which are carried, entrained, suspended or distributed within a working gaseous atmosphere by ultrasonic transducers, enables the temperature and humidity of that gaseous atmosphere to be controlled by the degree of application of the ultrasonic energy.
  • a transducer means to produce this effect requires that there be a controllable production of mechanical acoustic energy transferred as efficiently as possible to the atmosphere surrounding the liquid in droplet form carried by that atmosphere. It- is understood that vaporisation occurs as a result of creating suitable rarefication and compression waveforms in the atmosphere surrounding small liquid droplets such as to distort the droplet shape and impart sufficient energy so as to overcome the cohesive forces of the liquid molecules.
  • transducer apparatus A variety of transducer apparatus are considered suit ⁇ able for this purpose, typically but not exclusively, having magneto, electrostri ⁇ tive or peizostrictive characteristics. That is the transducer material changes its dimensions due to magnetization, electrostatic or electric forces applied to the material. These forces may produce linear and volumetric changes in dimensions in the transducer material at a variety of frequencies.
  • Typical magnetostrictive materials are iron, nickel, cobalt, ferrites, and alloys thereof, eg. Ni-Fe as well as ceramic compositions and exhibit a variety of Joule magnetostriction (length change) quantities as a function of the applied magnetic field strength.
  • the electromagnetic coupling factor, k, of these magneto strictive materials is affected by eddy current loss factors (reduced by considering construction, geometry) and their polarization state and stress configuration as well as the materials heat capacity, thermal conductivity and both static and dynamic tensile strength and the efficiency of the application of the requisite magnetic flux density to the material under predetermined mechanical stresses.
  • magnetostrictive transducers are non-linear, however, in a polarized state (achieved by the use of permanent magnets, direct current or operation at remanance) they are linear (i.e. piezomagnetic) .
  • Properly arranged magnetostrictive transducers can achieve radiated ultrasonic (acoustic) powers up to several kilowatts with efficiencies of 50%, however, operating frequencies are usually limited to frequencies below 100 kHz.
  • electrostatic transducers comprise a fixed conductive plate having one electric charge and a moveable conductive plate (diaphragm) to which is applied a variable (amplitude) attractive or repulsive electric charge.
  • the resulting force on the diaphragm produces a mechanical energy which is transferred to the surrounding atmosphere.
  • Typical piezoelectric transducers use crystals or polycrystalline ceramic materials and in their simplest form are arranged to form an expansion-contraction region along the axis between the electrodes when an alternating voltage, also typically a very low current is applied. These materi ⁇ als may be operated in various modes, two of those modes be ⁇ ing the 33-mode where the stress, strain and electric field are in the same direction and the 31-mode where the stress and strain are in the same direction but orthogonal to the electric field. For the example of piezoelectric ceramics their properties vary as a function of time, static stress, stress cycling and electric field strength.
  • the electro magnetic coupling factor, k, of these materials is an important measure of the effectiveness of the energy conversion mechanism and is a function of mutual elastic and dielectric energy density, elastic self energy density and dielectric self energy density.
  • a benefit of piezo electric transducers of the polymeric film type is the adaptability of their physical form to the shape required in the application. They are pliant, flexible, tough and light weight. These materials are based on a polyvinylidene flouride (PVDF) which show typically the highest piezo and pyroelectric activities of most polymers and is capable of being produced in a variety of thickness and configurations of shape and active area.
  • PVDF polyvinylidene flouride
  • Additional characteristics of this material comprise the ability to produce patterned transducer arrays, high piezoelectric sensitivity in planar and hydrostatic modes g which can produce volts into 10 ohm resistance, broad band
  • a method for atomizing a liquid at temperatures and pressures below the boiling point of the liquid comprises the steps of; a) providing a working atmosphere comprising a mixture of gas and suspended liquid droplets, and, b) subjecting said working atmosphere to ultrasonic energy which reduces the size of said liquid droplets .
  • a method for converting liquid into a vapour at temperatures and pressures below the boiling point of the liquid (evaporation) comprises the steps of; a) providing a working atmosphere that is to be cooled, comprising a mixture of gas and suspended liquid droplets, and, b) subjecting said working atmosphere to ultrasonic energy which partially evaporates said liquid droplets, thereby inducing absorption of latent heat of evaporation from the said working atmosphere thereby cooling the atmosphere.
  • a method for converting liquid into a vapour at temperatures and pressures below the boiling point of the liquid (evaporation) comprises the steps of; a) providing a working atmosphere comprising a mixture of gas and suspended liquid droplets, and, b) subjecting said working atmosphere to ultrasonic energy which evaporates said liquid droplets, thereby inducing absorption of latent heat of evaporation from the said working atmosphere thereby cooling the atmosphere.
  • a method of evaporation according to the method described above comprises the further step of c) circulating a portion of the working atmosphere so as to be subjected to step b) again and thereby further cool the working atmosphere.
  • a method of evaporation comprising the further step of g) using a predetermined ultrasonic energy frequency and amplitude which selectively vaporizes a selected liquid.
  • a method of conditioning air comprises the steps of; a) creating a flow of air through a passage, b) distributing droplets of liquid in said flowing air, c) applying ultrasonic energy into said flowing air containing liquid droplets, and thereby inducing absorption of latent heat of evaporation from said flowing air to cool said air.
  • a further aspect of the invention is an air-conditioning apparatus for conditioning an air atmosphere comprising an air flow passage for passing an air atmosphere therethrough, liquid droplet distribution means to distribute droplets of liquid in said air flow, and an ultrasonic energy emitter means arranged and adapted so as to emit ultrasonic energy into said air flow 'passage containing air and liquid droplets to thereby induce absorption of latent heat of evaporation from said flowing air to cool said air.
  • a bacterial reduction apparatus comprising an air flow passage for passing an air atmosphere therethrough, liquid droplet distribution means to distribute droplets of liquid containing bacteriological matter into said air flow, and an ultrasonic energy emitter means arranged and adapted so as to emit ultrasonic energy into said air flow passage containing air and said liquid droplets o thereby evaporate said liquid droplets destroying said bacteriological matter, inducing absorption of latent heat of evaporation from the said air and cooling the air and in combination reducing the incidence of live bacteriological matter in said air/vapour atmosphere passing from said flow passage.
  • a bacterial reduction apparatus comprises an ultrasonic energy emitter adapted to have its field of effect directed to the internal volume of a pipe containing a working atmosphere that is to be cooled comprising a mixture of gas and liquid droplets containing bacteriological matter, and, an ultrasonic energy emitter means arranged and adapted so as to emit ultrasonic energy into said working atmosphere to thereby evaporate said liquid droplets to induce an absorption of the latent heat of evaporation from the said working atmosphere thereby cooling the atmosphere and reducing the incidence of live bacteriological matter in said air/vapour atmosphere passing from said flow passage.
  • Fig. 1 depicts a schematic of an air conditioning system incorporating the method and apparatus of the invention
  • Fig. 2 depicts a schematic of an air-conditioning apparatus using a heat exchanger means incorporating the method and means of the invention
  • Fig. 3 depicts a schematic of a closed pipe work system incorporating the method and means of the invention.
  • incoming atmosphere 10 is a mixture of air and water vapour to which is added by ato ization means 11, a spray of water droplets 12 which can be carried by the air flow denoted by arrows 13.
  • the air, vapour, and water droplet mixture is directed into an air flow passage 14 by a negative pressure fan 15 (located coaxial with the air flow passage) .
  • a negative pressure fan 15 located coaxial with the air flow passage
  • an ultrasonic energy emitter means 16 arranged to direct its energy emission into the air flow passage.
  • the physical configuration of such an energy emitter means could take many forms.
  • the emitter is formed integral with a grid like form work 17 located in the air flow path within the air flow passage.
  • the emitter is required to create an environment in the air, vapour, water droplet air flow, which leads to the evaporation of the water droplets.
  • piezo film 18 is adhered to the grid like frame work 17.
  • the framework is designed to minimize friction to the air flow and to space the active (piezo film) ultrasonic emission areas within the air flow such that the field in which evaporation takes place is confined to the air flow passage in the vicinity of the grid like framework.
  • the framework may be arranged as an array of passages 19 and 20 in which the piezo film is placed in passageways 19 such that its field of effect envelopes the volume of the passageway.
  • Other passages 20 for communicating dry air to be cooled are arranged to lie orthogonal to the first said passages as in a heat exchanger configuration.
  • the other passages can act as the dry side of the heat exchanger and as latent heat of evaporation is drawn from the atmosphere within the first of said passages, heat will also be drawn from the other passages.
  • the air 20 flowing in the dry side of the heat exchanger looses heat and its temperature reduces.
  • This arrangement may be suitable for use in an air-conditioning apparatus to provide cool dry air to which can be added moisture if desired.
  • a means to condense the acquired water vapour 21 may be used to reduce the vapour pressure (relative humidity) of the air flow exiting from the first of said air flow passages. Since condensing water releases its latent heat of phase change, this heat if not used by the apparatus, may be released to the atmosphere and the condensed water 22 used in the evaporation process as a source of the water to be atomised. Typically, also, the condensed water is relatively cool and assists the cooling effect caused first by the atomised spray vaporising and then by the further vaporisation induced by the ultrasonic means.
  • moisture loaded air flow produced by the ultrasonic emitters can be injected into the wet side of a heat exchanger configuration wherein, upon condensation of the water in the air flow passages, latent heat of phase change is drawn from the air flow on the dry side of the heat exchanger.
  • FIG. 3 relates to a closed application of the process of the invention, although self contained in its configuration, this particular arrangement may be used to enhance the operation of a conventional open ended air conditioning system.
  • Fig. 3 depicts a cross-section of a single bore pipe 23 having an internal wall 24 and an internal atmospheric condition A, initially comprising atomized liquid in gaseous suspension.
  • the atomised liquid may be water, alcohol or other suitable liquid which has a change of state temperature at or below the pressure internal of the pipe, while the working or transport, gas used therein may be air, an inert gas or other suitable gas typically although not necessarily at atmospheric or lower pressure.
  • an ultrasonic energy emitter 25 preferably of the piezo film type.
  • a further embodiment not shown may provide for a portion of the pipe to be constructed of a suitable transducer material.
  • the film may be located in a grid like configuration within the pipe and/or the film may still be able to exert its field of effect into the pipe although it is attached or adhered to the outside of the pipe. It the latter case it could be that the mechanical resonance of the pipe could be chosen to match the ultrasonic frequencies required for the purposes of advantageously af ⁇ fecting the contents of the pipe.
  • the internal surface of the pipe may be advantageously shaped or profiled so as to promote the desired effect occurring within the pipe .
  • the atmosphere condition A When the piezo film is energized in a required zone of the pipe, the atmosphere condition A will change to a state Al, in which the liquid droplets suspended in the pipe volume are evaporated. This process draws latent heat of change of state from the gas atmosphere Al in the pipe as well as the region outside the pipe or as in this embodiment atmosphere B which exist outside the pipe.
  • the efficiency of this arrangement being of course dependant on the heat transfer characteristics of the pipe as determined by its material and surface profile and the characteristics of the region external of the pipe.
  • vaporised atmosphere Al is pumped to a location 26 for condensation and then for insertion again into the atmosphere at A and the latent heat of phase change from vapour to liquid occurring at 26 may be drawn off for heating purposes or vented to atmosphere.
  • Fig. 3 also depicts schematically the disposition of an atmosphere B surrounding the pipe which may advantageously made a part of the air flow of an open ended air conditioning apparatus.
  • the atmosphere B will be in the vicinity of the pipe and leave the vicinity at a cooler temperature because there will be. a loss of energy as the latent heat of change of state taking place within the pipe will be drawn from the passing air flow denoted as atmosphere B.
  • gas, liquid mixture used in the pipe could be different from the typically air/water mixture used external to the pipe and advantageously so when the pipe mixture is capable of producing temperature reduc ⁇ tions at temperatures below O'C.
  • the air/water mixture of the atmosphere B can be controlled in respect to its temperature and .vapour pressure by the controlled action of the piezo film both within and external to the pipe. Control is possible by way of varying one or more of a number of driving forces applied to the piezo film. These forces include the frequency of operation, the level of the signal applied and the duration of its application. Therefore, although there may be a number of controlled variables, it is possible using appropriate control means, to make it easy for the operator to adjust one indicator for temperature and one indicator for relative humidity.
  • the embodiment schematically depicted in Figs. 2 and 3 may form the basis for an arrangement of a plurality of such pipes, arranged so that a large volume of gas, liquid or atmosphere may be drawn past the pipes in quantities sufficient to control the temperature and humidity of larger volumes of atmosphere as may be required in domestic and industrial environments.
  • the environment in the vicinity of the cooling coils of a typical Reverse Cycle Air- Conditioner (RC A/C) may be controlled using the field of an ultrasonic emitter.
  • piezo film as an example of the ultrasonic emitter, could be placed adjacent or upon the cooling coils of the RC A/C and it will be found that there will be beneficial effect by the improvement of the efficiency of heat transfer.
  • any liquid contained within the atmosphere passing within the field of effect of the emitter will be evaporated thus reducing its temperature of the atmosphere adjacent its placement.
  • a further embodiment of the invention not depicted is that of adjusting the frequency and/or amplitude of the ultrasonic energy to selectively vaporize a liquid which has been entrained by any suitable atomisation means into an atmosphere as previously described.
  • any suitable atomisation means such as any suitable atomisation means.
  • the resulting atmosphere may be used in a particular chemical process to advantage as a result of the vaporization of the desired liquid.
  • the vaporisation process takes place at the entrance to the evaporator, which, typically comprises an isenthalpic nozzle arranged to create a two phase (liquid/vapour) atmosphere which is cooled in the process but the droplets do not always totally vaporise.
  • the evaporator typically comprises an isenthalpic nozzle arranged to create a two phase (liquid/vapour) atmosphere which is cooled in the process but the droplets do not always totally vaporise.
  • ultrasonic induced vaporisation with little extra energy expenditure to create the ultrasonic environment, will increase the amount of vaporisation, enhance the cooling effect of the evaporator and increase the quantity of heat drawn from the surroundings of the evaporator thus further cooling the enclosed refrigerator space. This may occur by way of the action of ultrasonic energy on the gaseous atmosphere itself and may advantageously induce sympathetic resonant vibrations in the mechanical structure of the evaporator apparatus.
  • the parameters of the environment required to produce this desired result comprise a suitable field flux of ultrasonic energy at an appropriate frequency of operation and an appropriate exposure period of the mixture within the field.
  • a variety of applications of this aspect of the invention are described herein.
  • One example is the use of such an environment in the operation of a cooling tower as is typically used in commercial air-conditioning plants.
  • the incidence of Legionella bacteria in its many forms has been cause for great concern to health officials. Therefore, it will be clearly apparent that, either the direct treatment of the water towers' water reservoir, or, treatment of the environment about the water tower cooling apparatus would be advantageous in this regard.
  • Placement of a suitable ultrasonic emitter in one or more of these locations would be beneficial by a) reducing or eliminating harmful bacteriological organisms and b) reducing the temperature by inducing further vaporisation.
  • domestic hot water systems may be kept at lower temperatures than are typically the case.
  • hot water services are kept at temperatures greater than 60"C for the express reason of providing an environment non-conducive to unwanted bacteriological growth, however, a lower temperature say between 50 * C and 55 * C would still suffice for domestic hot water purposes.
  • the thermostatically controlled hot water service temperature may be kept at more economical and safer temperatures.
  • a bacteriological barrier as generally proposed herein could also be adapted to fit at the outlets of air-condition ⁇ ing systems of any type, so that, the air, vapour, and suspended moisture mixture of the gasses being supplied to the room, operating theatre, etc, can be adequately treated to eliminate or reduce the level of airborne contaminants which would otherwise possibly be harmful to the room oc ⁇ cupants.

Landscapes

  • Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Veterinary Medicine (AREA)
  • Animal Behavior & Ethology (AREA)
  • General Health & Medical Sciences (AREA)
  • Public Health (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Epidemiology (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

The process of evaporating water to cool the surrounding atmosphere is well known. The invention proposes a method and apparatus (16) to use ultrasonic energy to vaporize liquid (22) which is entrained in an atmosphere (10) in the form of droplets (12). The creation of such an atmosphere provides a most conducive environment for such a process. In one example of the apparatus the ultrasonic energy is produced by a piezo electric film (18) arranged on a framework (17) through which the atmosphere is drawn by a fan (15). Judicious placement of such an apparatus allows for efficient operation of evaporative (21) and reverse cycle heat pump air- conditioning systems as well as refrigeration systems inclusive of the vapour compression and absorption types. With the apparatus of the invention selective vaporization of certain fluids will also improve particular chemical processes. Furthermore, the process of vaporization of fluid droplets in a gaseous atmosphere will also advantageously destroy bacteria which may be within the fluid.

Description

ULTRASONICATOMISING, COOLINGANDAIR-CONDITIONING
This invention relates to the control of the vapour content and temperature in various gaseous atmospheres, and although not limited to any particular application the invention is most particularly directed to air conditioning, medical and chemical processing procedures requiring such control.
BACKGROUND
When water changes state from a liquid to a vapour, an amount of heat energy known as the latent heat of change of state is absorbed from the surrounding atmosphere.
Air may be cooled by evaporation which is known from the typical evaporative air conditioning apparatus . On one hand the typical evaporative air conditioner provides a wanted cooling affect which is balanced against the generally unwanted increase in humidity (effectiveness of cooling being less as ambient relative humidity approaches 100%), while on the other hand, the wanted increase in humidity in a greenhouse environment provides unwanted reduction in temperature which typically is compensated by providing a further heating means and fan for dispersing the heated water vapour produced.
Cooling towers use evaporative cooling techniques and are found to operate more efficiently, when, rather than relying on air passing over the heat exchanger portion of the tower,, a fine spray of water is entrained into the inlet air stream. This arrangement lowers the dry bulb temperature and enhances the air side heat transfer due to droplet vaporisation, without wetting the heat exchanger surface and reducing or eliminating problems with algae and other contaminate build-up on the air side heat exchanger surfaces. It is also known that heat transfer co-efficients increase with decreasing flow velocity and also decreasing temperature difference between the surface and the air flow.
It is also known to operate an ultrasonic transducer which is submerged in a reservoir of water to induce pressure pulsations of acoustic or hydrodynamic fields which can lead to the pressure in the water being lower than the saturated vapour pressure and thus create a condition suitable for the onset of cavitation. This type of apparatus is typically used for ultrasonic cleaning.
In water, cavitation arises only at considerable pressure reductions which are quantified by the excess of hydrostatic pressure over the saturated vapour pressure, while in other liquids, such as cryogenic liquids cavitation arises more readily with only slight pressure pulsations. The reason is not only the difference between the static pressure and pressure of saturated vapours, but, cryogenic liquids have smaller values of surface tension than water.
Cavitation is known to have a nucleation phase, wherein, cavitation nuclei comprising gas pockets trapped in cracks/ crevices, hydrophobia impurities or icrobubbles stabilised in solution against total dissolution, are activated, and, a second growth phase, wherein microbubbles are formed and expand from the stabilised nuclei.
The uses of the phenomenon of cavitation are well known and include their use as a humidifier wherein an ultrasonic transducer submerged in a reservoir of water promotes the ejection of water molecules from the body of water at its surface interface.
It is also known to apply electrostatic fields to a region containing liquid droplets which creates the condition of individual water droplets accumulating mutually exclusive charges at opposite sides which interact with the attractive forces between the molecules of the liquid through surface tension and attractive forces between the charged liquid and the charged electrodes creating the electrostatic field which in combination creates a tendency for reducing droplet size in the field. This effect, however, is only significant when the atmosphere carrying the liquid (water for example) is moving at a rate greater than 30 m/s.
Electro-aerodynamic atomisation is a similar means of ato isation to that of the action of an electrostatic field. These processes cause atomisation not vaporisation. Electro- aerodynamic atomisation results from the application of non- static electrical fields to a liquid droplet laden atmosphere. Atomisation results from the opposing effect of the cohesive surface tension forces and the disruptive forces created by the repulsive forces between like charges at molecular level, where it is known, that the electric field necessary to cause disruption in the liquid mass increases as the liquid surface tension increases. In electric fields a droplet of water forms at the crest of the electric waves and it is observed that there is preferential migration of charges to surface protuberances caused by the distortion of the droplets by the electric field. New smaller droplets are formed from the crest of the surface waves, since the maximum concentration of electric charges and minimum value of surface tension will occur at thes-e areas.
A further atomisation process results from vibrating an element over which a controlled depth of fluid is passed (so called sonicating thin film liquids) from which small droplets of liquid are projected. The viscosity of the liquid, the depth of the film, the frequency and amplitude of the vibrating element all determine the size of the droplet produced. However, it is proposed that the creation of an atmosphere using a working gas carrying water droplets past an ultrasonic energy emitter which imparts its energy thereon can very efficiently vaporise droplets in the working gas. One of the very useful uses of this process is cooling and humidification effects, as described previously for evaporative air-conditioners.
The vaporisation, of water and other liquids which are carried, entrained, suspended or distributed within a working gaseous atmosphere by ultrasonic transducers, enables the temperature and humidity of that gaseous atmosphere to be controlled by the degree of application of the ultrasonic energy.
A transducer means to produce this effect requires that there be a controllable production of mechanical acoustic energy transferred as efficiently as possible to the atmosphere surrounding the liquid in droplet form carried by that atmosphere. It- is understood that vaporisation occurs as a result of creating suitable rarefication and compression waveforms in the atmosphere surrounding small liquid droplets such as to distort the droplet shape and impart sufficient energy so as to overcome the cohesive forces of the liquid molecules.
A variety of transducer apparatus are considered suit¬ able for this purpose, typically but not exclusively, having magneto, electrostriσtive or peizostrictive characteristics. That is the transducer material changes its dimensions due to magnetization, electrostatic or electric forces applied to the material. These forces may produce linear and volumetric changes in dimensions in the transducer material at a variety of frequencies.
Typical magnetostrictive materials are iron, nickel, cobalt, ferrites, and alloys thereof, eg. Ni-Fe as well as ceramic compositions and exhibit a variety of Joule magnetostriction (length change) quantities as a function of the applied magnetic field strength. The electromagnetic coupling factor, k, of these magneto strictive materials is affected by eddy current loss factors (reduced by considering construction, geometry) and their polarization state and stress configuration as well as the materials heat capacity, thermal conductivity and both static and dynamic tensile strength and the efficiency of the application of the requisite magnetic flux density to the material under predetermined mechanical stresses.
In an un-polarized state magnetostrictive transducers are non-linear, however, in a polarized state (achieved by the use of permanent magnets, direct current or operation at remanance) they are linear (i.e. piezomagnetic) .
Properly arranged magnetostrictive transducers can achieve radiated ultrasonic (acoustic) powers up to several kilowatts with efficiencies of 50%, however, operating frequencies are usually limited to frequencies below 100 kHz.
Typically electrostatic transducers comprise a fixed conductive plate having one electric charge and a moveable conductive plate (diaphragm) to which is applied a variable (amplitude) attractive or repulsive electric charge. The resulting force on the diaphragm produces a mechanical energy which is transferred to the surrounding atmosphere.
Typical piezoelectric transducers use crystals or polycrystalline ceramic materials and in their simplest form are arranged to form an expansion-contraction region along the axis between the electrodes when an alternating voltage, also typically a very low current is applied. These materi¬ als may be operated in various modes, two of those modes be¬ ing the 33-mode where the stress, strain and electric field are in the same direction and the 31-mode where the stress and strain are in the same direction but orthogonal to the electric field. For the example of piezoelectric ceramics their properties vary as a function of time, static stress, stress cycling and electric field strength.
The electro magnetic coupling factor, k, of these materials is an important measure of the effectiveness of the energy conversion mechanism and is a function of mutual elastic and dielectric energy density, elastic self energy density and dielectric self energy density.
A benefit of piezo electric transducers of the polymeric film type is the adaptability of their physical form to the shape required in the application. They are pliant, flexible, tough and light weight. These materials are based on a polyvinylidene flouride (PVDF) which show typically the highest piezo and pyroelectric activities of most polymers and is capable of being produced in a variety of thickness and configurations of shape and active area.
Additional characteristics of this material comprise the ability to produce patterned transducer arrays, high piezoelectric sensitivity in planar and hydrostatic modes g which can produce volts into 10 ohm resistance, broad band
_3 frequency response from 10 Hz to GHz providing also a wide
—8 6 dynamic response over 286 dB (10 to 10 psi) (utorr to
Mbar) , elastic compliance, high dielectric strength (up to 75V/um) , high mechanical strength 10 9-1010 Pascal modulus and importantly high stability particularly in high moisture, high temperature (100'C), chemical, oxidant and UV affected atmospheres. Low mechanical and electric impedance allows efficient transfer of energy to air or other gasses.
BRIEF DESCRIPTION OF THE INVENTION
In an aspect of the invention a method for atomizing a liquid at temperatures and pressures below the boiling point of the liquid (evaporation) comprises the steps of; a) providing a working atmosphere comprising a mixture of gas and suspended liquid droplets, and, b) subjecting said working atmosphere to ultrasonic energy which reduces the size of said liquid droplets .
In a further aspect of the invention a method for converting liquid into a vapour at temperatures and pressures below the boiling point of the liquid (evaporation) comprises the steps of; a) providing a working atmosphere that is to be cooled, comprising a mixture of gas and suspended liquid droplets, and, b) subjecting said working atmosphere to ultrasonic energy which partially evaporates said liquid droplets, thereby inducing absorption of latent heat of evaporation from the said working atmosphere thereby cooling the atmosphere.
In yet a further aspect of the invention a method for converting liquid into a vapour at temperatures and pressures below the boiling point of the liquid (evaporation) comprises the steps of; a) providing a working atmosphere comprising a mixture of gas and suspended liquid droplets, and, b) subjecting said working atmosphere to ultrasonic energy which evaporates said liquid droplets, thereby inducing absorption of latent heat of evaporation from the said working atmosphere thereby cooling the atmosphere.
In another aspect of the invention a method of evaporation according to the method described above comprises the further step of c) circulating a portion of the working atmosphere so as to be subjected to step b) again and thereby further cool the working atmosphere. Yet another aspect of the invention is a method of evaporation comprising the further step of g) using a predetermined ultrasonic energy frequency and amplitude which selectively vaporizes a selected liquid.
In yet a further aspect of the invention a method of conditioning air comprises the steps of; a) creating a flow of air through a passage, b) distributing droplets of liquid in said flowing air, c) applying ultrasonic energy into said flowing air containing liquid droplets, and thereby inducing absorption of latent heat of evaporation from said flowing air to cool said air.
A further aspect of the invention is an air-conditioning apparatus for conditioning an air atmosphere comprising an air flow passage for passing an air atmosphere therethrough, liquid droplet distribution means to distribute droplets of liquid in said air flow, and an ultrasonic energy emitter means arranged and adapted so as to emit ultrasonic energy into said air flow 'passage containing air and liquid droplets to thereby induce absorption of latent heat of evaporation from said flowing air to cool said air.
In an aspect of the invention a bacterial reduction apparatus comprising an air flow passage for passing an air atmosphere therethrough, liquid droplet distribution means to distribute droplets of liquid containing bacteriological matter into said air flow, and an ultrasonic energy emitter means arranged and adapted so as to emit ultrasonic energy into said air flow passage containing air and said liquid droplets o thereby evaporate said liquid droplets destroying said bacteriological matter, inducing absorption of latent heat of evaporation from the said air and cooling the air and in combination reducing the incidence of live bacteriological matter in said air/vapour atmosphere passing from said flow passage.
In a further aspect a bacterial reduction apparatus comprises an ultrasonic energy emitter adapted to have its field of effect directed to the internal volume of a pipe containing a working atmosphere that is to be cooled comprising a mixture of gas and liquid droplets containing bacteriological matter, and, an ultrasonic energy emitter means arranged and adapted so as to emit ultrasonic energy into said working atmosphere to thereby evaporate said liquid droplets to induce an absorption of the latent heat of evaporation from the said working atmosphere thereby cooling the atmosphere and reducing the incidence of live bacteriological matter in said air/vapour atmosphere passing from said flow passage.
BRIEF DESCRIPTION OF THE DRAWINGS
In order that the invention may be more clearly understood, reference will now be made to the accompanying drawings, wherein
Fig. 1 depicts a schematic of an air conditioning system incorporating the method and apparatus of the invention,
Fig. 2 depicts a schematic of an air-conditioning apparatus using a heat exchanger means incorporating the method and means of the invention, and
Fig. 3 depicts a schematic of a closed pipe work system incorporating the method and means of the invention. DETAILED DESCRIPTION OF THE INVENTION
It will be understood that the following descriptions relating to typical embodiments of the present invention are given for the purpose of illustration only and that this invention includes all modifications and equivalents with lie within the scope of the invention.
In an air-conditioning example, as depicted schematically in Fig. 1, incoming atmosphere 10 is a mixture of air and water vapour to which is added by ato ization means 11, a spray of water droplets 12 which can be carried by the air flow denoted by arrows 13.
In this particular atmospheric condition ultrasonic energy is most advantageously applied.
In this embodiment the air, vapour, and water droplet mixture is directed into an air flow passage 14 by a negative pressure fan 15 (located coaxial with the air flow passage) . Within the air flow passage is preferably located an ultrasonic energy emitter means 16 arranged to direct its energy emission into the air flow passage.
The physical configuration of such an energy emitter means could take many forms. In this embodiment the emitter is formed integral with a grid like form work 17 located in the air flow path within the air flow passage. The emitter is required to create an environment in the air, vapour, water droplet air flow, which leads to the evaporation of the water droplets.
In this embodiment piezo film 18 is adhered to the grid like frame work 17. The framework is designed to minimize friction to the air flow and to space the active (piezo film) ultrasonic emission areas within the air flow such that the field in which evaporation takes place is confined to the air flow passage in the vicinity of the grid like framework. In an alternative embodiment schematically depicted in Fig. 2 the framework may be arranged as an array of passages 19 and 20 in which the piezo film is placed in passageways 19 such that its field of effect envelopes the volume of the passageway. Other passages 20 for communicating dry air to be cooled are arranged to lie orthogonal to the first said passages as in a heat exchanger configuration. Thus the other passages can act as the dry side of the heat exchanger and as latent heat of evaporation is drawn from the atmosphere within the first of said passages, heat will also be drawn from the other passages. Thus the air 20 flowing in the dry side of the heat exchanger looses heat and its temperature reduces. This arrangement may be suitable for use in an air-conditioning apparatus to provide cool dry air to which can be added moisture if desired.
It is a property of the above process while in use, that the vapour pressure of the air flowing in the passages acted upon by the ultrasonic energy emitter means is increased, therefore, a means to condense the acquired water vapour 21 (refer to Fig. 1) may be used to reduce the vapour pressure (relative humidity) of the air flow exiting from the first of said air flow passages. Since condensing water releases its latent heat of phase change, this heat if not used by the apparatus, may be released to the atmosphere and the condensed water 22 used in the evaporation process as a source of the water to be atomised. Typically, also, the condensed water is relatively cool and assists the cooling effect caused first by the atomised spray vaporising and then by the further vaporisation induced by the ultrasonic means.
in a further adaption of the alternative embodiment described above, moisture loaded air flow produced by the ultrasonic emitters can be injected into the wet side of a heat exchanger configuration wherein, upon condensation of the water in the air flow passages, latent heat of phase change is drawn from the air flow on the dry side of the heat exchanger.
The preceding embodiments are an example of a open ended atmospheric application of the processes of the invention used typically in the control of temperature and humidity in domestic and industrial air conditioning.
The embodiment as depicted in Fig. 3 relates to a closed application of the process of the invention, although self contained in its configuration, this particular arrangement may be used to enhance the operation of a conventional open ended air conditioning system.
Fig. 3 depicts a cross-section of a single bore pipe 23 having an internal wall 24 and an internal atmospheric condition A, initially comprising atomized liquid in gaseous suspension. The atomised liquid may be water, alcohol or other suitable liquid which has a change of state temperature at or below the pressure internal of the pipe, while the working or transport, gas used therein may be air, an inert gas or other suitable gas typically although not necessarily at atmospheric or lower pressure.
On the internal surface of the wall 24 there is located an ultrasonic energy emitter 25, preferably of the piezo film type. A further embodiment not shown may provide for a portion of the pipe to be constructed of a suitable transducer material. Alternatively, the film may be located in a grid like configuration within the pipe and/or the film may still be able to exert its field of effect into the pipe although it is attached or adhered to the outside of the pipe. It the latter case it could be that the mechanical resonance of the pipe could be chosen to match the ultrasonic frequencies required for the purposes of advantageously af¬ fecting the contents of the pipe. Furthermore, the internal surface of the pipe may be advantageously shaped or profiled so as to promote the desired effect occurring within the pipe .
When the piezo film is energized in a required zone of the pipe, the atmosphere condition A will change to a state Al, in which the liquid droplets suspended in the pipe volume are evaporated. This process draws latent heat of change of state from the gas atmosphere Al in the pipe as well as the region outside the pipe or as in this embodiment atmosphere B which exist outside the pipe. The efficiency of this arrangement being of course dependant on the heat transfer characteristics of the pipe as determined by its material and surface profile and the characteristics of the region external of the pipe.
Schematically, as depicted in Fig. 3 the vaporised atmosphere Al is pumped to a location 26 for condensation and then for insertion again into the atmosphere at A and the latent heat of phase change from vapour to liquid occurring at 26 may be drawn off for heating purposes or vented to atmosphere.
Fig. 3 also depicts schematically the disposition of an atmosphere B surrounding the pipe which may advantageously made a part of the air flow of an open ended air conditioning apparatus. In this case, the atmosphere B will be in the vicinity of the pipe and leave the vicinity at a cooler temperature because there will be. a loss of energy as the latent heat of change of state taking place within the pipe will be drawn from the passing air flow denoted as atmosphere B.
However, further assistance to the process of cooling atmosphere B maybe provided by locating additional piezo film adjacent or upon the pipe, whereby, the field of influence of an ultrasonic energy field may also impinge on the atmosphere B flowing past the pipe. It is anticipated that in such an arrangement any droplets (atomized liquid) suspended in atmosphere B may be acted upon in such a way that evaporation is induced and further latent heat of phase change is drawn from atmosphere B to thereby produce cool moist (i.e. high vapour pressure) atmosphere.
It will be appreciated that the gas, liquid mixture used in the pipe could be different from the typically air/water mixture used external to the pipe and advantageously so when the pipe mixture is capable of producing temperature reduc¬ tions at temperatures below O'C.
Indeed, in the case of below water freezing temperatures any water that condenses on the pipe would be almost immediately re-evaporated and its latent heat of change of state typically taken from the atmosphere B while the latent heat of condensation lost into the pipe system.
It is further possible to appreciate that the air/water mixture of the atmosphere B can be controlled in respect to its temperature and .vapour pressure by the controlled action of the piezo film both within and external to the pipe. Control is possible by way of varying one or more of a number of driving forces applied to the piezo film. These forces include the frequency of operation, the level of the signal applied and the duration of its application. Therefore, although there may be a number of controlled variables, it is possible using appropriate control means, to make it easy for the operator to adjust one indicator for temperature and one indicator for relative humidity.
The embodiment schematically depicted in Figs. 2 and 3 may form the basis for an arrangement of a plurality of such pipes, arranged so that a large volume of gas, liquid or atmosphere may be drawn past the pipes in quantities sufficient to control the temperature and humidity of larger volumes of atmosphere as may be required in domestic and industrial environments. Although not depicted, the environment in the vicinity of the cooling coils of a typical Reverse Cycle Air- Conditioner (RC A/C) may be controlled using the field of an ultrasonic emitter. For example, piezo film, as an example of the ultrasonic emitter, could be placed adjacent or upon the cooling coils of the RC A/C and it will be found that there will be beneficial effect by the improvement of the efficiency of heat transfer.
Using the abovementioned arrangement any liquid contained within the atmosphere passing within the field of effect of the emitter will be evaporated thus reducing its temperature of the atmosphere adjacent its placement.
It is thought, that as long as the vapour pressure in the passing atmosphere is below saturation, this process can continue to produce benefits since moist atmosphere will a) assist the cooling effect of the RC A/C apparatus, and b) beneficially add moisture to the RC A/C air being produced which typically is dried by the A/C apparatus.
The tendency for the cooling coils to accumulate by way of condensation, water from the atmosphere being passed through them, provides the ideal environment for the application of the process of the invention. Evaporation of the water produced not only balances the loss of any latent heat of condensation but should assist the generally cooling effect of the cooling coils by promoting evaporation when the effect of the ultrasonic emitters is added to the process.
A further embodiment of the invention not depicted is that of adjusting the frequency and/or amplitude of the ultrasonic energy to selectively vaporize a liquid which has been entrained by any suitable atomisation means into an atmosphere as previously described. In this example, there may exist a number of fluids in a mixture and after atomisation the application of a particular ultrasonic energy will separate from the atmosphere in vapour form the desired fluid. Alternatively, the resulting atmosphere may be used in a particular chemical process to advantage as a result of the vaporization of the desired liquid.
VAPOUR COMPRESSION REFRIGERATION
Conventional refrigeration processes depend on the vaporisation of refrigerant generally in a closed system evaporator. Vaporising refrigerant extracts from the evaporator the necessary heat to supply the latent heat of vaporisation of the refrigerant and the evaporator, in turn draws the necessary heat from its surroundings thus cooling the enclosed refrigerator space.
The vaporisation process takes place at the entrance to the evaporator, which, typically comprises an isenthalpic nozzle arranged to create a two phase (liquid/vapour) atmosphere which is cooled in the process but the droplets do not always totally vaporise.
Therefore, ultrasonic induced vaporisation with little extra energy expenditure to create the ultrasonic environment, will increase the amount of vaporisation, enhance the cooling effect of the evaporator and increase the quantity of heat drawn from the surroundings of the evaporator thus further cooling the enclosed refrigerator space. This may occur by way of the action of ultrasonic energy on the gaseous atmosphere itself and may advantageously induce sympathetic resonant vibrations in the mechanical structure of the evaporator apparatus.
With the advantageous use of such an arrangement, not only will current CFC based refrigerants work more efficiently but more environmentally friendly refrigerants which previously worked less efficiently in traditional arrangements may work in the new arrangement with increased efficiency to rival current CFC based refrigerants.
ABSORPTION REFRIGERATION
Absorption refrigeration for domestic use has generally been abandoned for a number of reasons, namely, high running costs, they are expensive to build, poisonous refrigerant (ammonia) is typically used and because of the corrosive nature of the refrigerant a 10 year life time is typical. The three latter reasons have become lesser concerns as, manufacturing techniques, handling and alternative refrigerants and planned obsolescence, measures improve. However, with the use of a low cost ultrasonic vaporisation process which greatly enhances heat exchange efficiency, the economics of running such a refrigerator become more affordable. Add to this the improvements of technology which provides alternative energy especially in remote areas and small absorption refrigeration system which uses little energy becomes an even more economic proposition for these areas.
BACTERIA REDUCTION IN GASEOUS ENVIRONMENTS
Although not described in detail hereinbefore, it is believed that, even though the use of ultrasonic emitters to reduce or eliminate bacteriological organisms in liquid is well known, the use of ultrasonic emitters in a liquid vapour, liquid droplet and gaseous atmosphere to reduce or eliminate bacteriological organisms is not known.
The parameters of the environment required to produce this desired result comprise a suitable field flux of ultrasonic energy at an appropriate frequency of operation and an appropriate exposure period of the mixture within the field. A variety of applications of this aspect of the invention are described herein. One example is the use of such an environment in the operation of a cooling tower as is typically used in commercial air-conditioning plants. The incidence of Legionella bacteria in its many forms has been cause for great concern to health officials. Therefore, it will be clearly apparent that, either the direct treatment of the water towers' water reservoir, or, treatment of the environment about the water tower cooling apparatus would be advantageous in this regard.
Placement of a suitable ultrasonic emitter in one or more of these locations would be beneficial by a) reducing or eliminating harmful bacteriological organisms and b) reducing the temperature by inducing further vaporisation.
In a further example it may be seen that domestic hot water systems may be kept at lower temperatures than are typically the case. Generally, hot water services are kept at temperatures greater than 60"C for the express reason of providing an environment non-conducive to unwanted bacteriological growth, however, a lower temperature say between 50*C and 55*C would still suffice for domestic hot water purposes.
Therefore, by providing an efficient , reliable and safe in-line ultrasonic emitter device which adequately eliminates bacteria at the outlet of the hot water service, the thermostatically controlled hot water service temperature may be kept at more economical and safer temperatures.
A bacteriological barrier as generally proposed herein, could also be adapted to fit at the outlets of air-condition¬ ing systems of any type, so that, the air, vapour, and suspended moisture mixture of the gasses being supplied to the room, operating theatre, etc, can be adequately treated to eliminate or reduce the level of airborne contaminants which would otherwise possibly be harmful to the room oc¬ cupants.
An embodiment of such a barrier could be in much the same configuration as that depicted and described in regards to the grid framework shown in Fig. 1.

Claims

THE CLAIMS DEFINING THE INVENTION ARE AS FOLLOWS:
1. A method for atomizing a liquid at temperatures and pressures below the boiling point of the liquid (evaporation) comprising the steps of; a) providing a working atmosphere comprising a mixture of gas and suspended liquid droplets, and, b) subjecting said working atmosphere to ultrasonic energy which reduces the size of said liquid droplets.
2. A method for converting liquid into a vapour at temperatures and pressures below the boiling point of the liquid (evaporation) comprising the steps of; a) providing a working atmosphere that is to be cooled, comprising a mixture of gas and suspended liquid droplets, and, b) subjecting said working atmosphere to ultrasonic energy which partially evaporates said liquid droplets, thereby inducing absorption of latent heat of evaporation from the said working atmosphere thereby cooling the atmosphere.
3. A method for converting liquid into a vapour at temperatures and pressures below the boiling point of the liquid (evaporation) comprising the steps of; a) providing a working atmosphere comprising a mixture of gas and suspended liquid droplets, and, b) subjecting said working atmosphere to ultrasonic energy which evaporates said liquid droplets, thereby inducing absorption of latent heat of evaporation from the said working atmosphere thereby cooling the atmosphere.
4. A method of evaporation according to claims 2 or 3 comprising the further step of c) circulating a portion of the working atmosphere so as to be subjected to step b) again and thereby further cool the working atmosphere.
5. A method of evaporation according to claims 2 or 3 comprising the further step of d) circulating an immiscible liquid (gas or fluid) about said working atmosphere to thereby further cool the immiscible liquid by way of heat transfer between the liquid and atmosphere.
6. A method of evaporation according to claims 2 or 3 comprising the further step of e) using a predetermined ultrasonic energy frequency which selectively vaporizes a selected liquid.
7. A method of evaporation according to claims 2 or 3 comprising the further step of f) using a predetermined ultrasonic energy amplitude which selectively vaporizes a selected liquid.
8. A method of evaporation according to claims 2 or 3 comprising the further step of g) using a predetermined ultrasonic energy frequency and amplitude which selectively vaporizes a selected liquid.
9. A method of conditioning air comprising the steps of; a) creating a flow of air through a passage, b) distributing droplets of liquid in said flowing air, c) applying ultrasonic energy into said flowing air containing liquid droplets, and thereby inducing absorption of latent heat of evaporation from said flowing air to cool said air.
10. An air-conditioning apparatus for conditioning an air atmosphere comprising an air flow passage for passing an air atmosphere therethrough, liquid droplet distribution means to distribute droplets of liquid in said air flow, and an ultrasonic energy emitter means arranged and adapted so as to emit ultrasonic energy into said air flow passage containing air and liquid droplets to thereby induce absorption of latent heat of evaporation from said flowing air to cool said air.
11. An air-conditioning apparatus according to claim 10 wherein said ultrasonic energy emitter comprises an electrostrictive transducer.
12. An air-conditioning apparatus according to claim 10 wherein said ultrasonic energy emitter comprises an magnetostrictive transducer.
13. An air-conditioning apparatus according to claim 10 wherein said ultrasonic energy emitter comprises an piezoelectric transducer.
14. An air-conditioning apparatus according to claim 13 wherein said piezoelectric transducer comprises a piezo film sensor arranged to emit ultrasonic energy into said air flow passage.
15. An air-conditioning apparatus according to claim 14 wherein said piezo film sensor is arranged in a grid like configuration and said grid is located in said air flow passage such that air may pass through said grid wherein the liquid in said air flow is evaporated by way of the action of ultrasonic energy on the atmosphere passing therethrough, inducing absorption of latent heat of evaporation from said air and cooling the air.
16. A bacterial reduction apparatus comprising an air flow passage for passing an air atmosphere therethrough, liquid droplet distribution means to distribute droplets of liquid containing bacteriological matter into said air flow, and an ultrasonic energy emitter means arranged and adapted so as to emit ultrasonic energy into said air flow passage containing air and said liquid droplets to thereby evaporate said liquid droplets destroying said bacteriological matter, inducing absorption of latent heat of evaporation from the said air and cooling the air and in combination reducing the incidence of live bacteriological matter in said air/vapour atmosphere passing from said flow passage.
17. A bacterial reduction apparatus comprising an ultrasonic energy emitter adapted to have its field of effect directed to the internal volume of a pipe containing a working atmosphere that is to be cooled comprising a mixture of gas and liquid droplets containing bacteriological matter, and, an ultrasonic energy emitter means arranged and adapted so as to emit ultrasonic energy into said working atmosphere to thereby evaporate said liquid droplets to induce an absorption of the latent heat of evaporation from the said working atmosphere thereby cooling the atmosphere and reducing the incidence of live bacteriological matter in said air/vapour atmosphere passing from said flow passage.
PCT/AU1992/000619 1991-11-14 1992-11-16 Ultrasonic atomising, cooling and air-conditioning WO1993010404A1 (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
AUPK9478 1991-11-14
AUPK947891 1991-11-14
AUPL079492 1992-02-10
AUPL0794 1992-02-10

Publications (1)

Publication Number Publication Date
WO1993010404A1 true WO1993010404A1 (en) 1993-05-27

Family

ID=25644155

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/AU1992/000619 WO1993010404A1 (en) 1991-11-14 1992-11-16 Ultrasonic atomising, cooling and air-conditioning

Country Status (1)

Country Link
WO (1) WO1993010404A1 (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5775121A (en) * 1995-11-07 1998-07-07 Kabushiki Kaisha Seibu Giken Method and device for refrigerating a fluid
WO2014064666A1 (en) * 2012-10-26 2014-05-01 CoolFactor, LLC Intercooler heat exchanger for evaporative air conditioner system
WO2014064667A1 (en) * 2012-10-26 2014-05-01 CoolFactor, LLC Self-contained evaporative air conditioner system
WO2015069284A1 (en) * 2013-11-08 2015-05-14 CoolFactor, LLC Evaporative air conditioning system
US9091450B2 (en) 2012-08-15 2015-07-28 CoolFactor, LLC Evaporative air conditioning system
RU2581982C2 (en) * 2014-04-24 2016-04-20 Федеральное государственное бюджетное образовательное учреждение высшего образования "Пензенский государственный университет архитектуры и строительства" Device for heat and moisture treatment of air
US20180094879A1 (en) * 2016-10-05 2018-04-05 Johnson Controls Technology Company Ultrasonic enhanced heat exchanger systems and methods
WO2019195402A1 (en) * 2018-04-05 2019-10-10 Carrier Corporation Air handler unit
CN114669436A (en) * 2022-03-17 2022-06-28 重庆大学 Frequency modulation drive circuit, frequency modulation drive method and drive device

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU5053259A (en) * 1959-07-07 1960-01-14 N. V. Philips' Gloeilampenfabrieken Improvements in or relating to ultrasonic vibrators for dispersing fluids
SU499464A1 (en) * 1973-09-03 1976-01-15 Машиностроительный Завод "Сатурн" Device for moistening ventilation air
US4042016A (en) * 1975-10-28 1977-08-16 Evelyn Boochever Environmental humidification and cooling system
WO1979001074A1 (en) * 1978-05-16 1979-12-13 Ex Cell O Corp Method and means for applying bactericide to container for sterilization
SU932119A1 (en) * 1980-12-22 1982-05-30 Предприятие П/Я М-5147 Air humidifying method
SU1537969A1 (en) * 1986-10-14 1990-01-23 Ленинградский технологический институт холодильной промышленности Method of evaporation cooling of heat-exchange surface

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU5053259A (en) * 1959-07-07 1960-01-14 N. V. Philips' Gloeilampenfabrieken Improvements in or relating to ultrasonic vibrators for dispersing fluids
AU4109564A (en) * 1963-03-06 1965-08-19 International Business Machines Corporation Resonator for radiation generated by stimulated emission
SU499464A1 (en) * 1973-09-03 1976-01-15 Машиностроительный Завод "Сатурн" Device for moistening ventilation air
US4042016A (en) * 1975-10-28 1977-08-16 Evelyn Boochever Environmental humidification and cooling system
US4042016B1 (en) * 1975-10-28 1987-03-31
WO1979001074A1 (en) * 1978-05-16 1979-12-13 Ex Cell O Corp Method and means for applying bactericide to container for sterilization
SU932119A1 (en) * 1980-12-22 1982-05-30 Предприятие П/Я М-5147 Air humidifying method
SU1537969A1 (en) * 1986-10-14 1990-01-23 Ленинградский технологический институт холодильной промышленности Method of evaporation cooling of heat-exchange surface

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
DERWENT ABSTRACT, Accession No. 90381315/51, Class Q74; & SU,A,1 537 969 (LENGD REFRIGIND EN), 23 January 1990. *
DERWENT ABSTRACT, Accession No. E7148 K/14, Class Q74; & SU,A,932 119 (KHARTOV A.M.), 30 May 1982. *
DERWENT ABSTRACT, Accession No. K2180x/42, class Q74; & SU,A,499 464 (PANTY UKHIN S.I.), 29 March 1976. *

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5775121A (en) * 1995-11-07 1998-07-07 Kabushiki Kaisha Seibu Giken Method and device for refrigerating a fluid
US6055824A (en) * 1995-11-07 2000-05-02 Kabushiki Gaisha Seibu Giken Method and device for refrigerating a fluid
US9091450B2 (en) 2012-08-15 2015-07-28 CoolFactor, LLC Evaporative air conditioning system
WO2014064666A1 (en) * 2012-10-26 2014-05-01 CoolFactor, LLC Intercooler heat exchanger for evaporative air conditioner system
WO2014064667A1 (en) * 2012-10-26 2014-05-01 CoolFactor, LLC Self-contained evaporative air conditioner system
WO2015069284A1 (en) * 2013-11-08 2015-05-14 CoolFactor, LLC Evaporative air conditioning system
RU2581982C2 (en) * 2014-04-24 2016-04-20 Федеральное государственное бюджетное образовательное учреждение высшего образования "Пензенский государственный университет архитектуры и строительства" Device for heat and moisture treatment of air
US20180094879A1 (en) * 2016-10-05 2018-04-05 Johnson Controls Technology Company Ultrasonic enhanced heat exchanger systems and methods
US10563931B2 (en) * 2016-10-05 2020-02-18 Johnson Controls Technology Company Ultrasonic enhanced heat exchanger systems and methods
WO2019195402A1 (en) * 2018-04-05 2019-10-10 Carrier Corporation Air handler unit
US11719445B2 (en) 2018-04-05 2023-08-08 Carrier Corporation Air handler unit
CN114669436A (en) * 2022-03-17 2022-06-28 重庆大学 Frequency modulation drive circuit, frequency modulation drive method and drive device
CN114669436B (en) * 2022-03-17 2024-02-02 重庆大学 Frequency modulation drive circuit, frequency modulation drive method, and drive device

Similar Documents

Publication Publication Date Title
EP0773412B1 (en) A method and a device for refrigeration of fluid and desiccative refrigeration of gas
WO1993010404A1 (en) Ultrasonic atomising, cooling and air-conditioning
CA2502087C (en) System and method for humidifying homes and commercial sites
Alrbai et al. Energy and exergy analysis of a novel humidification-dehumidification desalination system with fogging technique
US20090126385A1 (en) Switch cabinet
US20040168462A1 (en) Air conditioning system
JP2004524875A (en) Humidifying method and device using silver ion water
WO2010142012A1 (en) Atmospheric water generator
JP5537010B2 (en) Plant growing device
KR100461934B1 (en) Fluid cooling and gas dehumidification cooling method and apparatus
JP2010082213A (en) Hair care appliance incorporating reduced water mist spraying device
US12151194B2 (en) Atmospheric water generator apparatus
JP5523689B2 (en) Air conditioner
JP3540107B2 (en) Method and apparatus for fluid cooling and gas dehumidification cooling
CN103988039A (en) Heat exchanger for cooling a heating tube and method thereof
JPH10311691A (en) Gas cooling method and apparatus
JP2019502090A (en) Highly efficient systems and equipment in mass transfer
Ahmad et al. Performance evaluation of a novel hydrophobic membrane used in a desalination system: a comparison between static and moving configurations
US20030161754A1 (en) Method and vibrating device for conditioning, air-conditioning, cooling and decontaminating, disinfecting and sterilization physical media
GB2582622A (en) Cooling apparatus and method of cooling
EA043312B1 (en) INSTALLATION FOR PRODUCING ATMOSPHERIC WATER
CN117146494A (en) Sterilization and moisture preservation device and refrigerator
KR20010011692A (en) Condenser
JP3101385U (en) Humidity adjustment device
JPH02213630A (en) Humidifying device

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): AT AU BB BG BR CA CH CS DE DK ES FI GB HU JP KP KR LK LU MG MN MW NL NO PL RO RU SD SE US

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): AT BE CH DE DK ES FR GB GR IE IT LU MC NL SE BF BJ CF CG CI CM GA GN ML MR SN TD TG

122 Ep: pct application non-entry in european phase
REG Reference to national code

Ref country code: DE

Ref legal event code: 8642

NENP Non-entry into the national phase

Ref country code: CA

点击 这是indexloc提供的php浏览器服务,不要输入任何密码和下载