WO2002056988B1 - Method and apparatus for production of droplets - Google Patents

Method and apparatus for production of droplets

Info

Publication number
WO2002056988B1
WO2002056988B1 PCT/IL2001/001217 IL0101217W WO02056988B1 WO 2002056988 B1 WO2002056988 B1 WO 2002056988B1 IL 0101217 W IL0101217 W IL 0101217W WO 02056988 B1 WO02056988 B1 WO 02056988B1
Authority
WO
WIPO (PCT)
Prior art keywords
gas
region
liquid
permeable
cylinder
Prior art date
Application number
PCT/IL2001/001217
Other languages
French (fr)
Other versions
WO2002056988A3 (en
WO2002056988A2 (en
Inventor
Akper Sadykhov
Original Assignee
Ultrasonic Dryer Ltd
Akper Sadykhov
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 Ultrasonic Dryer Ltd, Akper Sadykhov filed Critical Ultrasonic Dryer Ltd
Priority to US10/466,489 priority Critical patent/US6899322B2/en
Priority to DE60131897T priority patent/DE60131897T2/en
Priority to EP01273332A priority patent/EP1358004B1/en
Priority to CN018221203A priority patent/CN1500002B/en
Priority to CA002435156A priority patent/CA2435156C/en
Priority to AU2002217410A priority patent/AU2002217410B2/en
Publication of WO2002056988A2 publication Critical patent/WO2002056988A2/en
Publication of WO2002056988A3 publication Critical patent/WO2002056988A3/en
Publication of WO2002056988B1 publication Critical patent/WO2002056988B1/en

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28CHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
    • F28C3/00Other direct-contact heat-exchange apparatus
    • F28C3/06Other direct-contact heat-exchange apparatus the heat-exchange media being a liquid and a gas or vapour
    • 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05BSPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B7/00Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas
    • B05B7/0012Apparatus for achieving spraying before discharge from the apparatus
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05BSPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B7/00Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas
    • B05B7/24Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas with means, e.g. a container, for supplying liquid or other fluent material to a discharge device
    • B05B7/2483Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas with means, e.g. a container, for supplying liquid or other fluent material to a discharge device the supplying means involving no pressure or aspiration, e.g. means involving gravity or capillarity
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M29/00Apparatus for re-atomising condensed fuel or homogenising fuel-air mixture
    • 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S261/00Gas and liquid contact apparatus
    • Y10S261/25Fuel spread out into a film
    • 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S261/00Gas and liquid contact apparatus
    • Y10S261/65Vaporizers

Abstract

The invention includes a method and apparatus (100) for producing mist of a liquid phase having very fine and mono-dispersed droplets. The method is realized by an apparatus (100) including a partition (101), defined by a first side surface (107) and a second side surface (113). The first side surface (107) is wetted by a liquid phase to form a film thereon, while the second side surface (113) is substantially dry. A gas stream is directed through the partition (101) from the dry side (113) to the wetted side (107) thereby forming a mist having droplets of less than i micron in size and a concentration of at least 1,000,000,000,000 per cubic cm.

Claims

AMENDED CLAIMS[received by the International Bureau on 4 August 2002 (04.08.2002); original claims 1-20 replaced by amended claims 1-20 (3 pages)]
1. A method for formation of a mist consisting of ultra-fine droplets, said method comprising the steps of: a) providing a partition, at least a region thereof being gas permeable, said region is defined by a first and by a second surface b) moistening one surface of the region by a liquid to form a film thereon, while leaving the second surface of the region substantially dry and c) establishing a stream of gas directed from the dry surface to the moistened surface of the region, wherein said gas stream is capable to pass the gas-permeable region covered by the film.
2. The method as defined in claim 1, in which said gas-permeable region has open porosity 7-36%, said film has thickness 3-5 μm and said gas stream is passed at pressure of at least 180 mbar and with a flow rate of at least 1.5 m3 /h.
3. The method as defined in claim 2, in which said gas is selected from the group consisting of air, nitrogen, carbon oxide, oxygen, ozone, inert gas and their combination.
4. The method as defined in claim 3 in which said liquid phase is selected from the group consisting of mono-phase liquid, solution, emulsion and suspension.
5. The method as defined in claim 3, in which said liquid phase is selected from the group consisting of an organic liquid, an inorganic liquid and their combination.
6. The method as defined in claim 5, in which said organic liquid is selected from the group consisting of alcohol, kerosene, oil and a liquid medication.
7. The method as defined in claim 6, in which said inorganic liquid is water.
8. The method as defined in claim 4, in which said gas is air, said liquid phase is water and said gas stream is passed at pressure 470-600 mbar and with flow rate 2.9-8.7 m3 /h.
9. An apparatus for formation of a mist consisting of ultra-fine droplets, said apparatus comprises a) a partition, at least a region thereof being gas-permeable, said region is defined by a first and a second surface 19 b) a moistening means for moistening one surface of the region by a liquid phase c) a means for establishing a gas stream directed from the dry surface of the region to the moistened surface thereof wherein said gas stream is capable to pass the gas-permeable region moistened by the liquid.
10. The apparatus as defined in claim 9, in which said partition comprises horizontally disposed gas-permeable cylinder, which is made of metallic material having thickness 1-3 mm, open porosity 26% and pore size 0.5-8.7 microns, said cylinder is disposed within a gas-impermeable cylindrical housing.
11. The apparatus as defined in claim 10, in which said gas-permeable cylinder is mounted with possibility for rotation along its longitudinal axis within the housing, said moistening means comprises a perforated pipe, extending along the cylinder and delivering the liquid phase from an external source to the inner surface of the cylinder.
12. The apparatus as defined in claim 9, in which said means for establishing the gas stream comprises a gas cylinder or a pump.
13. The apparatus as defined in claim 9, in which said means for establishing the gas stream comprises pump, residing within the housing, said pump is in communication with the outside atmosphere.
14. The apparatus as defined in claim 10, in which said gas-permeable cylinder is rigidly secured within the housing and said moistening means comprises a rotating sprinkle means, linearly displaceable within the gas-permeable cylinder and said apparatus comprises a displacing mechanism for displacing the sprinkle means.
15. The apparatus as defined in claim 10, in which said gas-permeable cylinder is directed horizontally.
16. The apparatus as defined in claim 10, in which said gas-permeable cylinder is directed vertically, wherein said moistening means comprises a rotating sprinkle means located in the upper part of the gas-permeable cylinder and said sprinkle means is rigidly secured on a hollow support, which communicates with the means for establishing the gas stream. 20
17. The apparatus as defined in claim 10, in which said moistening means comprises a vessel, filled with the liquid phase and said vessel is in communication with the gas-permeable cylinder.
18. The apparatus as defined in claim 17, in which said liquid phase is a medication.
19. A mist, produced by the method of claim 1, said mist consisting of liquid droplets, which are less than 1 micron, said droplets drifting with velocity of 1-15 cm/sec.
20. The mist as defined in claim 19, in which said liquid is water and concentration of droplets in the mist is at least 1x10 cm" .
PCT/IL2001/001217 2001-01-18 2001-12-31 Method and apparatus for production of droplets WO2002056988A2 (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
US10/466,489 US6899322B2 (en) 2001-01-18 2001-12-31 Method and apparatus for production of droplets
DE60131897T DE60131897T2 (en) 2001-01-18 2001-12-31 METHOD AND DEVICE FOR PRODUCING DROPLETS
EP01273332A EP1358004B1 (en) 2001-01-18 2001-12-31 Method and apparatus for production of droplets
CN018221203A CN1500002B (en) 2001-01-18 2001-12-31 Method and apparatus for production of droplets
CA002435156A CA2435156C (en) 2001-01-18 2001-12-31 Method and apparatus for production of droplets
AU2002217410A AU2002217410B2 (en) 2001-01-18 2001-12-31 Method and apparatus for production of droplets

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US26203201P 2001-01-18 2001-01-18
US60/262,032 2001-01-18

Publications (3)

Publication Number Publication Date
WO2002056988A2 WO2002056988A2 (en) 2002-07-25
WO2002056988A3 WO2002056988A3 (en) 2002-10-10
WO2002056988B1 true WO2002056988B1 (en) 2003-03-20

Family

ID=22995891

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/IL2001/001217 WO2002056988A2 (en) 2001-01-18 2001-12-31 Method and apparatus for production of droplets

Country Status (9)

Country Link
US (1) US6899322B2 (en)
EP (1) EP1358004B1 (en)
CN (1) CN1500002B (en)
AT (1) ATE380578T1 (en)
AU (1) AU2002217410B2 (en)
CA (1) CA2435156C (en)
DE (1) DE60131897T2 (en)
ES (1) ES2298193T3 (en)
WO (1) WO2002056988A2 (en)

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7604685B2 (en) * 2004-11-22 2009-10-20 Porous Media Corp Method for the selective extraction of acids
US8529667B2 (en) * 2004-11-22 2013-09-10 Matt Thundyil Method for the selective extraction of acids, bases and polar salts
AU2006275317B2 (en) 2005-08-04 2012-08-09 Saban Ventures Pty Limited Improved aerosol
ITPD20060051A1 (en) * 2006-02-21 2007-08-22 Carel Spa AIR HUMIDIFICATION SYSTEM FOR LARGE SIZE ENVIRONMENTS AND A HUMIDIFICATION MODULE USED IN THIS PLANT
AU2008210270B8 (en) 2007-02-02 2012-04-26 Saban Ventures Pty Limited Membrane vapour concentrator
US20090064874A1 (en) * 2007-08-24 2009-03-12 Fabristeel Private Limited Method and food holding cabinet with humidity generation
WO2010085780A1 (en) 2009-01-26 2010-07-29 Teva Pharmaceutical Industries Ltd. Processes for coating a carrier with microparticles
US10857311B2 (en) 2010-01-12 2020-12-08 Omega Life Science Ltd. Method and apparatus for producing fine concentrated aerosol
CN103286031B (en) * 2013-05-16 2015-07-22 中国科学院光电研究院 High-frequency and high-speed micron-sized droplet generating device
GB2525634B (en) * 2014-04-30 2019-02-06 Univ Southampton A method for generating droplets
US10052443B2 (en) 2014-10-13 2018-08-21 Omega Life Science Ltd. Nebulizers and uses thereof
DE102015012783A1 (en) * 2015-10-05 2017-04-06 Dräger Safety AG & Co. KGaA Conditioning module for tempering and humidifying a flowing gas

Family Cites Families (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1023063A (en) * 1911-01-03 1912-04-09 Lowell C Bassford Window-screen.
US1132679A (en) * 1914-10-14 1915-03-23 Thomas E Murray Method of neutralizing corrosive fumes in gases.
FR1031185A (en) * 1951-01-19 1953-06-22 Method and device for applying liquid substances to a support
FR1473399A (en) * 1966-03-03 1967-03-17 United Shoe Machinery Ab Liquid atomizer
US3583635A (en) * 1969-02-24 1971-06-08 Jerome H Lemelson Spraying systems
GB8325047D0 (en) 1983-09-19 1983-10-19 Medica Aid Ltd Nebulizers
SE449440B (en) 1983-12-19 1987-05-04 Jr Mans Arborelius NEBULIZER FOR SUBMICRON PREPARATION, HOMOGEN AEROSOL
US4941618A (en) 1986-07-07 1990-07-17 Leeman Labs Inc. Nebulizer employing a fine mesh screen
JPH01126863U (en) 1988-02-24 1989-08-30
US5030390A (en) * 1989-07-20 1991-07-09 University Of Delaware Process for cooling water in an inflated fabric cooling dome
US5431345A (en) 1993-11-12 1995-07-11 The Procter & Gamble Company Foam dispensing system for a foamable liquid
CN2182669Y (en) * 1994-02-03 1994-11-16 廖为生 Emulsifying and mixing apparatus for oils
US5535989A (en) * 1994-12-02 1996-07-16 Sen; Dipak K. Liquid film producing process and apparatus for fluid-liquid contacting
KR0144599B1 (en) 1995-07-01 1998-07-15 윤덕용 Liquid-drop generator and device for preparing fine-partides
KR19990001064A (en) * 1996-06-27 1999-01-15 나이또오도미히사 Atomization Method and Apparatus
JPH11316031A (en) * 1998-05-06 1999-11-16 Yasumasa Akazawa Air processing device
US6315272B1 (en) * 1999-01-06 2001-11-13 Emerson Electric Co. Humidifier with stacked reservoir
IL129208A0 (en) * 1999-03-28 2000-02-17 Liposol Ltd A method and apparatus for nebulizing a liquid particulary useful for the aerosol delivery of biopharmaceuticals
US6527257B1 (en) * 2000-09-05 2003-03-04 Rps Products, Inc. Decorative humidifier and fountain combination

Also Published As

Publication number Publication date
US6899322B2 (en) 2005-05-31
EP1358004A2 (en) 2003-11-05
DE60131897T2 (en) 2008-12-04
EP1358004B1 (en) 2007-12-12
AU2002217410B2 (en) 2008-05-01
CA2435156C (en) 2010-02-02
CN1500002A (en) 2004-05-26
CN1500002B (en) 2011-07-27
CA2435156A1 (en) 2002-07-25
ES2298193T3 (en) 2008-05-16
ATE380578T1 (en) 2007-12-15
WO2002056988A3 (en) 2002-10-10
EP1358004A4 (en) 2004-04-28
US20040113292A1 (en) 2004-06-17
WO2002056988A2 (en) 2002-07-25
DE60131897D1 (en) 2008-01-24

Similar Documents

Publication Publication Date Title
WO2002056988B1 (en) Method and apparatus for production of droplets
ATE288789T1 (en) CATALYST AND METHOD FOR PURIFYING MATERIAL STREAMS
US4161282A (en) Microcapillary nebulizer and method
Li et al. Use of permeation and absorption methods for CO2 removal in hollow fibre membrane modules
Aoki et al. Enantioselective permeation through poly [γ-[3-(pentamethyldisiloxanyl) propyl]-l-glutamate] membranes
CN101218181A (en) Apparatus and method for preparing oxygen water
NO972936D0 (en) Process for the preparation of a chemical compound
AU7930500A (en) Filtering unit for a virucide substance
EP0084768B1 (en) Continuous production of polymethylpentene membranes
AU2002217410A1 (en) Method and apparatus for production of droplets
CA2098684A1 (en) Composite Porous Carbonaceous Membranes
JPH10507123A (en) Method and apparatus for separating a liquid-liquid mixture
JP7243972B2 (en) Fine bubble manufacturing device and fine bubble manufacturing method
JP2000246075A (en) Organic gas separation filter and its preparation
JP3258469B2 (en) Gas-liquid separation device
CA1097390A (en) Microcapillary nebulizer and method
JPS6250401B2 (en)
JPS6332545U (en)
JP2022144980A (en) Method for producing ultrafine bubble liquid
JPS6070336A (en) Method for yielding gas having constant concentration
JP2000157851A (en) Organic gas separating filter and organic gas separating method using the same
JP2000007323A (en) Production of microporous material, microporous material and separation of fluid
JPH0699123B2 (en) Excited Oxygen Molecule O ▲ Lower 2 ▼ (Upper 1 ▼ Δ) Generation Method
EP0370540B1 (en) Device for removal of ozone from and simultaneously moistening of air
JPH07213804A (en) Method for deaerating liquid material and device therefor

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A2

Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NO NZ OM PH PL PT RO RU SD SE SG SI SK SL TJ TM TN TR TT TZ UA UG US UZ VN YU ZA ZM ZW

AL Designated countries for regional patents

Kind code of ref document: A2

Designated state(s): GH GM KE LS MW MZ SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG

121 Ep: the epo has been informed by wipo that ep was designated in this application
AK Designated states

Kind code of ref document: A3

Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NO NZ OM PH PL PT RO RU SD SE SG SI SK SL TJ TM TN TR TT TZ UA UG US UZ VN YU ZA ZM ZW

AL Designated countries for regional patents

Kind code of ref document: A3

Designated state(s): GH GM KE LS MW MZ SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG

DFPE Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101)
B Later publication of amended claims
WWE Wipo information: entry into national phase

Ref document number: 10466489

Country of ref document: US

Ref document number: 2435156

Country of ref document: CA

WWE Wipo information: entry into national phase

Ref document number: 2001273332

Country of ref document: EP

Ref document number: 018221203

Country of ref document: CN

WWE Wipo information: entry into national phase

Ref document number: 2002217410

Country of ref document: AU

WWP Wipo information: published in national office

Ref document number: 2001273332

Country of ref document: EP

REG Reference to national code

Ref country code: DE

Ref legal event code: 8642

NENP Non-entry into the national phase

Ref country code: JP

WWW Wipo information: withdrawn in national office

Ref document number: JP

WWG Wipo information: grant in national office

Ref document number: 2001273332

Country of ref document: EP