EP0057324A1 - Process of spraying emulsions and apparatus thereof - Google Patents

Process of spraying emulsions and apparatus thereof Download PDF

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Publication number
EP0057324A1
EP0057324A1 EP81306005A EP81306005A EP0057324A1 EP 0057324 A1 EP0057324 A1 EP 0057324A1 EP 81306005 A EP81306005 A EP 81306005A EP 81306005 A EP81306005 A EP 81306005A EP 0057324 A1 EP0057324 A1 EP 0057324A1
Authority
EP
European Patent Office
Prior art keywords
liquid
emulsion
orifice
charged
potential
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP81306005A
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German (de)
French (fr)
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EP0057324B1 (en
Inventor
Ronald Alan Coffee
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Imperial Chemical Industries Ltd
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Imperial Chemical Industries Ltd
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 Imperial Chemical Industries Ltd filed Critical Imperial Chemical Industries Ltd
Priority to AT81306005T priority Critical patent/ATE19597T1/en
Publication of EP0057324A1 publication Critical patent/EP0057324A1/en
Application granted granted Critical
Publication of EP0057324B1 publication Critical patent/EP0057324B1/en
Expired legal-status Critical Current

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05BSPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B5/00Electrostatic spraying apparatus; Spraying apparatus with means for charging the spray electrically; Apparatus for spraying liquids or other fluent materials by other electric means
    • B05B5/16Arrangements for supplying liquids or other fluent material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/40Mixing liquids with liquids; Emulsifying
    • B01F23/41Emulsifying
    • B01F23/411Emulsifying using electrical or magnetic fields, heat or vibrations
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00Other mixers; Mixing plants; Combinations of mixers
    • B01F33/05Mixers using radiation, e.g. magnetic fields or microwaves to mix the material

Definitions

  • This invention relates to spraying emulsions. More particularly, it relates to new processes for forming emulsions and spraying the emulsions so formed, and to apparatus therefor.
  • An emulsion consists of small particles (generally of mean diameter in the range 0.1 to 10 microns) of a first liquid dispersed in a second liquid immiscible therewith.
  • an emulsion may be formed of finely divided particles of oil in water; or conversely, of finely divided particles of water in oil, the latter being commonly referred to as an invert emulsion.
  • An emulsion is a two- phase system; the particles constitute the disperse phase, while the medium in which they are suspended is the continuous phase. The propertiies of emulsions naturally depend on the properties of the two phases, their relative proportions and the particle size of the disperse phase.
  • Dilute emulsions containing for example up to 10% or so of disperse phase, generally have, for example, a viscosity not dissimilar from that of the continuous phase; but increasing the proportion of the disperse phase leads to thickening, and the formation of immobile, scarcely pourable systems.
  • the present invention is concerned with relatively dilute emulsions, not too thick to be able to flowlike liquids.
  • Emulsions have a variety of uses; for example in the- food and pharmaceutical industries. Cosmetics may be formulated asemulsions, and so also may pesticides. The present invention relates to emulsions to be used as sprays.
  • Emulsions are generally formed by thoroughly agitating the two phases together, for example in a high shear mixer. This is a relatively inefficient process, consuming unnecessary energy.
  • emulsions so formed are not necessarily stable, and may break down into separate bulk phases on storage.
  • the present invention provides a more efficient method of forming emulsions, not dependent on mechanical mixing, and which prevents emulsion break-down by reducing or eliminating storage time.
  • a process for forming and spraying a dilute emulsion of a first liquid in a second liquid immiscible therewith which comprises passing small amounts of the first liquid into a body of the second liquid while electrically charging the first liquid relative to the second liquid to a potential sufficient to cause emulsification therein, and atomising the charged emulsion thereby formed.
  • Such atomisation may be carried. out wholly or partly by mechanical means, but conveniently it may be effected by passing the charged emulsion into a region of high electrical field strength thereby causing it to atomise.
  • the invention further comprises apparatus for forming and spraying an electrically charged emulsion of a first liquid in a second liquid immiscible therewith which comprises an orifice formed in an electrically conducting material communicating with a vessel for containing the second liquid, means for delivering the first liquid to and through the orifice, means for charging the orifice to a high potential, and a sprayhead for receiving the electrically charged emulsion formed at the orifice and for emitting the emulsion in the form of an electrically charged spray.
  • the sprayhead comprises an electrically conducting surface for receiving the electrically charged emulsion, and means for creating a field strength at the surface sufficient to atomise the emulsion therefrom in the form of a fine spray.
  • the emulsions being electrostatically charged, are attracted to spray targets and coat them more evenly than uncharged sprays would do. Electrostatic force fields carry the charged particles behind the target, so as to coat all sides of it.
  • the method and apparatus of the invention may be used for spraying paints and like coatings on to structures or articles of manufacture, and (with particular advantage) for spraying pesticides (eg, insecticides, herbicides, fungicides and the like) on to crops or weeds.
  • pesticides eg, insecticides, herbicides, fungicides and the like
  • Conveniently emulsions according to the invention comprise from about 1 to about 10% by weight disperse phase, though higher and lower amounts may be used where appropriate.
  • a container 1 of insulating material (glass) is provided with an earthed jacket 13 of conductive material, and with a conduit 2 for delivering liquid.
  • a metallic exit nozzle 3 In the base of the container 1 is a metallic exit nozzle 3, with a bore of capillary.size.
  • a metal ring 4 connected (as shown in Figure 2) to earth 19.
  • a second container 5 of insulating material (glass) fed by a liquid delivering conduit 6.
  • a second metallic exit nozzle 7, of capillary dimensions is provided in the base of container 1 a second metallic exit nozzle 7, of capillary dimensions.
  • Both nozzles 3 and 7 are connected (as shown in Figure 2) to a source of high potential 8 (0-20 kilovolts, 200 microamp module) via a switch 9.
  • a source of high potential 8 (0-20 kilovolts, 200 microamp module)
  • a switch 9 Below the container 5, within the container 1, and symmetrically disposed around the outlet of the nozzle 7, is a second earthed metal ring. 10.
  • the nozzle 3 may be closed by an exterior cap or bung 12.
  • a hydrocarbon oil 11 is passed into the container 1 from the conduit 2 until the level of oil 11 is above the base of container 5.
  • An aqueous solution containing 7% by weight of para q uat dichloride is passed through conduit 6 into container 5.
  • Capillary-sized droplets of the aqueous solution pass out through nozzle 7 and sink through the oil 11.
  • the switch 9 is then closed, applying a voltage of the order of 15 kilovolts to the nozzles 7 and 3.
  • the oil in the container 1 becomes turbulent, exhibiting negative surface tension due to the electrical charge it carries.
  • the cap 12 is then removed, and the emulsion (containing about 4% weight disperse phase) issues from the nozzle 3.
  • the electric field between the nozzle 3 and the earthed ring 4 causes the emulsion to atomise as fine particles, which pass outwards and are attracted to suitable targets, eg, weeds.
  • suitable targets eg, weeds.
  • the flows of oil 11 through conduit 2 and of aqueous solution through conduit 6 are adjusted to maintain the levels of liquid in containers 1 and 5 constant.
  • the particle size of the disperse phase in the emulsion may be controlled by control of the field strength at the nozzle 7; eg, by varying the distance between the nozzle 7 and the ring 10, or, more conveniently, by varying the applied voltage. The stronger the field the smaller are the droplets.
  • the particle size of droplets in the atomised emulsion may be controlled by control of the field strength at the nozzle 3. This may be done by varying the voltage on the nozzle 3, the position of the ring 4, or by applying a variable voltage (positive or negative with respect to the potential of the nozzle 3) to the ring 4 instead of earthing it.
  • the same apparatus may be used, if desired, to form an emulsion in which water or an aqueous solution is the continuous phase and oil is the disperse phase, by feeding water to container 1 and oil to container 2.
  • the nozzle 7 may be charged by induction, as shown in Figure 3. If the nozzle 7 is connected to the earth 19, and the source of potential 8 to ring 10, a strong charge of opposite sign will be induced on nozzle 7 and liquid passing through will be charged by contact in the same way as if the nozzle 7 were connected to source of potential 8, except that the charge will be of opposite sign.
  • An emulsion will be formed in just the same way, with the charging current being taken from earth. This saves current at nozzle 7, but slightly more is used at nozzle3, because the emulsion has to be discharged and recharged in the opposite sense before atomisation.
  • the power consumption of the device is not high, and is readily adapted to use in portable devices powered by dry cells, or even solar cells. For agricultural spraying, however, it will often be convenient to mount the device on a vehicle (eg a tractor or aircraft) and power it from a power source carried on the vehicle (eg the tractor battery).
  • the emulsion may be atomised wholly or partly mechanically, eg from a pressure nozzle or spinning cup or disc.
  • electrostatic atomisation is preferred, with advantages which may include lower energy usage, apparatus with fewer or no moving parts, and spray droplets of very regular and controllable size.

Abstract

Method of forming and spraying emulsions of two immiscible liquids by introducing small amounts of highly charged disperse phase into a body of continuous phase followed by direct electrostatic spraying of the charged emulsions so formed. Also apparatus therefor.

Description

  • This invention relates to spraying emulsions. More particularly, it relates to new processes for forming emulsions and spraying the emulsions so formed, and to apparatus therefor.
  • An emulsion consists of small particles (generally of mean diameter in the range 0.1 to 10 microns) of a first liquid dispersed in a second liquid immiscible therewith. For example, an emulsion may be formed of finely divided particles of oil in water; or conversely, of finely divided particles of water in oil, the latter being commonly referred to as an invert emulsion. An emulsion is a two- phase system; the particles constitute the disperse phase, while the medium in which they are suspended is the continuous phase. The propertiies of emulsions naturally depend on the properties of the two phases, their relative proportions and the particle size of the disperse phase. Dilute emulsions, containing for example up to 10% or so of disperse phase, generally have, for example, a viscosity not dissimilar from that of the continuous phase; but increasing the proportion of the disperse phase leads to thickening, and the formation of immobile, scarcely pourable systems. The present invention is concerned with relatively dilute emulsions, not too thick to be able to flowlike liquids.
  • Emulsions have a variety of uses; for example in the- food and pharmaceutical industries. Cosmetics may be formulated asemulsions, and so also may pesticides. The present invention relates to emulsions to be used as sprays.
  • Emulsions are generally formed by thoroughly agitating the two phases together, for example in a high shear mixer. This is a relatively inefficient process, consuming unnecessary energy.
  • Moreover, emulsions so formed are not necessarily stable, and may break down into separate bulk phases on storage. The present invention provides a more efficient method of forming emulsions, not dependent on mechanical mixing, and which prevents emulsion break-down by reducing or eliminating storage time.
  • According to the present invention we provide a process for forming and spraying a dilute emulsion of a first liquid in a second liquid immiscible therewith, which comprises passing small amounts of the first liquid into a body of the second liquid while electrically charging the first liquid relative to the second liquid to a potential sufficient to cause emulsification therein, and atomising the charged emulsion thereby formed. Such atomisation may be carried. out wholly or partly by mechanical means, but conveniently it may be effected by passing the charged emulsion into a region of high electrical field strength thereby causing it to atomise.
  • The invention further comprises apparatus for forming and spraying an electrically charged emulsion of a first liquid in a second liquid immiscible therewith which comprises an orifice formed in an electrically conducting material communicating with a vessel for containing the second liquid, means for delivering the first liquid to and through the orifice, means for charging the orifice to a high potential, and a sprayhead for receiving the electrically charged emulsion formed at the orifice and for emitting the emulsion in the form of an electrically charged spray. Conveniently the sprayhead comprises an electrically conducting surface for receiving the electrically charged emulsion, and means for creating a field strength at the surface sufficient to atomise the emulsion therefrom in the form of a fine spray.
  • The emulsions, being electrostatically charged, are attracted to spray targets and coat them more evenly than uncharged sprays would do. Electrostatic force fields carry the charged particles behind the target, so as to coat all sides of it. The method and apparatus of the invention may be used for spraying paints and like coatings on to structures or articles of manufacture, and (with particular advantage) for spraying pesticides (eg, insecticides, herbicides, fungicides and the like) on to crops or weeds. Conveniently emulsions according to the invention comprise from about 1 to about 10% by weight disperse phase, though higher and lower amounts may be used where appropriate.
  • A specific embodiment of the invention will now be described with reference to the drawings, in which:
    • Figure 1 is a vertical cross-section through a spraying device according to the invention adapted to spray an invert emulsion of aqueous herbicide in oil;
    • Figure 2 is a circuit diagram for the device;
    • Figure 3 is an alternative circuit diagram for the device.
  • In figure 1, a container 1 of insulating material (glass) is provided with an earthed jacket 13 of conductive material, and with a conduit 2 for delivering liquid. In the base of the container 1 is a metallic exit nozzle 3, with a bore of capillary.size. Below the container 1, and disposed symmetrically around the outlet of nozzle 3, is a metal ring 4 connected (as shown in Figure 2) to earth 19. Centrally within the upper part of the container 1 is a second container 5 of insulating material (glass) fed by a liquid delivering conduit 6. In the base of container 5 is a second metallic exit nozzle 7, of capillary dimensions. Both nozzles 3 and 7 are connected (as shown in Figure 2) to a source of high potential 8 (0-20 kilovolts, 200 microamp module) via a switch 9. Below the container 5, within the container 1, and symmetrically disposed around the outlet of the nozzle 7, is a second earthed metal ring. 10. The nozzle 3 may be closed by an exterior cap or bung 12.
  • In operation, a hydrocarbon oil 11 is passed into the container 1 from the conduit 2 until the level of oil 11 is above the base of container 5. An aqueous solution containing 7% by weight of paraquat dichloride is passed through conduit 6 into container 5. Capillary-sized droplets of the aqueous solution pass out through nozzle 7 and sink through the oil 11. The switch 9 is then closed, applying a voltage of the order of 15 kilovolts to the nozzles 7 and 3. At once the passage of capillary-sized droplets into the oil 11 ceases, and the oil becomes cloudy, indicating the formation of an emulsion. The liquid in the container 1 becomes turbulent, exhibiting negative surface tension due to the electrical charge it carries. The cap 12 is then removed, and the emulsion (containing about 4% weight disperse phase) issues from the nozzle 3. The electric field between the nozzle 3 and the earthed ring 4 causes the emulsion to atomise as fine particles, which pass outwards and are attracted to suitable targets, eg, weeds. Meanwhile the flows of oil 11 through conduit 2 and of aqueous solution through conduit 6 are adjusted to maintain the levels of liquid in containers 1 and 5 constant.
  • The particle size of the disperse phase in the emulsion may be controlled by control of the field strength at the nozzle 7; eg, by varying the distance between the nozzle 7 and the ring 10, or, more conveniently, by varying the applied voltage. The stronger the field the smaller are the droplets. Similarly, the particle size of droplets in the atomised emulsion may be controlled by control of the field strength at the nozzle 3. This may be done by varying the voltage on the nozzle 3, the position of the ring 4, or by applying a variable voltage (positive or negative with respect to the potential of the nozzle 3) to the ring 4 instead of earthing it.
  • The same apparatus may be used, if desired, to form an emulsion in which water or an aqueous solution is the continuous phase and oil is the disperse phase, by feeding water to container 1 and oil to container 2.
  • If desired, the nozzle 7 may be charged by induction, as shown in Figure 3. If the nozzle 7 is connected to the earth 19, and the source of potential 8 to ring 10, a strong charge of opposite sign will be induced on nozzle 7 and liquid passing through will be charged by contact in the same way as if the nozzle 7 were connected to source of potential 8, except that the charge will be of opposite sign. An emulsion will be formed in just the same way, with the charging current being taken from earth. This saves current at nozzle 7, but slightly more is used at nozzle3, because the emulsion has to be discharged and recharged in the opposite sense before atomisation. In any case the power consumption of the device is not high, and is readily adapted to use in portable devices powered by dry cells, or even solar cells. For agricultural spraying, however, it will often be convenient to mount the device on a vehicle (eg a tractor or aircraft) and power it from a power source carried on the vehicle (eg the tractor battery).
  • If desired, (eg to obtain a greater throughput rate than is normally conveniently available through electrostatic atomisation) the emulsion may be atomised wholly or partly mechanically, eg from a pressure nozzle or spinning cup or disc. Generally, however, electrostatic atomisation is preferred, with advantages which may include lower energy usage, apparatus with fewer or no moving parts, and spray droplets of very regular and controllable size.

Claims (10)

1. A process for forming and spraying a dilute emulsion of a first liquid in a second liquid immiscible therewith which comprises passing small amounts of the first liquid into a body of the second liquid while electrically charging the first liquid relative to the second liquid to a potential sufficient to cause emulsification therein, and atomising the charged emulsion thereby formed.
2. A process as claimed in claim 1 wherein atomisation is effected by passing the charged emulsion into a region of high electrical field strength.
3. A process as claimed in either of claims 1 or 2 wherein the first liquid comprises a pesticide.
4. Apparatus for carrying out the process of claim 1 which comprises an orifice formed in an electrically conducting material communicating with a vessel for containing the second liquid, means for delivering the first liquid to and through the orifice means for charging the orifice to a high potential and a sprayhead for receiving the electrically charged emulsion formed at the orifice and for emitting the emulsion in the form of an electrically charged spray.
5. Apparatus as claimed in claim 4 in which the sprayhead comprises an electrically conducting surface with means for creating a field strength at the surface sufficient to atomise the emulsion therefrom in the form of a fine spray.
6. Apparatus as claimed in claim 5 wherein the means for creating field strength at the surface comprises an electrode at a potential different from that of the surface.
7. Apparatus as claimed in claim 6 in which the electrode is earthed.
8. Apparatus as claimed in any of claims 4 to 6 which is provided with an electrode adjacent the orifice, and at a different potential therefrom, to intensify the electric field thereat.
9. Apparatus as claimed in claim 8 wherein the electrode adjacent the orifice is earthed.
10. Apparatus as claimed in any of claims 4 to 9 mounted on a vehicle and adapted for agricultural spraying.
EP81306005A 1981-01-30 1981-12-21 Process of spraying emulsions and apparatus thereof Expired EP0057324B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT81306005T ATE19597T1 (en) 1981-01-30 1981-12-21 METHOD AND DEVICE FOR SPRAYING EMULSIONS.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB8102823 1981-01-30
GB8102823 1981-01-31

Publications (2)

Publication Number Publication Date
EP0057324A1 true EP0057324A1 (en) 1982-08-11
EP0057324B1 EP0057324B1 (en) 1986-05-07

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ID=10519331

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EP81306005A Expired EP0057324B1 (en) 1981-01-30 1981-12-21 Process of spraying emulsions and apparatus thereof

Country Status (7)

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EP (1) EP0057324B1 (en)
JP (1) JPS57159564A (en)
AT (1) ATE19597T1 (en)
AU (1) AU7917082A (en)
CA (1) CA1176508A (en)
DE (1) DE3174591D1 (en)
NZ (1) NZ199410A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0356030A2 (en) * 1988-08-15 1990-02-28 United Kingdom Atomic Energy Authority A method of enhanced solvent Extraction and apparatus therefor
WO2002055211A1 (en) * 2001-01-12 2002-07-18 The Procter & Gamble Company Electrostatic spray device
US6682004B2 (en) 1999-08-18 2004-01-27 The Procter & Gamble Company Electrostatic spray device
US6814318B2 (en) 1999-08-18 2004-11-09 The Procter & Gamble Company Disposable cartridge for electrostatic spray device
US6860439B2 (en) 2002-03-01 2005-03-01 Unilever Home & Personal Care Usa, Division Of Conopco, Inc. Electrostatic spraying of a cosmetic composition
WO2007131917A1 (en) * 2006-05-15 2007-11-22 Unilever Plc Process for preparing an emulsion
US7712687B2 (en) 1999-08-18 2010-05-11 The Procter & Gamble Company Electrostatic spray device
CN110935338A (en) * 2019-09-24 2020-03-31 福建爱溥环保设备有限公司 Device and method for mixing oil and water into floccule

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4877173B2 (en) * 2007-09-21 2012-02-15 パナソニック電工株式会社 Electrostatic atomizer and heated air blower equipped with the same

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR639245A (en) * 1927-08-09 1928-06-16 Process for preparing emulsions by means of an electric charge
GB320919A (en) * 1928-06-19 1929-10-21 Provia Soc Improved process of and apparatus for making bituminous emulsions and distributing same on road surfaces
FR1017481A (en) * 1950-02-07 1952-12-11 Onera (Off Nat Aerospatiale) Improvements in means for the production of electrified particles, in particular electrified droplets
FR1087802A (en) * 1952-04-18 1955-03-01 Harper J Ransburg Company Process for coating objects by spraying and equipment for its implementation
FR1122243A (en) * 1955-01-07 1956-09-04 Bonnet Reymond Sa Advanced atomizer
FR1182266A (en) * 1957-04-15 1959-06-24 Automatic valve with emulsion pump
US3131131A (en) * 1962-04-03 1964-04-28 Socony Mobil Oil Co Inc Electrostatic mixing in microbial conversions
US3873023A (en) * 1972-09-18 1975-03-25 Ransburg Corp Apparatus for and method of spraying plural component materials
GB1564973A (en) * 1976-12-30 1980-04-16 Research Corp Electrostatic spray nozzle system
GB1569707A (en) * 1976-07-15 1980-06-18 Ici Ltd Atomisation of liquids

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR639245A (en) * 1927-08-09 1928-06-16 Process for preparing emulsions by means of an electric charge
GB320919A (en) * 1928-06-19 1929-10-21 Provia Soc Improved process of and apparatus for making bituminous emulsions and distributing same on road surfaces
FR1017481A (en) * 1950-02-07 1952-12-11 Onera (Off Nat Aerospatiale) Improvements in means for the production of electrified particles, in particular electrified droplets
FR1087802A (en) * 1952-04-18 1955-03-01 Harper J Ransburg Company Process for coating objects by spraying and equipment for its implementation
FR1122243A (en) * 1955-01-07 1956-09-04 Bonnet Reymond Sa Advanced atomizer
FR1182266A (en) * 1957-04-15 1959-06-24 Automatic valve with emulsion pump
US3131131A (en) * 1962-04-03 1964-04-28 Socony Mobil Oil Co Inc Electrostatic mixing in microbial conversions
US3873023A (en) * 1972-09-18 1975-03-25 Ransburg Corp Apparatus for and method of spraying plural component materials
GB1569707A (en) * 1976-07-15 1980-06-18 Ici Ltd Atomisation of liquids
GB1564973A (en) * 1976-12-30 1980-04-16 Research Corp Electrostatic spray nozzle system

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0356030A2 (en) * 1988-08-15 1990-02-28 United Kingdom Atomic Energy Authority A method of enhanced solvent Extraction and apparatus therefor
EP0356030A3 (en) * 1988-08-15 1990-09-05 United Kingdom Atomic Energy Authority A method of enhanced solvent extraction and apparatus therefor
US5022973A (en) * 1988-08-15 1991-06-11 United Kingdom Atomic Energy Authority Method of electrostatically enhanced solvent extraction and apparatus therefor
US6682004B2 (en) 1999-08-18 2004-01-27 The Procter & Gamble Company Electrostatic spray device
US6814318B2 (en) 1999-08-18 2004-11-09 The Procter & Gamble Company Disposable cartridge for electrostatic spray device
US7152817B2 (en) 1999-08-18 2006-12-26 The Procter & Gamble Company Electrostatic spray device
US7712687B2 (en) 1999-08-18 2010-05-11 The Procter & Gamble Company Electrostatic spray device
WO2002055211A1 (en) * 2001-01-12 2002-07-18 The Procter & Gamble Company Electrostatic spray device
CN1292840C (en) * 2001-01-12 2007-01-03 宝洁公司 Electrostatic spray device
US6860439B2 (en) 2002-03-01 2005-03-01 Unilever Home & Personal Care Usa, Division Of Conopco, Inc. Electrostatic spraying of a cosmetic composition
WO2007131917A1 (en) * 2006-05-15 2007-11-22 Unilever Plc Process for preparing an emulsion
CN110935338A (en) * 2019-09-24 2020-03-31 福建爱溥环保设备有限公司 Device and method for mixing oil and water into floccule

Also Published As

Publication number Publication date
JPS57159564A (en) 1982-10-01
EP0057324B1 (en) 1986-05-07
NZ199410A (en) 1985-08-16
AU7917082A (en) 1982-08-12
ATE19597T1 (en) 1986-05-15
CA1176508A (en) 1984-10-23
DE3174591D1 (en) 1986-06-12

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