WO2020238974A1 - 一种电场装置 - Google Patents

一种电场装置 Download PDF

Info

Publication number
WO2020238974A1
WO2020238974A1 PCT/CN2020/092672 CN2020092672W WO2020238974A1 WO 2020238974 A1 WO2020238974 A1 WO 2020238974A1 CN 2020092672 W CN2020092672 W CN 2020092672W WO 2020238974 A1 WO2020238974 A1 WO 2020238974A1
Authority
WO
WIPO (PCT)
Prior art keywords
electric field
anode
cathode
present
field anode
Prior art date
Application number
PCT/CN2020/092672
Other languages
English (en)
French (fr)
Inventor
唐万福
王大祥
段志军
邹永安
奚勇
Original Assignee
上海必修福企业管理有限公司
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
Priority claimed from PCT/CN2019/111813 external-priority patent/WO2020083096A1/zh
Application filed by 上海必修福企业管理有限公司 filed Critical 上海必修福企业管理有限公司
Priority to CN202090000584.1U priority Critical patent/CN218834819U/zh
Publication of WO2020238974A1 publication Critical patent/WO2020238974A1/zh

Links

Images

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/01—Pretreatment of the gases prior to electrostatic precipitation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/02—Plant or installations having external electricity supply
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34—Constructional details or accessories or operation thereof
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34—Constructional details or accessories or operation thereof
    • B03C3/38—Particle charging or ionising stations, e.g. using electric discharge, radioactive radiation or flames
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34—Constructional details or accessories or operation thereof
    • B03C3/40—Electrode constructions
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34—Constructional details or accessories or operation thereof
    • B03C3/40—Electrode constructions
    • B03C3/41—Ionising-electrodes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34—Constructional details or accessories or operation thereof
    • B03C3/40—Electrode constructions
    • B03C3/45—Collecting-electrodes
    • B03C3/49—Collecting-electrodes tubular
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/01—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust by means of electric or electrostatic separators
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02M—SUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M35/00—Combustion-air cleaners, air intakes, intake silencers, or induction systems specially adapted for, or arranged on, internal-combustion engines
    • F02M35/02—Air cleaners

Definitions

  • the invention belongs to the field of electric field technology, and specifically relates to an electric field device.
  • the electric field device includes an electric field anode and an electric field cathode.
  • the electric field anode is a hollow tube.
  • the electric field cathode passes through the electric field anode. Both ends of the electric field anode and the electric field cathode are flush.
  • the direction of the electric field is basically from the electric field cathode to the electric field anode.
  • the discharge efficiency and processing efficiency of this electric field structure are generally low, and the energy consumption is high.
  • There is also a coupling phenomenon in the existing electric field that is, charged materials will repeatedly circulate between the two electrodes of the electric field to form electric field coupling consumption, which leads to a decrease in the efficiency of electric field processing and an increase in energy consumption.
  • the existing electric field devices have defects such as large size, high energy consumption, and low processing efficiency.
  • the purpose of the present invention is to provide an electric field device to solve at least one of the technical problems of the existing electric field device such as large power consumption, large volume, high cost, and low processing efficiency.
  • Example 1 provided by the present invention: an electric field device comprising an electric field device inlet, an electric field device outlet, an electric field cathode and an electric field anode, the electric field cathode and the electric field anode are used to generate an ionizing electric field.
  • Example 2 provided by the present invention: including the above example 1, wherein the electric field device further includes an electric field device inlet and an electric field device outlet; the electric field anode includes a first anode portion and a second anode portion, the first anode The part is close to the entrance of the electric field device, the second anode part is close to the outlet of the electric field device, and at least one cathode support plate is arranged between the first anode part and the second anode part.
  • Example 3 provided by the present invention: including the above example 1 or 2, wherein the electric field device further includes an insulation mechanism for achieving insulation between the cathode support plate and the electric field anode.
  • Example 4 provided by the present invention: including the above example 3, wherein an electric field channel is formed between the electric field anode and the electric field cathode, and the insulating mechanism is arranged outside the electric field channel.
  • Example 5 provided by the present invention: including the above example 3 or 4, wherein the insulating mechanism includes an insulating part and a heat insulating part; the material of the insulating part is a ceramic material or a glass material.
  • Example 6 provided by the present invention: including the above example 5, wherein the insulating portion is an umbrella-shaped string ceramic column, an umbrella-shaped string glass column, a columnar string ceramic column or a columnar glass column, with glaze on the inside and outside of the umbrella or the inside and outside of the column.
  • the insulating portion is an umbrella-shaped string ceramic column, an umbrella-shaped string glass column, a columnar string ceramic column or a columnar glass column, with glaze on the inside and outside of the umbrella or the inside and outside of the column.
  • Example 7 provided by the present invention: including the above example 6, wherein the distance between the outer edge of the umbrella string ceramic column or the umbrella string glass column and the electric field anode is more than 1.4 times the electric field distance, and the umbrella string ceramic column Or the sum of the pitch of the umbrella ledge of the umbrella-shaped glass column is more than 1.4 times the insulation distance of the umbrella-shaped ceramic column or umbrella-shaped glass column.
  • the total length of the umbrella edge of the umbrella-shaped ceramic column or umbrella-shaped glass column is the umbrella.
  • the insulation distance of the shaped string ceramic column or umbrella string glass column is more than 1.4 times.
  • Example 8 provided by the present invention: includes any one of the above examples 2 to 7, wherein the length of the first anode portion is 1/10 to 1/4, 1/4 to the length of the electric field anode 1/3, 1/3 to 1/2, 1/2 to 2/3, 2/3 to 3/4, or 3/4 to 9/10.
  • Example 9 provided by the present invention: includes any one of the above examples 2 to 8, wherein the length of the first anode part is long enough to remove some dust and reduce accumulation in the insulation mechanism and The dust on the cathode support plate reduces the electric breakdown caused by the dust.
  • Example 10 provided by the present invention includes any one of the foregoing examples 1 to 9, wherein the electric field cathode includes at least one electrode rod.
  • Example 11 provided by the present invention: including the above example 10, wherein the diameter of the electrode rod is not greater than 3 mm.
  • Example 12 provided by the present invention: including the above examples 10 or 11, wherein the shape of the electrode rod is needle, polygon, burr, threaded rod or column.
  • Example 13 provided by the present invention: including any one of the above examples 1 to 12, wherein the electric field anode is composed of a hollow tube bundle.
  • Example 14 provided by the present invention: includes any one of the above examples 13, wherein the diameter of the tube inscribed circle of the hollow tube bundle ranges from 5 mm to 400 mm.
  • Example 15 provided by the present invention: including the above examples 13 or 14, wherein the hollow cross section of the electric field anode tube bundle is circular or polygonal.
  • Example 16 provided by the present invention: includes the above example 15, wherein the polygon is a hexagon.
  • Example 17 provided by the present invention includes any one of the above examples 13 to 16, wherein the tube bundle of the electric field anode is in a honeycomb shape.
  • Example 18 provided by the present invention includes any one of the foregoing examples 1 to 17, wherein the electric field cathode penetrates the electric field anode.
  • Example 19 provided by the present invention: includes any one of the foregoing Examples 1 to 18, wherein the electric field device further includes an auxiliary electric field unit for generating an auxiliary electric field that is not parallel to the ionization electric field.
  • Example 20 includes any one of the above examples 1 to 18, wherein the electric field device further includes an auxiliary electric field unit, the ionization electric field includes a flow channel, and the auxiliary electric field unit is used to generate and The auxiliary electric field where the flow channel is not vertical.
  • Example 21 provided by the present invention: includes the above examples 19 or 20, wherein the auxiliary electric field unit includes a first electrode, and the first electrode of the auxiliary electric field unit is arranged at or near the entrance of the ionization electric field.
  • Example 22 provided by the present invention: including the above example 21, wherein the first electrode is a cathode.
  • Example 23 provided by the present invention: including the above example 21 or 22, wherein the first electrode of the auxiliary electric field unit is an extension of the electric field cathode.
  • Example 25 includes any one of the foregoing Examples 19 to 24, wherein the auxiliary electric field unit includes a second electrode, and the second electrode of the auxiliary electric field unit is arranged at or near the ionization electric field The exit.
  • Example 26 provided by the present invention: including the above example 25, wherein the second electrode is an anode.
  • Example 27 provided by the present invention: including the above example 25 or 26, wherein the second electrode of the auxiliary electric field unit is an extension of the electric field anode.
  • Example 29 provided by the present invention: includes any one of the foregoing Examples 19 to 22, wherein the first electrode of the auxiliary electric field unit and the electric field anode and the electric field cathode of the ionization electric field are arranged independently.
  • Example 30 provided by the present invention: includes any one of the foregoing Examples 19 to 20, 25, and 26, wherein the second electrode of the auxiliary electric field unit and the electric field anode and the electric field cathode of the ionization electric field are independently arranged.
  • Example 31 provided by the present invention: includes any one of the foregoing examples 1 to 30, wherein the ratio of the working area of the electric field anode to the discharge area of the electric field cathode is 1.667:1 to 1680:1.
  • Example 32 provided by the present invention: includes any one of the foregoing examples 1 to 31, wherein the ratio of the working area of the electric field anode to the discharge area of the electric field cathode is 6.67:1 to 56.67:1.
  • Example 33 includes any one of the foregoing Examples 1 to 32, wherein the diameter of the electric field cathode is 1-3 mm, and the distance between the electric field anode and the electric field cathode is 2.5-139.9 Mm; the ratio of the working area of the electric field anode to the discharge area of the electric field cathode is 1.667:1 to 1680:1.
  • Example 34 provided by the present invention: includes any one of the foregoing Examples 1 to 33, wherein the distance between the electric field anode and the electric field cathode is less than 150 mm.
  • Example 35 includes any one of the foregoing Examples 1 to 34, wherein the distance between the electric field anode and the electric field cathode is 2.5-139.9 mm.
  • Example 36 provided by the present invention: includes any one of the foregoing Examples 1 to 35, wherein the distance between the electric field anode and the electric field cathode is 5-100 mm.
  • Example 37 provided by the present invention: includes any one of the foregoing Examples 1 to 36, wherein the length of the electric field anode is 10-180 mm.
  • Example 38 provided by the present invention: includes any one of the foregoing Examples 1 to 37, wherein the length of the electric field anode is 60-180 mm.
  • Example 39 provided by the present invention: includes any one of the foregoing Examples 1 to 36, wherein the length of the electric field anode is 10-90 mm.
  • Example 40 provided by the present invention: includes any one of the foregoing Examples 1 to 39, wherein the length of the electric field cathode is 30-180 mm.
  • Example 41 provided by the present invention: includes any one of the foregoing Examples 1 to 40, wherein the length of the electric field cathode is 54-176 mm.
  • Example 42 provided by the present invention: includes any one of the foregoing Examples 1 to 39, wherein the length of the electric field cathode is 10-90 mm.
  • Example 43 provided by the present invention: includes any one of the foregoing Examples 31 to 41, wherein, when operating, the number of coupling times of the ionization electric field is ⁇ 3.
  • Example 44 provided by the present invention: includes any one of the foregoing Examples 19 to 41, wherein, when operating, the number of coupling times of the ionization electric field is ⁇ 3.
  • Example 45 provided by the present invention: includes any one of the above examples 1 to 41, wherein the ratio of the working area of the electric field anode to the discharge area of the electric field cathode, the electric field anode and the electric field cathode The distance between the poles, the length of the electric field anode and the length of the electric field cathode make the coupling times of the ionization electric field ⁇ 3.
  • Example 46 provided by the present invention: includes any one of the foregoing Examples 1 to 45, wherein the value range of the ionization electric field voltage is 1kv-50kv.
  • Example 47 provided by the present invention: includes any one of the foregoing Examples 1 to 46, wherein the electric field device includes a plurality of electric field stages, and each of the electric field stages includes a plurality of electric field generating units, and the electric field generating units There may be one or more; the electric field generating unit includes the electric field anode and the electric field cathode.
  • Example 48 provided by the present invention: includes the above example 47, wherein, when there are more than two electric field levels, the electric field levels are connected in series.
  • Example 49 includes any one of the foregoing Examples 1 to 48, wherein the electric field device further includes a plurality of connecting housings, and the series electric field stages are connected through the connecting housings.
  • Example 50 provided by the present invention: includes the above example 49, wherein the distance between adjacent electric field levels is more than 1.4 times the distance between the electric field anode and the electric field cathode.
  • Example 51 includes any one of the foregoing Examples 1 to 50, wherein the electric field device further comprises a front electrode, and the front electrode is connected to the electric field anode and the entrance of the electric field device. Between the ionizing electric field formed by the electric field cathode.
  • Example 52 provided by the present invention: includes the above example 51, wherein the front electrode is in the shape of a surface, a mesh, a plate, or a plate.
  • Example 53 provided by the present invention: includes the above example 51 or 52, wherein at least one through hole is provided on the front electrode.
  • Example 54 provided by the present invention: includes the above example 53, wherein the through hole is polygonal, circular, oval, square, rectangular, trapezoidal, or rhombus.
  • Example 55 provided by the present invention: includes the above example 53 or 54, wherein the aperture of the through hole is 0.1-3 mm.
  • Example 56 includes any one of the foregoing Examples 51 to 55, wherein the front electrode is a combination of one or more of solid, liquid, gaseous molecular clusters, or plasma .
  • Example 57 provided by the present invention: includes any one of the foregoing Examples 51 to 56, wherein the front electrode is a conductive mixed state material, a biological body naturally mixes a conductive material, or an object is artificially processed to form a conductive material.
  • Example 58 provided by the present invention: includes any one of the foregoing Examples 51 to 57, wherein the front electrode is 304 steel or graphite.
  • Example 59 provided by the present invention: includes any one of the foregoing Examples 51 to 57, wherein the front electrode is an ion-containing conductive liquid.
  • Example 60 provided by the present invention: includes any one of the foregoing Examples 51 to 59, wherein the front electrode is perpendicular to the electric field anode.
  • Example 61 provided by the present invention: includes any one of the foregoing Examples 51 to 60, wherein the front electrode is parallel to the electric field anode.
  • Example 62 provided by the present invention: includes any one of the foregoing Examples 51 to 61, wherein the front electrode adopts a metal wire mesh.
  • Example 63 provided by the present invention: includes any one of the foregoing Examples 51 to 62, wherein the voltage between the front electrode and the electric field anode is different from that between the electric field cathode and the electric field anode The voltage.
  • Example 64 provided by the present invention: includes any one of the foregoing Examples 51 to 63, wherein the voltage between the front electrode and the electric field anode is less than the initial corona initiation voltage.
  • Example 65 provided by the present invention: includes any one of the foregoing Examples 51 to 64, wherein the voltage between the front electrode and the electric field anode is 0.1-2 kv/mm.
  • Example 66 provided by the present invention: includes any one of the foregoing Examples 51 to 65, wherein the electric field device includes a flow channel, the front electrode is located in the flow channel; the cross-sectional area of the front electrode The cross-sectional area ratio of the flow channel is 99%-10%, or 90-10%, or 80-20%, or 70-30%, or 60-40%, or 50%.
  • Example 67 provided by the present invention: A method for reducing the coupling of dust removal electric field, including the following steps:
  • Example 68 provided by the present invention: including Example 67, including selecting the ratio of the working area of the electric field anode to the discharge area of the electric field cathode.
  • Example 69 provided by the present invention: includes Example 68, wherein the ratio of the working area of the electric field anode to the discharge area of the electric field cathode is selected to be 1.667:1 to 1680:1.
  • Example 70 provided by the present invention includes Example 68, wherein the ratio of the working area of the electric field anode to the discharge area of the electric field cathode is selected to be 6.67:1 to 56.67:1.
  • Example 71 provided by the present invention: includes any one of Examples 67 to 70, including selecting the electric field cathode to have a diameter of 1-3 mm, and the distance between the electric field anode and the electric field cathode to be 2.5-139.9 mm
  • the ratio of the working area of the electric field anode to the discharge area of the electric field cathode is 1.667:1 to 1680:1.
  • Example 72 provided by the present invention: includes any one of Examples 67 to 71, wherein the distance between the electric field anode and the electric field cathode is selected to be less than 150 mm.
  • Example 73 provided by the present invention: includes any one of Examples 67 to 71, wherein the distance between the electric field anode and the electric field cathode is selected to be 2.5-139.9 mm.
  • Example 74 provided by the present invention: includes any one of Examples 67 to 71, including selecting the distance between the electric field anode and the electric field cathode to be 5-100 mm.
  • Example 75 provided by the present invention: including any one of Examples 67 to 74, including selecting the electric field anode length to be 10-180 mm.
  • Example 76 provided by the present invention: includes any one of Examples 67 to 74, including selecting the electric field anode length to be 60-180 mm.
  • Example 77 provided by the present invention: including any one of Examples 67 to 76, including selecting the electric field cathode length to be 30-180 mm.
  • Example 78 provided by the present invention: includes any one of Examples 67 to 76, including selecting the electric field cathode length to be 54-176 mm.
  • Example 79 provided by the present invention: includes any one of Examples 67 to 78, wherein it includes selecting that the electric field cathode includes at least one electrode rod.
  • Example 80 provided by the present invention: includes Example 79, which includes selecting the electrode rod to have a diameter not greater than 3 mm.
  • Example 81 provided by the present invention: includes Example 79 or 80, which includes selecting the shape of the electrode rod to be needle-shaped, polygonal, burr-shaped, threaded rod-shaped, or columnar.
  • Example 82 provided by the present invention: including any one of Examples 67 to 81, including selecting that the electric field anode is composed of a hollow tube bundle.
  • Example 83 provided by the present invention: including Example 82, wherein the diameter of the tube inscribed circle including the hollow tube bundle is selected in the range of 5mm-400mm.
  • Example 84 provided by the present invention: including Example 83, wherein the hollow section including the selection of the anode tube bundle is circular or polygonal.
  • Example 85 provided by the present invention: includes Example 84, which includes selecting the polygon as a hexagon.
  • Example 86 provided by the present invention: includes any one of Examples 82 to 85, wherein the tube bundle including the selection of the electric field anode is in a honeycomb shape.
  • Example 87 provided by the present invention: includes any one of Examples 67 to 86, wherein it includes selecting the electric field cathode to penetrate into the electric field anode.
  • Example 88 provided by the present invention: includes any one of Examples 67 to 87, wherein the size of the electric field anode or/and the electric field cathode is selected such that the number of electric field couplings is ⁇ 3.
  • the electric field device provided by the invention can be applied to the technical field of gas dust removal, and can effectively remove nanoparticles in the air.
  • FIG. 1 is a schematic diagram of the structure of an electric field device in Embodiment 1 of the present invention.
  • FIG. 2 is a schematic diagram of the structure of the electric field generating unit in the embodiment 2-11 and the embodiment 24-27 of the present invention.
  • Fig. 3 is an A-A view of the electric field generating unit of Fig. 2 in embodiment 2, embodiment 5, and embodiment 27 of the present invention.
  • Fig. 4 is an A-A view of the electric field generating unit of Fig. 2 with length and angle marked in embodiment 2 and embodiment 5 of the present invention.
  • Embodiment 5 is a schematic diagram of the structure of the electric field device with two electric field levels in Embodiment 2, Embodiment 5, and Embodiment 27 of the present invention.
  • Embodiment 12 is a schematic diagram of the structure of an electric field device in Embodiment 12 of the present invention.
  • FIG. 7 is a schematic structural diagram of an electric field device in Embodiment 14 of the present invention.
  • FIG. 8 is a schematic structural diagram of an electric field device in Embodiment 15 of the present invention.
  • FIG. 9 is a schematic structural diagram of an electric field device in Embodiment 16 of the present invention.
  • an electric field device which includes an electric field device inlet, an electric field device outlet, an electric field cathode, and an electric field anode.
  • the electric field cathode and the electric field anode are used to generate an ionizing electric field.
  • the electric field cathode includes a plurality of cathode wires.
  • the diameter of the cathode wire can be 0.1mm-20mm, and the size parameter can be adjusted according to the application and processing requirements. In an embodiment of the present invention, the diameter of the cathode wire is not greater than 3 mm.
  • the cathode wire uses a metal wire or an alloy wire that is easy to discharge, is temperature-resistant, can support its own weight, and is electrochemically stable.
  • the material of the cathode wire is titanium. The specific shape of the cathode wire is adjusted according to the shape of the electric field anode.
  • the cathode wire For example, if the working surface of the electric field anode is flat, the cross section of the cathode wire is circular; if the working surface of the electric field anode is circular, the cathode wire needs to be designed in a multi-faceted shape . The length of the cathode wire is adjusted according to the electric field anode.
  • the electric field cathode includes a plurality of cathode rods.
  • the diameter of the cathode rod is not greater than 3 mm.
  • the cathode rod uses a metal rod or alloy rod that is easy to discharge.
  • the shape of the cathode rod can be needle-like, polygonal, burr-like, threaded rod-like or column-like. The shape of the cathode rod can be adjusted according to the shape of the electric field anode.
  • the cross section of the cathode rod needs to be designed to be circular; if the working surface of the electric field anode is an arc surface, the cathode rod needs to be Designed into a multi-faceted shape.
  • the electric field cathode is penetrated in the electric field anode.
  • the electric field anode includes one or more hollow anode tubes arranged in parallel. When there are multiple hollow anode tubes, all the hollow anode tubes constitute a honeycomb electric field anode.
  • the cross section of the hollow anode tube may be circular or polygonal. In an embodiment of the present invention, the cross section of the hollow anode tube is a polygon, and the polygon is a hexagon. If the cross section of the hollow anode tube is circular, a uniform electric field can be formed between the electric field anode and the electric field cathode.
  • the diameter of the tube inscribed circle of the hollow anode tube ranges from 5 mm to 400 mm.
  • the electric field cathode is installed on the cathode support plate, and the cathode support plate and the electric field anode are connected by an insulating mechanism.
  • the insulation mechanism is used to achieve insulation between the cathode support plate and the electric field anode.
  • the electric field anode includes a first anode part and a second anode part, that is, the first anode part is close to the inlet of the electric field device, and the second anode part is close to the outlet of the electric field device.
  • the cathode support plate and the insulation mechanism are between the first anode part and the second anode part, that is, the insulation mechanism is installed in the middle of the ionization electric field or the middle of the electric field cathode, which can support the electric field cathode and play a good role in the electric field cathode. Relative to the fixing effect of the electric field anode, the electric field cathode and the electric field anode maintain a set distance. In the prior art, the support point of the cathode is at the end of the cathode, and it is difficult to maintain the distance between the cathode and the anode.
  • the insulation mechanism is arranged outside the electric field flow channel, that is, outside the electric field flow channel, to prevent or reduce dust in the gas from gathering on the insulation mechanism, causing the insulation mechanism to break down or conduct electricity.
  • the insulation mechanism adopts a high-voltage resistant ceramic insulator to insulate the electric field cathode and the electric field anode.
  • the electric field anode is also called a kind of housing.
  • the insulating mechanism includes insulating ceramic pillars.
  • the length of the first anode portion occupies 1/10 to 1/4, 1/4 to 1/3, 1/3 to 1/2, 1/2 to 2/3 of the total length of the electric field anode. 2/3 to 3/4, or 3/4 to 9/10.
  • the second anode part is located behind the cathode support plate and the insulating mechanism in the gas flow direction.
  • the first anode part and the second anode part may use different power sources.
  • the insulating mechanism is arranged outside the electric field flow channel between the electric field cathode and the electric field anode. Therefore, the insulation mechanism is suspended outside the electric field anode.
  • the insulating mechanism may be made of non-conductor temperature-resistant materials, such as ceramics, glass, and the like.
  • the material insulation that is completely airtight and air-free requires an insulation isolation thickness of >0.3mm/kv; air insulation requires >1.4mm/kv.
  • the insulation distance can be set at more than 1.4 times the distance between the electric field cathode and the electric field anode.
  • the insulating mechanism uses ceramics, and the surface is glazed; adhesives or organic materials cannot be used to fill the connection, and the temperature resistance is greater than 350 degrees Celsius.
  • the insulation mechanism includes an insulation part and a heat insulation part.
  • the material of the insulating part is ceramic material or glass material.
  • the insulating part may be an umbrella-shaped string of ceramic pillars or glass pillars with glaze on the inside and outside of the umbrella.
  • the distance between the outer edge of the umbrella string ceramic column or the glass column and the electric field anode is greater than or equal to 1.4 times the electric field distance, that is, greater than or equal to 1.4 times the electrode pitch.
  • the sum of the pitches of umbrella protrusions of the umbrella string ceramic columns or glass columns is greater than or equal to 1.4 times the insulation pitch of the umbrella string ceramic columns.
  • the total inner depth of the umbrella side of the umbrella string ceramic column or the glass column is greater than or equal to 1.4 times the insulation distance of the umbrella string ceramic column.
  • the insulating part can also be a columnar string of ceramic columns or glass columns with glaze on the inside and outside of the columns. In an embodiment of the present invention, the insulating portion may also be tower-shaped.
  • a heating rod is arranged in the insulating part, and when the temperature around the insulating part approaches the dew point, the heating rod is activated and heated. Due to the temperature difference between the inside and outside of the insulating part during use, condensation is likely to occur on the inside and outside of the insulating part.
  • the outer surface of the insulating part may spontaneously or be heated by gas to generate high temperature, and necessary isolation protection is required to prevent burns.
  • the insulation part includes a protective enclosure located outside the insulation part.
  • the end of the insulating part that needs condensation location also needs to be insulated to prevent the environment and the heat dissipation high temperature heating condensation component.
  • the lead wires of the power supply of the electric field device are connected through the wall using umbrella-shaped string ceramic pillars or glass pillars, using elastic contacts to connect the cathode support plate in the wall, and plugging and unplugging the sealed insulating protective wiring cap outside the wall.
  • the insulation distance between the lead wire and the wall conductor and the wall is greater than the ceramic insulation distance of the umbrella string ceramic column or glass column.
  • the high voltage part removes the lead wire and is directly installed on the end to ensure safety.
  • the overall external insulation of the high voltage module is protected by ip68, and the medium is used for heat exchange and heat dissipation.
  • the electric field anode and the electric field cathode are respectively electrically connected to the two electrodes of the power supply.
  • the voltage applied to the electric field anode and the electric field cathode needs to select an appropriate voltage level.
  • the specific voltage level selected depends on the volume, temperature resistance, and dust holding rate of the electric field device.
  • the voltage is from 1kv to 50kv; first consider the temperature resistance conditions when designing, the parameters of the pole spacing and temperature: 1MM ⁇ 30 degrees, the working area is greater than 0.1 square / thousand cubic meters / hour, the electric field length is greater than 5 times of the inscribed circle of the single tube , Control the flow velocity of the electric field to be less than 9 m/s.
  • the electric field anode is composed of a hollow anode tube and has a honeycomb shape.
  • the shape of the hollow anode tube port can be circular or polygonal.
  • the inscribed circle of the hollow anode tube ranges from 5-400mm, the corresponding voltage is between 0.1-120kv, and the corresponding current of the hollow anode tube is between 0.1-30A; different inscribed circles correspond to different The corona voltage is about 1KV/1MM.
  • the electric field device includes an electric field stage, the electric field stage includes a plurality of electric field generating units, and there may be one or more electric field generating units.
  • the electric field generating unit includes the electric field anode and the electric field cathode, and there are one or more electric field generating units.
  • the electric field device When there are multiple electric field levels, the ionization efficiency of the electric field device can be effectively improved.
  • each electric field anode has the same polarity, and each electric field cathode has the same polarity.
  • the electric field levels are connected in series.
  • the electric field device further includes a plurality of connecting shells, and the series electric field stages are connected by the connecting shells; the distance between the electric field stages of two adjacent stages is more than 1.4 times the pole pitch.
  • the inventor of the present invention has discovered through research that the disadvantages of poor ionization efficiency and high energy consumption of existing electric field devices are caused by the above-mentioned electric field coupling phenomenon.
  • the size (ie, volume) of the electric field device can be significantly reduced by reducing the number of electric field couplings.
  • an asymmetric structure is adopted between the electric field cathode and the electric field anode.
  • polar particles are subjected to a force of the same magnitude but opposite in direction, and the polar particles reciprocate in the electric field; in an asymmetric electric field, the polar particles are subjected to two different forces, and the polar particles act towards Move in the direction of great force to avoid coupling.
  • an electric field device which includes an electric field device inlet, an electric field device outlet, an electric field cathode, and an electric field anode, where the electric field cathode and the electric field anode are used to generate an ionizing electric field;
  • the ratio of the working area of the electric field anode to the discharge area of the electric field cathode is 1.667:1 to 1680:1.
  • the ratio of the working area of the electric field anode to the discharge area of the electric field cathode is 6.67:1 to 56.67:1.
  • the ratio of the working area of the electric field anode to the discharge area of the electric field cathode is such that the coupling times of the ionization electric field are ⁇ 3.
  • the ratio of the working area of the electric field anode to the discharge area of the electric field cathode, the distance between the electric field anode and the electric field cathode, the length of the electric field anode, and the electric field makes the coupling times of the ionization electric field ⁇ 3.
  • the electric field device of the present invention forms an ionizing electric field between the electric field cathode and the electric field anode.
  • the method for reducing electric field coupling includes the following steps: selecting the ratio of the working area of the electric field anode to the discharge area of the electric field cathode so that the number of electric field couplings is ⁇ 3.
  • the ratio of the working area of the electric field anode to the discharge area of the electric field cathode may be: 1.667:1 to 1680:1; 3.334:1 to 13.34:1; 6.67: 1-56.67:1; 13.34:1 -28.33:1.
  • This embodiment selects the working area of a relatively large electric field anode and the discharge area of a relatively small electric field cathode.
  • the specific selection of the above area ratio can reduce the discharge area of the electric field cathode, reduce the suction force, expand the area of the electric field anode, and expand the suction force. , That is, an asymmetric electrode attraction is generated between the electric field cathode and the electric field anode, so that negative ions or substances with negative ions fall on the surface of the electric field anode, although the polarity is changed, but can no longer be absorbed by the electric field cathode, and the electric field coupling is reduced to realize the electric field coupling Times ⁇ 3.
  • the working area refers to the area of the working surface of the electric field anode.
  • the working area is the inner surface area of the hollow regular hexagonal tube.
  • the discharge area refers to the area of the working surface of the electric field cathode.
  • the electric field cathode is rod-shaped, the discharge area is the rod-shaped outer surface area.
  • Negative ions include any negative ions or negative ion-bearing substances such as oxygen ions obtained after oxygen is ionized, nitrogen ions obtained after nitrogen is ionized.
  • an electric field device which includes an electric field device inlet, an electric field device outlet, an electric field cathode, and an electric field anode.
  • the electric field cathode and the electric field anode are used to generate an ionizing electric field; the length of the electric field anode is 10-180mm.
  • the length of the electric field anode is 60-180 mm.
  • the length of the electric field anode is such that the coupling times of the ionization electric field are ⁇ 3.
  • an electric field device which includes an electric field device inlet, an electric field device outlet, an electric field cathode, and an electric field anode.
  • the electric field cathode and the electric field anode are used to generate an ionizing electric field; the length of the electric field cathode is 30-180mm.
  • the length of the electric field cathode is 54-176 mm.
  • the length of the electric field anode is such that the number of coupling times of the ionization electric field is ⁇ 3.
  • an electric field device which includes an electric field device inlet, an electric field device outlet, an electric field cathode, and an electric field anode.
  • the electric field cathode and the electric field anode are used to generate an ionizing electric field; the electric field anode and the electric field
  • the electrode spacing of the electric field cathode is less than 150mm.
  • the distance between the electric field anode and the electric field cathode is 2.5-139.9 mm.
  • the distance between the electric field anode and the electric field cathode is 5-100 mm.
  • the distance between the electric field anode and the electric field cathode is such that the coupling times of the ionization electric field are ⁇ 3.
  • the length of the electric field anode can be 10-180mm, 10-20mm, 20-30mm, 60-180mm, 30-40mm, 40-50mm, 50-60mm, 60-70mm, 70-80mm, 80mm. -90mm, 90-100mm, 100-110mm, 110-120mm, 120-130mm, 130-140mm, 140-150mm, 150-160mm, 160-170mm, 170-180mm, 60mm, 180mm, 10mm or 30mm.
  • the length of the electric field anode refers to the minimum length from one end to the other end of the working surface of the electric field anode. Choosing this length of the electric field anode can effectively reduce the electric field coupling.
  • the length of the electric field anode may be 10-90mm, 15-20mm, 20-25mm, 25-30mm, 30-35mm, 35-40mm, 40-45mm, 45-50mm, 50-55mm, 55mm. -60mm, 60-65mm, 65-70mm, 70-75mm, 75-80mm, 80-85mm or 85-90mm.
  • the design of this length can make the electric field anode and electric field device have high temperature resistance characteristics, and make the electric field device at high temperature High efficiency processing capacity under impact.
  • the length of the electric field cathode may be 30-180mm, 54-176mm, 30-40mm, 40-50mm, 50-54mm, 54-60mm, 60-70mm, 70-80mm, 80-90mm, 90mm. -100mm, 100-110mm, 110-120mm, 120-130mm, 130-140mm, 140-150mm, 150-160mm, 160-170mm, 170-176mm, 170-180mm, 54mm, 180mm, or 30mm.
  • the length of the electric field cathode refers to the minimum length from one end to the other end of the working surface of the electric field cathode. Choosing this length of the electric field cathode can effectively reduce electric field coupling.
  • the length of the electric field cathode may be 10-90mm, 15-20mm, 20-25mm, 25-30mm, 30-35mm, 35-40mm, 40-45mm, 45-50mm, 50-55mm, 55mm. -60mm, 60-65mm, 65-70mm, 70-75mm, 75-80mm, 80-85mm or 85-90mm.
  • the design of this length can make the electric field cathode and electric field device have high temperature resistance characteristics, and make the electric field device at high temperature High efficiency processing capacity under impact.
  • the distance between the electric field anode and the electric field cathode may be 5-30mm, 2.5-139.9mm, 9.9-139.9mm, 2.5-9.9mm, 9.9-20mm, 20-30mm, 30-40mm, 40mm. -50mm, 50-60mm, 60-70mm, 70-80mm, 80-90mm, 90-100mm, 100-110mm, 110-120mm, 120-130mm, 130-139.9mm, 9.9mm, 139.9mm, or 2.5mm.
  • the distance between the anode of the electric field and the cathode of the electric field is also referred to as the electrode pitch.
  • the pole distance specifically refers to the minimum vertical distance between the working surfaces of the electric field anode and the electric field cathode. The selection of this pole spacing can effectively reduce the electric field coupling and make the electric field device have high temperature resistance characteristics.
  • the diameter of the electric field cathode is 1-3 mm, and the distance between the electric field anode and the electric field cathode is 2.5-139.9 mm; the working area of the electric field anode is equal to that of the electric field cathode.
  • the ratio of the discharge area is 1.667:1 to 1680:1.
  • the present invention provides a method for reducing electric field coupling, including the following steps:
  • the electric field anode or/and the electric field cathode are selected.
  • the size of the electric field anode or/and the electric field cathode is selected such that the number of electric field couplings is ⁇ 3.
  • the ratio of the working area of the electric field anode to the discharge area of the electric field cathode is selected.
  • the ratio of the working area of the electric field anode to the discharge area of the electric field cathode is selected to be 1.667:1 to 1680:1.
  • the ratio of the working area of the electric field anode to the discharge area of the electric field cathode is selected to be 6.67-56.67:1.
  • the diameter of the electric field cathode is 1-3 mm, and the distance between the electric field anode and the electric field cathode is 2.5-139.9 mm; the working area of the electric field anode is equal to that of the electric field cathode.
  • the ratio of the discharge area is 1.667:1 to 1680:1.
  • the distance between the electric field anode and the electric field cathode is selected to be less than 150 mm.
  • the distance between the electric field anode and the electric field cathode is selected to be 2.5-139.9 mm. More preferably, the distance between the electric field anode and the electric field cathode is selected to be 5.0-100 mm.
  • the length of the electric field anode is selected to be 10-180 mm. More preferably, the length of the electric field anode is selected to be 60-180 mm.
  • the length of the electric field cathode is selected to be 30-180 mm. More preferably, the length of the electric field cathode is selected to be 54-176 mm.
  • the electric field device further includes an auxiliary electric field unit for generating an auxiliary electric field that is not parallel to the ionization electric field.
  • the electric field device further includes an auxiliary electric field unit, the ionization electric field includes a flow channel, and the auxiliary electric field unit is used to generate an auxiliary electric field that is not perpendicular to the flow channel.
  • the auxiliary electric field unit includes a first electrode, and the first electrode of the auxiliary electric field unit is disposed at or near the entrance of the ionization electric field.
  • the first electrode is a cathode.
  • the first electrode of the auxiliary electric field unit is an extension of the electric field cathode.
  • the auxiliary electric field unit includes a second electrode, and the second electrode of the auxiliary electric field unit is disposed at or near the outlet of the ionization electric field.
  • the second electrode is an anode.
  • the second electrode of the auxiliary electric field unit is an extension of the electric field anode.
  • the electrode of the auxiliary electric field and the electrode of the ionization electric field are arranged independently.
  • the ionizing electric field between the electric field anode and the electric field cathode is also called the first electric field.
  • a second electric field that is not parallel to the first electric field is formed between the electric field anode and the electric field cathode.
  • the flow channel of the second electric field and the ionization electric field are not perpendicular.
  • the second electric field is also called an auxiliary electric field, and can be formed by one or two auxiliary electrodes.
  • the auxiliary electrode can be placed at the entrance or exit of the ionizing electric field, and the auxiliary electrode can be charged with a negative potential, Or positive potential.
  • the auxiliary electrode When the second electric field is formed by two auxiliary electrodes, one of the auxiliary electrodes can have a negative potential and the other auxiliary electrode can have a positive potential; one auxiliary electrode can be placed at the entrance of the ionization electric field, and the other auxiliary electrode can be placed at the entrance of the ionization electric field.
  • the auxiliary electrode may be a part of the electric field cathode or the electric field anode, that is, the auxiliary electrode may be an extension of the electric field cathode or the electric field anode, and the electric field cathode and the electric field anode have different lengths.
  • the auxiliary electrode may also be a separate electrode, that is, the auxiliary electrode may not be part of the electric field cathode or electric field anode.
  • the voltage of the second electric field is different from the voltage of the first electric field and can be controlled separately according to the working conditions.
  • the auxiliary electrode includes a first electrode and/or a second electrode in the auxiliary electric field unit.
  • the electric field device includes a front electrode between the entrance of the electric field device and the ionizing electric field formed by the electric field anode and the electric field cathode.
  • the gas flows through the front electrode from the entrance of the electric field device, the particles in the gas will be charged.
  • the shape of the front electrode may be a surface, a mesh, a perforated plate, a plate, a needle bar, a ball cage, a box, a tube, a natural material form, or a material processed form.
  • the mesh shape is a shape including any porous structure.
  • the front electrode can be a non-porous structure or a porous structure.
  • the front electrode has a hole structure, one or more through holes are provided on the front electrode.
  • the shape of the through hole may be a polygon, a circle, an oval, a square, a rectangle, a trapezoid, or a rhombus.
  • the outline size of the through hole may be 0.1-3mm, 0.1-0.2mm, 0.2-0.5mm, 0.5-1mm, 1-1.2mm, 1.2-1.5mm, 1.5-2mm, 2-2.5mm , 2.5-2.8mm, or 2.8-3mm.
  • the shape of the front electrode can be one or more of solid, liquid, gas molecular clusters, plasma, conductive mixed state substances, biological substances naturally mixed with conductive substances, or artificial processing of objects to form conductive substances.
  • the front electrode is solid, solid metal, such as 304 steel, or other solid conductors, such as graphite, can be used.
  • the front electrode is a liquid, it may be an ion-containing conductive liquid.
  • the front electrode is perpendicular to the electric field anode. In an embodiment of the present invention, the front electrode is parallel to the electric field anode. In an embodiment of the present invention, the front electrode adopts a metal wire mesh. In an embodiment of the present invention, the voltage between the front electrode and the electric field anode is different from the voltage between the electric field cathode and the electric field anode. In an embodiment of the present invention, the voltage between the front electrode and the electric field anode is less than the initial corona initiation voltage. The initial corona voltage is the minimum voltage between the electric field cathode and the electric field anode. In an embodiment of the present invention, the voltage between the front electrode and the electric field anode may be 0.1-2 kv/mm.
  • the electric field device includes a flow channel, and the front electrode is located in the flow channel.
  • the ratio of the cross-sectional area of the front electrode to the cross-sectional area of the flow channel is 99%-10%, or 90-10%, or 80-20%, or 70-30%, or 60-40% , Or 50%.
  • the cross-sectional area of the front electrode refers to the sum of the area of the solid part of the front electrode along the cross-section.
  • the front electrode has a negative potential.
  • the electric field device provided by the present invention can be applied to the field of gas dust removal technology, such as electrostatic dust removal devices, and can also be used as plasma generators (fluorescent lamps), ozone generators and other devices that require electric field participation.
  • gas dust removal technology such as electrostatic dust removal devices
  • plasma generators fluorescent lamps
  • ozone generators and other devices that require electric field participation.
  • the following takes the electric field device provided by the present invention as an electrostatic precipitator as an example for implementation and description, and the structure of the electrostatic precipitator is the same as the structure of the above electric field device:
  • an electric field device is also used to remove dust and purify the particles contained in the dust-containing gas.
  • the basic principle is to use high-voltage discharge to generate plasma to charge the particles, and then adsorb the charged particles to the dust collecting electrode to achieve electric field dust removal.
  • the existing electrostatic precipitator has problems such as large space occupation, high energy consumption, and low processing efficiency.
  • the electric field device provided by the present invention is small in size and low in energy consumption, and can be applied to the technical field of gas dust removal. Some embodiments can effectively remove particulate matter in the gas.
  • the electric field device may include an electric field cathode and an electric field anode, and an ionizing electric field is formed between the electric field cathode and the electric field anode.
  • an ionizing electric field is formed between the electric field cathode and the electric field anode.
  • the electric field anode may include one or more hollow anode tubes arranged in parallel. When there are multiple hollow anode tubes, all the hollow anode tubes constitute a honeycomb electric field anode.
  • the cross section of the hollow anode tube may be circular or polygonal. If the cross section of the hollow anode tube is circular, a uniform electric field can be formed between the electric field anode and the electric field cathode, and the inner wall of the hollow anode tube is not easy to accumulate dust. If the hollow anode tube has a triangular cross section, 3 dust accumulation surfaces and 3 remote dust holding angles can be formed on the inner wall of the hollow anode tube.
  • the hollow anode tube with this structure has the highest dust holding rate. If the cross section of the hollow anode tube is quadrilateral, 4 dust accumulation surfaces and 4 dust holding angles can be obtained, but the assembly structure is unstable. If the cross section of the hollow anode tube is hexagonal, 6 dust accumulation surfaces and 6 dust retention angles can be formed, and the dust accumulation surface and dust retention rate are balanced. If the cross section of the hollow anode tube is more polygonal, more dust accumulation edges can be obtained, but the dust holding rate is lost.
  • the insulation mechanism is arranged outside the electric field flow channel, that is, outside the electric field flow channel, to prevent or reduce dust in the gas from gathering on the insulation mechanism, causing the insulation mechanism to break down or conduct electricity.
  • the first anode part is located in front of the cathode support plate and the insulating mechanism in the gas flow direction.
  • the first anode part can remove water in the gas and prevent water from entering the insulating mechanism, causing short circuit and ignition of the insulating mechanism. .
  • the first anode part can remove a considerable part of the dust in the gas. When the gas passes through the insulation mechanism, a considerable part of the dust has been eliminated, reducing the possibility of short-circuiting of the insulation mechanism caused by the dust.
  • the insulating mechanism includes insulating ceramic pillars. The design of the first anode part is mainly to protect the insulating ceramic pillars from being polluted by particles in the gas.
  • an anode part can effectively reduce the pollution of the insulating ceramic pillar and increase the use time of the product.
  • the first anode part and the electric field cathode first contact the polluting gas, and the insulating mechanism contacts the gas to achieve the purpose of first removing dust and then passing through the insulating mechanism, reducing pollution to the insulating mechanism and extending
  • the cleaning and maintenance cycle corresponds to the insulating support of the electrode after use.
  • the length of the first anode part is long enough to remove some dust, reduce dust accumulated on the insulation mechanism and the cathode support plate, and reduce electric breakdown caused by the dust.
  • the existing industrial electrostatic dust collection electric field is composed of a dust collecting electrode and a discharge electrode.
  • Each electrode of the electric field is composed of an electrode plate, and the electrodes are arranged in parallel to form the electric field electrodes.
  • the electrodes have the opposite adsorption force to the charged dust. But when the charge is negative, it is adsorbed by the positive electrode, and when the charge is positive, it is adsorbed by the negative plate. But after adsorption, the chargeability is reversed and tends to be the same polarity as the electrode plate, that is, the dust on the positive electrode plate will tend to the negative electrode again, and the dust on the negative electrode plate will tend to the positive electrode. This movement and force are repeated endlessly, forming Electric field coupling consumption.
  • the coupling consumption of the electric field causes the efficiency of electrostatic adsorption of particles with weak adhesion and liquid mist to decline or fail. Therefore, the dust collection efficiency is low and the energy consumption is high.
  • the inventor of the present invention has discovered through research that the disadvantages of poor removal efficiency and high energy consumption of existing electric field devices are caused by electric field coupling.
  • the invention can significantly reduce the size (namely volume) of the electric field dust removal device by reducing the number of electric field couplings.
  • the size of the electric field dust removal device of the present invention is about one-fifth the size of the existing ionization dust removal device.
  • the gas flow rate in the existing electric field dust removal device is set to about 1m/s, and the present invention can still obtain a higher gas flow rate when the gas flow rate is increased to 6m/s. Particle removal rate.
  • the size of the electric field dust removal device can be reduced.
  • the present invention can significantly improve the particle removal efficiency. For example, when the gas flow rate is about 1m/s, the prior art electric field dust removal device can remove about 70% of the particulate matter in the engine exhaust, but the present invention can remove about 99% of the particulate matter, even when the gas flow rate is 6m/s .
  • the dust removal efficiency of the electrostatic dust collection electric field is usually low, and the energy consumption is high.
  • the dust collection electric field in the prior art often chooses multiple stages in series to improve the overall dust collection efficiency. Such a series connection of multiple electric fields will cause the dust collector to occupy a larger space and consume higher energy consumption, and the dust removal efficiency of a single electric field is still substantially low.
  • the electric field device includes an auxiliary electric field that is not parallel to the electric field anode and the electric field cathode.
  • the electric field device further includes an auxiliary electric field, the ionization electric field includes a flow channel, and the auxiliary electric field is not perpendicular to the flow channel.
  • the auxiliary electric field exerts a backward force on the negatively charged oxygen ion flow between the electric field anode and the electric field cathode, so that the negatively charged oxygen ion flow between the electric field anode and the electric field cathode has a backward movement speed.
  • the negatively charged oxygen ions will be combined with the substance to be treated in the process of moving to the anode of the electric field and backward, because the oxygen ions move backwards Speed, when the oxygen ions are combined with the substance to be treated, there will be no strong collision between the two, so as to avoid large energy consumption due to the strong collision, making the oxygen ions easy to combine with the substance to be treated, and
  • the charging efficiency of the substances to be treated in the gas is higher, and more substances to be treated can be collected under the action of the electric field anode, which ensures higher dust removal efficiency of the electric field device provided by the present invention.
  • the dust removal electric field cannot be applied to the exhaust gas with thin oxygen and the low resistance dust that cannot be successfully charged.
  • the oxygen content in the exhaust gas of an oxygen-exhausted car is extremely low, the lowest is only 0.3%, and it can be ionized almost without oxygen, so oxygen ions cannot be produced, electrons cannot be transferred, and dust cannot be charged.
  • water mist and metal dust they are easy to charge and lose electricity. After using oxygen ionization, they will soon fail, and the electric field cannot collect such dust.
  • the electrostatic dust collection electric field in the prior art has a low collection efficiency for dust waiting to be processed.
  • the electric field device includes a front electrode between the entrance of the electric field device and the ionizing electric field formed by the electric field anode and the electric field cathode.
  • the gas flows through the front electrode from the entrance of the electric field device, the particles in the gas will be charged.
  • one or more through holes are provided on the front electrode, and when gas passes through the through holes on the front electrode, the particles in the gas are charged.
  • the gas with particles passes through the through holes on the front electrode, the gas with particles passes through the front electrode, which increases the contact area between the gas with particles and the front electrode and increases the charging efficiency.
  • the through hole on the front electrode in the present invention is any hole that allows substances to flow through the front electrode.
  • the front electrode charges the particles in the gas .
  • the electric field anode exerts an attractive force on the charged particles, causing the charged particles to move toward the electric field anode until the charged particles adhere to the electric field anode.
  • the front electrode introduces electrons into the particles in the gas, and the electrons are transferred between the front electrode and the electric field anode to charge more particles in the gas.
  • the charged particles conduct electrons between the front electrode and the electric field anode and form a current.
  • the front electrode charges the particulate matter in the gas by contacting the particulate matter in the gas. In an embodiment of the present invention, the front electrode transfers electrons to the particulate matter in the gas by contacting the particulate matter in the gas, and charges the particulate matter in the gas.
  • the temperature of the electrostatic field withstand gas is 200°C. If the temperature exceeds 200°C, it will cause electric field breakdown, especially the miniaturized high-efficiency electric field.
  • the electric field withstand temperature of the honeycomb tube bundle with a length of 400 mm and a diameter of 300 mm is 90°C. Below 90°C, the dust collection efficiency of this electric field reaches 99%, but when the temperature rises to 120°C, the electric field will break down and intermittently fail, causing the dust collection efficiency to drop significantly below 50%.
  • the prior art methods to solve the high temperature resistance of the electric field are usually to increase the distance between the electric field anode and the electric field cathode, increase the length of the electric field anode and the electric field cathode, and prevent the electric field from breakdown.
  • the present invention proposes to reduce the length of the electric field anode and the electric field cathode. That is to shorten the length of the electric field anode and the electric field cathode: the length of the electric field anode is 1-9cm, and the length of the electric field cathode is 1-9cm, which solves the problem of high temperature resistance of the electric field generating unit and electric field device.
  • the prior art gives the opposite technical enlightenment.
  • the present invention overcomes technical prejudice (increasing the distance between the electric field anode and the electric field cathode, and increasing the length of the electric field anode and the electric field cathode), and adopts the technical means that people discard due to technical prejudice, thereby solving the technology to be solved by the present invention problem.
  • the present invention proposes to reduce the length of the electric field anode and the electric field cathode, that is, to shorten the length of the electric field anode and the electric field cathode: the length of the electric field anode is 1-9 cm, and the length of the electric field cathode is 1-9 cm. Short, there are few opportunities for active molecules to be connected in series, and no breakdown current can be formed. At the same time, the short-circuit deformation caused by the thermal deformation of the electric field is reduced due to the short, and it is less likely to cause breakdown.
  • the resistance temperature of the electric field device can reach 500°C or even greater than 500°C , And the dust collection efficiency is as high as 50%.
  • the electric field generating unit and the electric field device of the present application have both high temperature tolerance and high dust collection efficiency.
  • the technical effect of the present application produces For those skilled in the art, it is impossible to predict or reason out in advance, and this application has achieved unexpected technical effects.
  • the invention produces unexpected technical effects, on the one hand, it shows that the invention has made significant progress. It also reflects that the technical solution of the invention is not obvious.
  • the corresponding dust collection efficiency when the electric field temperature is 200°C, the corresponding dust collection efficiency is 99.9%; when the electric field temperature is 400°C, the corresponding dust collection efficiency is 90%; when the electric field temperature is 500°C, the corresponding dust collection efficiency is The dust collection efficiency is 50%.
  • FIG. 1 shows a schematic diagram of the structure of the electric field device in this embodiment.
  • the electric field device includes an electric field device inlet 1011, a front electrode 1013, and an insulating mechanism 1015.
  • the electric field device includes an electric field anode 10141 and an electric field cathode 10142 arranged in the electric field anode 10141, and an electric field is formed between the electric field anode 10141 and the electric field cathode 10142.
  • the front electrode 1013 is disposed at the entrance 1011 of the electric field device, and the front electrode 1013 is a conductive mesh plate.
  • the inside of the electric field anode 10141 is composed of a honeycomb-shaped and hollow anode tube bundle group, and the shape of the port of the anode tube bundle is a hexagon.
  • the electric field cathode 10142 includes a plurality of electrode rods, which pierce each anode tube bundle in the anode tube bundle one by one, wherein the shape of the electrode rod is needle-like, polygonal, burr-like, and threaded rod. Shaped or columnar.
  • the ratio of the working area of the electric field anode 10141 to the discharge area of the electric field cathode 10142 is 1680:1, the distance between the electric field anode 10141 and the electric field cathode 10142 is 9.9 mm, the length of the electric field anode 10141 is 60 mm, and the length of the electric field cathode 10142 is 54mm.
  • the outlet end of the electric field cathode 10142 is lower than the outlet end of the electric field anode 10141, and the inlet end of the electric field cathode 10142 is flush with the inlet end of the electric field anode 10141.
  • There is an included angle ⁇ between the exit end of 10141 and the near exit end of the electric field cathode 10142, and ⁇ 90°.
  • the electric field cathode 10142 is mounted on the cathode support plate 10143, and the cathode support plate 10143 and the electric field anode 10141 are connected through an insulating mechanism 1015.
  • the insulation mechanism 1015 is used to achieve insulation between the cathode support plate 10143 and the electric field anode 10141.
  • the electric field anode 10141 includes a first anode portion 101412 and a second anode portion 101411, that is, the first anode portion 101412 is close to the entrance of the electric field device, and the second anode portion 101411 is close to the outlet of the electric field device.
  • the cathode support plate and the insulation mechanism are between the first anode part 101412 and the second anode part 101411, that is, the insulation mechanism 1015 is installed in the middle of the ionization electric field or the middle of the electric field cathode 10142, which can support the electric field cathode 10142 well, and
  • the electric field cathode 10142 is fixed with respect to the electric field anode 10141, and a set distance is maintained between the electric field cathode 10142 and the electric field anode 10141.
  • the insulation mechanism 1015 includes an insulation part and a heat insulation part.
  • the insulating part is made of ceramic material or glass material.
  • the insulating part is an umbrella-shaped string of ceramic columns or glass columns, or a column-shaped string of ceramic columns or glass columns, and the inside and outside of the umbrella or the inside and outside of the column are covered with glaze.
  • the electric field generating unit in this embodiment can be applied to the electric field device of the present invention.
  • FIG. 2 for the schematic diagram of the electric field generating unit of this embodiment.
  • FIG. 3 for the AA view of the electric field generating unit of this embodiment.
  • the length of the electric field generating unit in this embodiment is marked See FIG. 4 for the AA view of the electric field generating unit with angle and angle.
  • FIG. 2 it includes an electric field anode 4051 and an electric field cathode 4052 for generating an electric field.
  • the electric field anode 4051 and the electric field cathode 4052 are respectively electrically connected to two electrodes of a power source.
  • the power source is a DC power source.
  • the anode 4051 and the electric field cathode 4052 are electrically connected to the anode and the cathode of the DC power supply, respectively.
  • the electric field anode 4051 has a positive electric potential
  • the electric field cathode 4052 has a negative electric potential.
  • the DC power supply in this embodiment may specifically be a DC high voltage power supply.
  • a discharge electric field is formed between the electric field anode 4051 and the electric field cathode 4052, and the discharge electric field is an electrostatic field.
  • the electric field anode 4051 has a hollow regular hexagonal tube shape
  • the electric field cathode 4052 has a rod shape
  • the electric field cathode 4052 penetrates the electric field anode 4051.
  • This embodiment also provides a method for reducing electric field coupling, including the steps of selecting the ratio of the working area of the electric field anode 4051 to the discharge area of the electric field cathode 4052 to be 6.67:1, and the distance L3 between the electric field anode 4051 and the electric field cathode 4052 is 9.9mm, the electric field anode 4051 length L1 is 60mm, the electric field cathode 4052 length L2 is 54mm, the electric field anode 4051 includes a fluid channel, the fluid channel includes an inlet end and an outlet end, the electric field cathode 4052 is placed in the fluid channel Wherein, the electric field cathode 4052 extends in the direction of the fluid channel, the inlet end of the electric field anode 4051 is flush with the proximal inlet end of the electric field cathode 4052, and there is an angle between the outlet end of the electric field anode 4051 and the proximal outlet end of the electric field cathode 4052 ⁇ , and
  • the electric field device includes an electric field stage composed of a plurality of the above-mentioned electric field generating units, and there are multiple electric field stages, so as to effectively improve the processing efficiency of the electric field device by using the multiple electric field generating units.
  • each electric field anode has the same polarity
  • each electric field cathode has the same polarity.
  • the electric field stages of the plurality of electric field stages are connected in series, and the series electric field stages are connected by a connecting shell, and the distance between the electric field stages of two adjacent stages is greater than 1.4 times of the pole spacing.
  • FIG. 5 for a schematic diagram of the structure of the electric field device with two electric field levels in this embodiment.
  • the electric field levels are two levels, namely the first electric field 4053 and the second electric field 4054.
  • the first electric field 4053 and the second electric field 4054 The secondary electric field 4054 is connected in series through the connecting housing 4055.
  • This embodiment adopts the existing method for detecting the number of electric field couplings, and the details are as follows:
  • the concentration of the water mist is 200 mg/m 3 , and the wind speed is less than 1.5m/s.
  • the movement from the cathode of the electric field to the anode of the electric field and then to the cathode of the electric field is a reentry, recorded as a coupling, visual observation
  • the number of turns of the water mist is the number of couplings.
  • the electric field device provided in this embodiment can be used to remove particles in the air. Under the action of the electric field anode 4051 and the electric field cathode 4052, this embodiment can collect more particles, realize the number of electric field couplings ⁇ 3, and reduce the electric field The coupling consumption of aerosol, water mist, oil mist and loose and smooth particles in the air saves 30-50% of electric energy in the electric field. In this embodiment, multiple electric field generating units are used to effectively improve the dust removal efficiency of the electric field device.
  • the electric field generating unit in this embodiment can be applied to the electric field device of the present invention. As shown in FIG. 2, it includes an electric field anode 4051 and an electric field cathode 4052 for generating an electric field.
  • the electric field anode 4051 and the electric field cathode 4052 are respectively connected to the two power sources. Each electrode is electrically connected, the power source is a DC power source, and the electric field anode 4051 and the electric field cathode 4052 are electrically connected to the anode and the cathode of the DC power source, respectively.
  • the electric field anode 4051 has a positive electric potential
  • the electric field cathode 4052 has a negative electric potential.
  • the DC power supply in this embodiment may specifically be a DC high-voltage power supply.
  • a discharge electric field is formed between the electric field anode 4051 and the electric field cathode 4052, and the discharge electric field is an electrostatic field.
  • the electric field anode 4051 has a hollow regular hexagonal tube shape
  • the electric field cathode 4052 has a rod shape
  • the electric field cathode 4052 penetrates the electric field anode 4051.
  • This embodiment also provides a method for reducing electric field coupling, including the following steps: selecting the ratio of the working area of the electric field anode 4051 to the discharge area of the electric field cathode 4052 as 1680:1, and the distance between the electric field anode 4051 and the electric field cathode 4052 as 139.9 mm, the electric field anode 4051 has a length of 180 mm, and the electric field cathode 4052 has a length of 180 mm.
  • the electric field anode 4051 includes a fluid channel.
  • the fluid channel includes an inlet end and an outlet end.
  • the electric field cathode 4052 is placed in the fluid channel.
  • the electric field cathode 4052 extends along the direction of the fluid channel.
  • the inlet end of the electric field anode 4051 is flush with the near inlet end of the electric field cathode 4052, and the outlet end of the electric field anode 4051 is flush with the near outlet end of the electric field cathode 4052.
  • the number of times of electric field coupling is ⁇ 3, which can reduce the coupling consumption of the electric field and save the electric field power by 20-40%.
  • the electric field device provided in this embodiment can be used to remove particles in the air. Under the action of the electric field anode 4051 and the electric field cathode 4052, this embodiment can collect more particles, realize the number of electric field couplings ⁇ 3, and reduce the electric field The coupling consumption of aerosol, water mist, oil mist and loose and smooth particles in the air saves 20-40% of the electric energy of the electric field.
  • the electric field generating unit in this embodiment can be applied to the electric field device of the present invention. As shown in FIG. 2, it includes an electric field anode 4051 and an electric field cathode 4052 for generating an electric field.
  • the electric field anode 4051 and the electric field cathode 4052 are respectively connected to the two power sources. Each electrode is electrically connected, the power source is a DC power source, and the electric field anode 4051 and the electric field cathode 4052 are electrically connected to the anode and the cathode of the DC power source, respectively.
  • the electric field anode 4051 has a positive electric potential
  • the electric field cathode 4052 has a negative electric potential.
  • the DC power supply in this embodiment may specifically be a DC high voltage power supply.
  • a discharge electric field is formed between the electric field anode 4051 and the electric field cathode 4052, and the discharge electric field is an electrostatic field.
  • the electric field anode 4051 has a hollow regular hexagonal tube shape
  • the electric field cathode 4052 has a rod shape
  • the electric field cathode 4052 penetrates the electric field anode 4051.
  • This embodiment also provides a method for reducing electric field coupling, including the following steps: selecting the ratio of the working area of the electric field anode 4051 to the discharge area of the electric field cathode 4052 to be 1.667:1, and the distance between the electric field anode 4051 and the electric field cathode 4052 to be 2.4 mm, the electric field anode 4051 has a length of 30 mm, and the electric field cathode 4052 has a length of 30 mm.
  • the electric field anode 4051 includes a fluid channel.
  • the fluid channel includes an inlet end and an outlet end.
  • the electric field cathode 4052 is placed in the fluid channel.
  • the electric field cathode 4052 extends along the direction of the fluid channel.
  • the inlet end of the electric field anode 4051 is flush with the near inlet end of the electric field cathode 4052, and the outlet end of the electric field anode 4051 is flush with the near outlet end of the electric field cathode 4052.
  • the number of times of electric field coupling is ⁇ 3, which can reduce the coupling consumption of the electric field and save the electric energy of the electric field by 10-30%.
  • the electric field device provided in this embodiment can be used to remove particles in the air. Under the action of the electric field anode 4051 and the electric field cathode 4052, this embodiment can collect more particles, realize the number of electric field couplings ⁇ 3, and reduce the electric field The coupling consumption of aerosol, water mist, oil mist, loose and smooth particles in the air saves 10-30% of the electric energy of the electric field.
  • the electric field generating unit in this embodiment can be applied to the electric field device in the electric field dust removal system of the semiconductor manufacturing clean room system of the present invention.
  • it includes an electric field anode 4051 and an electric field cathode 4052 for generating an electric field.
  • the electric field cathode 4051 and the electric field cathode 4052 are respectively electrically connected to two electrodes of a power source.
  • the power source is a DC power source.
  • the electric field anode 4051 and the electric field cathode 4052 are electrically connected to the anode and the cathode of the DC power source, respectively.
  • the electric field anode 4051 has a positive electric potential
  • the electric field cathode 4052 has a negative electric potential.
  • the DC power supply in this embodiment may specifically be a DC high-voltage power supply.
  • a discharge electric field is formed between the electric field anode 4051 and the electric field cathode 4052, and the discharge electric field is an electrostatic field.
  • the electric field anode 4051 in this embodiment is a hollow regular hexagonal tube, the electric field cathode 4052 is rod-shaped, and the electric field cathode 4052 penetrates the electric field anode 4051.
  • the working area of the electric field anode 4051 The ratio of the discharge area to the electric field cathode 4052 is 6.67:1, the distance L3 between the electric field anode 4051 and the electric field cathode 4052 is 9.9 mm, the electric field anode 4051 length L1 is 60 mm, and the electric field cathode 4052 length L2 is 54 mm.
  • the anode 4051 includes a fluid channel, the fluid channel includes an inlet end and an outlet end, the electric field cathode 4052 is placed in the fluid channel, the electric field cathode 4052 extends in the direction of the fluid channel, and the inlet end of the electric field anode 4051 is connected to the electric field.
  • the electric field device includes an electric field stage composed of a plurality of the above-mentioned electric field generating units, and there are multiple electric field stages so as to effectively improve the dust collection efficiency of the electric field device by using a plurality of dust collecting units.
  • each electric field anode has the same polarity
  • each electric field cathode has the same polarity.
  • the electric field stages of the plurality of electric field stages are connected in series, and the series electric field stages are connected by a connecting shell.
  • the distance between the electric field stages of two adjacent stages is greater than 1.4 times of the pole spacing.
  • the electric field has two levels, namely, the first electric field 4053 and the second electric field 4054.
  • the first electric field 4053 and the second electric field 4054 are connected in series through the connecting housing 4055.
  • the electric field device provided in this embodiment can be used to remove particulate matter in the air. Under the action of the electric field anode 4051 and the electric field cathode 4052, more materials to be processed can be collected, ensuring higher dust collection efficiency of the electric field generating unit , The dust collection efficiency of typical particles pm0.23 is above 99.99%.
  • the electric field generating unit in this embodiment can be applied to the electric field device of the present invention. As shown in FIG. 2, it includes an electric field anode 4051 and an electric field cathode 4052 for generating an electric field.
  • the electric field anode 4051 and the electric field cathode 4052 are respectively connected to the two power sources. Each electrode is electrically connected, the power source is a DC power source, and the electric field anode 4051 and the electric field cathode 4052 are electrically connected to the anode and cathode of the DC power source, respectively.
  • the electric field anode 4051 has a positive electric potential
  • the electric field cathode 4052 has a negative electric potential.
  • the DC power supply in this embodiment may specifically be a DC high voltage power supply.
  • a discharge electric field is formed between the electric field anode 4051 and the electric field cathode 4052, and the discharge electric field is an electrostatic field.
  • the electric field anode 4051 has a hollow regular hexagonal tube shape
  • the electric field cathode 4052 has a rod shape
  • the electric field cathode 4052 penetrates the electric field anode 4051.
  • the ratio of the working area of the electric field anode 4051 to the discharge area of the electric field cathode 4052 is 1680: 1.
  • the distance between the electric field anode 4051 and the electric field cathode 4052 is 139.9 mm
  • the electric field anode 4051 has a length of 180 mm
  • the electric field cathode 4052 has a length of 180 mm.
  • the electric field anode 4051 includes a fluid channel, and the fluid channel includes an inlet end and an outlet.
  • the electric field cathode 4052 is placed in the fluid channel, the electric field cathode 4052 extends in the direction of the fluid channel, the inlet end of the electric field anode 4051 is flush with the near inlet end of the electric field cathode 4052, and the outlet end of the electric field anode 4051 It is flush with the near exit end of the electric field cathode 4052.
  • the electric field device includes an electric field stage composed of a plurality of the above-mentioned electric field generating units, and there are multiple electric field stages so as to effectively improve the dust collection efficiency of the electric field device by using the multiple electric field generating units.
  • each electric field anode has the same polarity
  • each electric field cathode has the same polarity.
  • the electric field device provided in this embodiment can be used to remove particulate matter in the air. Under the action of the electric field anode 4051 and the electric field cathode 4052, more materials to be processed can be collected, ensuring higher dust collection efficiency of the electric field generating unit , The dust collection efficiency of typical particles pm0.23 is above 99.99%.
  • the electric field generating unit in this embodiment can be applied to the electric field device of the present invention. As shown in FIG. 2, it includes an electric field anode 4051 and an electric field cathode 4052 for generating an electric field.
  • the electric field anode 4051 and the electric field cathode 4052 are respectively connected to the two power sources. Each electrode is electrically connected, the power source is a DC power source, and the electric field anode 4051 and the electric field cathode 4052 are electrically connected to the anode and cathode of the DC power source, respectively.
  • the electric field anode 4051 has a positive electric potential
  • the electric field cathode 4052 has a negative electric potential.
  • the DC power supply in this embodiment may specifically be a DC high-voltage power supply.
  • a discharge electric field is formed between the electric field anode 4051 and the electric field cathode 4052, and the discharge electric field is an electrostatic field.
  • the electric field anode 4051 is in the shape of a hollow regular hexagon
  • the electric field cathode 4052 is in the shape of a rod
  • the electric field cathode 4052 is inserted in the electric field anode 4051.
  • the ratio of the working area of the electric field anode 4051 to the discharge area of the electric field cathode 4052 is 1.667: 1.
  • the distance between the electric field anode 4051 and the electric field cathode 4052 is 2.4 mm.
  • the electric field anode 4051 has a length of 30 mm and the electric field cathode 4052 has a length of 30 mm.
  • the electric field anode 4051 includes a fluid channel.
  • the fluid channel includes an inlet end and an outlet end.
  • the electric field cathode 4052 is placed in the fluid channel.
  • the cathode 4052 extends in the direction of the fluid channel, the inlet end of the electric field anode 4051 is flush with the proximal inlet end of the electric field cathode 4052, and the outlet end of the electric field anode 4051 is flush with the proximal outlet end of the electric field cathode 4052.
  • the electric field anode 4051 and the electric field cathode 4052 constitute an electric field generating unit, and there are multiple electric field generating units to effectively improve the dust collection efficiency of the electric field device by using multiple electric field generating units.
  • the electric field device provided in this embodiment can be used to remove particulate matter in the air. Under the action of the electric field anode 4051 and the electric field cathode 4052, more materials to be processed can be collected, ensuring higher dust collection efficiency of the electric field generating unit , The dust collection efficiency of typical particles pm0.23 is above 99.99%.
  • the electric field generating unit in this embodiment can be applied to the electric field device of the present invention. As shown in FIG. 2, it includes an electric field anode 4051 and an electric field cathode 4052 for generating an electric field.
  • the electric field anode 4051 and the electric field cathode 4052 are respectively connected to the two power sources. Each electrode is electrically connected, the power source is a DC power source, and the electric field anode 4051 and the electric field cathode 4052 are electrically connected to the anode and cathode of the DC power source, respectively.
  • the electric field anode 4051 has a positive electric potential
  • the electric field cathode 4052 has a negative electric potential.
  • the DC power supply in this embodiment may specifically be a DC high voltage power supply.
  • a discharge electric field is formed between the electric field anode 4051 and the electric field cathode 4052, and the discharge electric field is an electrostatic field.
  • the electric field anode 4051 has a hollow regular hexagonal tube shape
  • the electric field cathode 4052 has a rod shape
  • the electric field cathode 4052 penetrates the electric field anode 4051.
  • the method of reducing electric field coupling includes the following steps: selecting the ratio of the working area of the electric field anode 4051 to the discharge area of the electric field cathode 4052 to be 27.566:1, the distance between the electric field anode 4051 and the electric field cathode 4052 is 2.3 mm, and the length of the electric field anode 4051 is
  • the electric field cathode 4052 has a length of 4 mm, the electric field anode 4051 includes a fluid channel, the fluid channel includes an inlet end and an outlet end, the electric field cathode 4052 is placed in the fluid channel, and the electric field cathode 4052 runs along the fluid channel.
  • the inlet end of the electric field anode 4051 is flush with the near inlet end of the electric field cathode 4052, the outlet end of the electric field anode 4051 is flush with the near outlet end of the electric field cathode 4052, and then under the action of the electric field anode 4051 and the electric field cathode 4052 , Realizing the number of electric field coupling ⁇ 3, which can reduce the coupling consumption of the electric field.
  • the electric field device provided in this embodiment can be used to remove particulate matter in the air. Under the action of the electric field anode 4051 and the electric field cathode 4052, more materials to be processed can be collected, ensuring higher dust collection efficiency of the electric field generating unit .
  • the electric field generating unit in this embodiment can be applied to the electric field device of the present invention. As shown in FIG. 2, it includes an electric field anode 4051 and an electric field cathode 4052 for generating an electric field.
  • the electric field anode 4051 and the electric field cathode 4052 are respectively connected to the two power sources. Each electrode is electrically connected, the power source is a DC power source, and the electric field anode 4051 and the electric field cathode 4052 are electrically connected to the anode and cathode of the DC power source, respectively.
  • the electric field anode 4051 has a positive electric potential
  • the electric field cathode 4052 has a negative electric potential.
  • the DC power supply in this embodiment may specifically be a DC high voltage power supply.
  • a discharge electric field is formed between the electric field anode 4051 and the electric field cathode 4052, and the discharge electric field is an electrostatic field.
  • the electric field anode 4051 has a hollow regular hexagonal tube shape
  • the electric field cathode 4052 has a rod shape
  • the electric field cathode 4052 penetrates the electric field anode 4051.
  • the method of reducing electric field coupling includes the following steps: selecting the ratio of the working area of the electric field anode 4051 to the discharge area of the electric field cathode 4052 to be 1.108:1, the distance between the electric field anode 4051 and the electric field cathode 4052 is 2.3 mm, and the electric field anode 051 length is 60mm, the electric field cathode 4052 has a length of 200mm, the electric field anode 4051 includes a fluid channel, the fluid channel includes an inlet end and an outlet end, the electric field cathode 4052 is placed in the fluid channel, and the electric field cathode 4052 runs along the fluid channel.
  • the inlet end of the electric field anode 4051 is flush with the near inlet end of the electric field cathode 4052, the outlet end of the electric field anode 4051 is flush with the near outlet end of the electric field cathode 4052, and then under the action of the electric field anode 4051 and the electric field cathode 4052 , Realizing the number of electric field coupling ⁇ 3, which can reduce the coupling consumption of the electric field.
  • the electric field device provided in this embodiment can be used to remove particulate matter in the air. Under the action of the electric field anode 4051 and the electric field cathode 4052, more materials to be processed can be collected, ensuring higher dust collection efficiency of the electric field generating unit .
  • the electric field generating unit in this embodiment can be applied to the electric field device of the present invention. As shown in FIG. 2, it includes an electric field anode 4051 and an electric field cathode 4052 for generating an electric field.
  • the electric field anode 4051 and the electric field cathode 4052 are respectively connected to the two power sources. Each electrode is electrically connected, the power source is a DC power source, and the electric field anode 4051 and the electric field cathode 4052 are electrically connected to the anode and cathode of the DC power source, respectively.
  • the electric field anode 4051 has a positive electric potential
  • the electric field cathode 4052 has a negative electric potential.
  • the DC power supply in this embodiment may specifically be a DC high voltage power supply.
  • a discharge electric field is formed between the electric field anode 4051 and the electric field cathode 4052, and the discharge electric field is an electrostatic field.
  • the electric field anode 4051 has a hollow regular hexagonal tube shape
  • the electric field cathode 4052 has a rod shape
  • the electric field cathode 4052 penetrates the electric field anode 4051.
  • the method of reducing electric field coupling includes the following steps: selecting the ratio of the working area of the electric field anode 4051 to the discharge area of the electric field cathode 4052 to be 3065:1, the distance between the electric field anode 4051 and the electric field cathode 4052 is 249mm, and the electric field anode 4051 length is 2000mm
  • the electric field cathode 4052 has a length of 180 mm, the electric field anode 4051 includes a fluid channel, the fluid channel includes an inlet end and an outlet end, the electric field cathode 4052 is placed in the fluid channel, and the electric field cathode 4052 runs along the fluid channel.
  • the inlet end of the electric field anode 4051 is flush with the near inlet end of the electric field cathode 4052, the outlet end of the electric field anode 4051 is flush with the near outlet end of the electric field cathode 4052, and then under the action of the electric field anode 4051 and the electric field cathode 4052, Achieve electric field coupling times ⁇ 3.
  • the electric field device provided in this embodiment can be used to remove particulate matter in the air. Under the action of the electric field anode 4051 and the electric field cathode 4052, more materials to be processed can be collected, ensuring higher dust collection efficiency of the electric field generating unit .
  • the electric field generating unit in this embodiment can be applied to the electric field device of the present invention. As shown in FIG. 2, it includes an electric field anode 4051 and an electric field cathode 4052 for generating an electric field.
  • the electric field anode 4051 and the electric field cathode 4052 are respectively connected to the two power sources. Each electrode is electrically connected, the power source is a DC power source, and the electric field anode 4051 and the electric field cathode 4052 are electrically connected to the anode and cathode of the DC power source, respectively.
  • the electric field anode 4051 has a positive electric potential
  • the electric field cathode 4052 has a negative electric potential.
  • the DC power supply in this embodiment may specifically be a DC high-voltage power supply.
  • a discharge electric field is formed between the electric field anode 4051 and the electric field cathode 4052, and the discharge electric field is an electrostatic field.
  • the electric field anode 4051 has a hollow regular hexagonal tube shape
  • the electric field cathode 4052 has a rod shape
  • the electric field cathode 4052 penetrates the electric field anode 4051.
  • the method of reducing electric field coupling includes the following steps: selecting the ratio of the working area of the electric field anode 4051 to the discharge area of the electric field cathode 4052 to be 1.338:1, the distance between the electric field anode 4051 and the electric field cathode 4052 is 5 mm, and the electric field anode 4051 length is 2 mm
  • the electric field cathode 4052 has a length of 10 mm.
  • the electric field anode 4051 includes a fluid channel.
  • the fluid channel includes an inlet end and an outlet end.
  • the electric field cathode 4052 is placed in the fluid channel.
  • the inlet end of the electric field anode 4051 is flush with the near inlet end of the electric field cathode 4052, the outlet end of the electric field anode 4051 is flush with the near outlet end of the electric field cathode 4052, and then under the action of the electric field anode 4051 and the electric field cathode 4052, Achieve electric field coupling times ⁇ 3.
  • the electric field device provided in this embodiment can be used to remove particulate matter in the air. Under the action of the electric field anode 4051 and the electric field cathode 4052, more materials to be processed can be collected, ensuring higher dust collection efficiency of the electric field generating unit .
  • the electric field device includes an electric field cathode 5081 and an electric field anode 5082 which are electrically connected to the cathode and anode of the DC power supply, respectively, and the auxiliary electrode 5083 is electrically connected to the anode of the DC power supply.
  • the electric field cathode 5081 has a negative potential
  • the electric field anode 5082 and the auxiliary electrode 5083 both have a positive potential.
  • the auxiliary electrode 5083 and the electric field anode 5082 are fixedly connected in this embodiment. After the electric field anode 5082 is electrically connected to the anode of the DC power supply, the auxiliary electrode 5083 is also electrically connected to the anode of the DC power supply, and the auxiliary electrode 5083 and the electric field anode 5082 have the same positive potential.
  • the auxiliary electrode 5083 in this embodiment can extend in the front-to-back direction, that is, the length direction of the auxiliary electrode 5083 can be the same as the length direction of the electric field anode 5082.
  • the electric field anode 5082 is tubular, the electric field cathode 5081 is rod-shaped, and the electric field cathode 5081 penetrates the electric field anode 5082.
  • the auxiliary electrode 5083 in this embodiment is also tubular, and the auxiliary electrode 5083 and the electric field anode 5082 constitute the anode tube 5084.
  • the front end of the anode tube 5084 is flush with the electric field cathode 5081, and the rear end of the anode tube 5084 extends backward beyond the rear end of the electric field cathode 5081.
  • the part of the anode tube 5084 that extends backward is the auxiliary electrode 5083.
  • the electric field anode 5082 and the electric field cathode 5081 have the same length, and the electric field anode 5082 and the electric field cathode 5081 are opposite in the front and rear direction; the auxiliary electrode 5083 is located behind the electric field anode 5082 and the electric field cathode 5081. In this way, an auxiliary electric field is formed between the auxiliary electrode 5083 and the electric field cathode 5081.
  • the electric field device provided in this embodiment can be used to remove particulate matter in the air.
  • the auxiliary electric field described above exerts a backward force on the negatively charged oxygen ion flow between the electric field anode 5082 and the electric field cathode 5081.
  • the negatively charged oxygen ions will combine with the substance to be treated in the process of moving to the electric field anode 5082 and backward, because the oxygen ions have a backward moving speed
  • the oxygen ions are combined with the substance to be treated, there will be no strong collision between the two, thereby avoiding large energy consumption due to the strong collision, making the oxygen ions easy to combine with the substance to be treated, and making
  • the charging efficiency of the substances to be treated in the gas is higher, and furthermore, under the action of the electric field anode 5082 and the anode tube 5084, more substances to be treated can be collected, ensuring higher dust removal efficiency of the electric field device.
  • the electric field anode 5082, the auxiliary electrode 5083, and the electric field cathode 5081 constitute a dust removal unit, and there are multiple dust removal units to effectively improve the dust removal efficiency of the electric field device by using multiple dust removal units.
  • the DC power supply in this embodiment may specifically be a DC high-voltage power supply.
  • a discharge electric field is formed between the electric field cathode 5081 and the electric field anode 5082, and the discharge electric field is an electrostatic field.
  • the auxiliary electrode 5083 Without the auxiliary electrode 5083, the ions flow in the electric field between the electric field cathode 5081 and the electric field anode 5082 along the direction perpendicular to the electrodes, and flow back and forth between the two electrodes, causing ions to be folded back and forth between the electrodes for consumption.
  • the auxiliary electrode 5083 is used to stagger the relative positions of the electrodes to form a relative imbalance between the electric field anode 5082 and the electric field cathode 5081.
  • an auxiliary electrode 5083 is used to form an electric field capable of directing ion flow.
  • the collection rate of the electric field device for particles entering the electric field in the direction of ion flow is nearly doubled than that of particles entering the electric field in the direction of counter ion flow, thereby improving the efficiency of electric field dust accumulation and reducing electric field power consumption.
  • the main reason for the low dust removal efficiency of the dust-collecting electric field in the prior art is that the direction of the dust entering the electric field is opposite or perpendicular to the direction of the ion flow in the electric field, which causes the dust and the ion flow to collide violently and produce large energy consumption. It also affects the charging efficiency, thereby reducing the electric field dust collection efficiency in the prior art and increasing the energy consumption.
  • the electric field device in this embodiment When the electric field device in this embodiment is used to collect dust in the gas, the gas and dust enter the electric field along the ion flow direction, the dust is fully charged, and the electric field consumption is small; the dust collection efficiency of the unipolar electric field can reach more than 99.99%. When gas and dust enter the electric field against the direction of ion flow, the dust is not fully charged, and the electric power consumption of the electric field will increase, and the dust collection efficiency will be 40%-75%.
  • the ion flow formed by the electric field device in this embodiment is beneficial to the unpowered fan fluid transportation, oxygenation, heat exchange, and the like.
  • the electric field device provided in this embodiment includes an electric field cathode and an electric field anode respectively electrically connected to the cathode and anode of the DC power supply, and the auxiliary electrode is electrically connected to the cathode of the DC power supply.
  • the auxiliary electrode and the electric field cathode both have a negative electric potential, and the electric field anode has a positive electric potential.
  • the auxiliary electrode can be fixedly connected to the electric field cathode. In this way, after the electric field cathode is electrically connected to the cathode of the DC power supply, the auxiliary electrode is also electrically connected to the cathode of the DC power supply. At the same time, the auxiliary electrode in this embodiment extends in the front-rear direction.
  • the electric field anode is tubular, the electric field cathode is rod-shaped, and the electric field cathode penetrates the electric field anode.
  • the above-mentioned auxiliary electrode in this embodiment is also rod-shaped, and the auxiliary electrode and the electric field cathode constitute a cathode rod. The front end of the cathode rod forwards beyond the front end of the electric field anode, and the part of the cathode rod that exceeds the electric field anode forward is the auxiliary electrode.
  • the length of the electric field anode and the electric field cathode are the same, and the electric field anode and the electric field cathode are opposite in the front and rear direction; the auxiliary electrode is located in front of the electric field anode and the electric field cathode.
  • an auxiliary electric field is formed between the auxiliary electrode and the electric field anode, and the auxiliary electric field applies a backward force to the negatively charged oxygen ion flow between the electric field anode and the electric field cathode, so that the negatively charged oxygen ions between the electric field anode and the electric field cathode
  • the flow has a backward movement speed.
  • the electric field device provided in this embodiment can be used to remove particulate matter in the air.
  • the gas containing the substance to be treated flows from front to back into the tubular electric field anode, the negatively charged oxygen ions will move towards the electric field anode and back.
  • oxygen ions have a backward moving speed
  • when the oxygen ions are combined with the substance to be treated there will be no strong collision between the two, thus avoiding the larger collision caused by the stronger collision.
  • Energy consumption makes it easier for oxygen ions to combine with the substance to be treated, and makes the charging efficiency of the substance to be treated in the gas higher.
  • more substances to be treated can be collected to ensure the electric field device The dust removal efficiency is higher.
  • the electric field anode, the auxiliary electrode, and the electric field cathode constitute a dust removal unit, and there are multiple dust removal units to effectively improve the dust removal efficiency of the electric field device by using multiple dust removal units.
  • FIG. 7 for a schematic diagram of the structure of the electric field device in this embodiment.
  • the auxiliary electrode 5083 extends in the left-right direction.
  • the length direction of the auxiliary electrode 5083 in this embodiment is different from the length direction of the electric field anode 5082 and the electric field cathode 5081.
  • the auxiliary electrode 5083 may be perpendicular to the electric field anode 5082.
  • the electric field cathode 5081 and the electric field anode 5082 are electrically connected to the cathode and anode of the DC power supply, respectively, and the auxiliary electrode 5083 is electrically connected to the anode of the DC power supply.
  • the electric field cathode 5081 has a negative potential
  • the electric field anode 5082 and the auxiliary electrode 5083 both have a positive potential.
  • the electric field cathode 5081 and the electric field anode 5082 are opposed to each other in the front and rear direction, and the auxiliary electrode 5083 is located behind the electric field anode 5082 and the electric field cathode 5081.
  • an auxiliary electric field is formed between the auxiliary electrode 5083 and the electric field cathode 5081, and the auxiliary electric field applies a backward force to the negatively charged oxygen ion flow between the electric field anode 5082 and the electric field cathode 5081.
  • the electric field device provided in this embodiment can be used to remove particulate matter in the air.
  • the gas containing the substance to be treated flows from front to back into the electric field between the electric field anode 5082 and the electric field cathode 5081, the negatively charged oxygen ions are moving towards The electric field anode 5082 will be combined with the material to be processed during the backward movement.
  • oxygen ions have a backward moving speed, when the oxygen ions are combined with the material to be processed, there will be no strong collision between the two, thus Avoid large energy consumption due to strong collisions, make oxygen ions easy to combine with the substance to be treated, and make the charging efficiency of the substance to be treated in the gas higher, and then under the action of the electric field anode 5082, it can be more More materials to be processed are collected to ensure higher dust removal efficiency of the electric field device.
  • the auxiliary electrode 5083 extends in the left-right direction.
  • the length direction of the auxiliary electrode 5083 in this embodiment is different from the length direction of the electric field anode 5082 and the electric field cathode 5081.
  • the auxiliary electrode 5083 may be perpendicular to the electric field cathode 5081.
  • the electric field cathode 5081 and the electric field anode 5082 are electrically connected to the cathode and anode of the DC power supply, respectively, and the auxiliary electrode 5083 is electrically connected to the cathode of the DC power supply.
  • the electric field cathode 5081 and the auxiliary electrode 5083 both have a negative electric potential, and the electric field anode 5082 has a positive electric potential.
  • the electric field cathode 5081 and the electric field anode 5082 are opposite to each other in the front and rear direction, and the auxiliary electrode 5083 is located in front of the electric field anode 5082 and the electric field cathode 5081.
  • an auxiliary electric field is formed between the auxiliary electrode 5083 and the electric field anode 5082.
  • the auxiliary electric field applies a backward force to the negatively charged oxygen ion flow between the electric field anode 5082 and the electric field cathode 5081, so that the electric field anode 5082 and the electric field cathode 5081 are
  • the stream of negatively charged oxygen ions has a backward moving speed.
  • the negatively charged oxygen ions will be combined with the substance to be treated in the process of moving to the electric field anode 5082 and backward.
  • Oxygen ions have a backward moving speed.
  • the oxygen ions are combined with the material to be treated, there will be no strong collision between the two, thus avoiding the large energy consumption caused by the strong collision, making the oxygen ions easy to interact with
  • the combination of the substances to be treated makes the charging efficiency of the substances to be treated in the gas higher. Then, under the action of the electric field anode 5082, more substances to be treated can be collected, ensuring higher dust removal efficiency of the electric field device.
  • the electric field device includes an electric field device inlet 3085, a flow channel 3086, an electric field flow channel 3087, and an electric field device outlet 3088 that are connected in sequence.
  • a front electrode 3083 is installed in the flow channel 3086.
  • the ratio of the area to the cross-sectional area of the flow channel 3086 is 99%-10%.
  • the electric field device also includes an electric field cathode 3081 and an electric field anode 3082.
  • the electric field flow channel 3087 is located between the electric field cathode 3081 and the electric field anode 3082.
  • the electric field device provided in this embodiment can be used to remove particulate matter in the air.
  • the gas containing particulate matter enters the flow channel 3086 through the electric field device inlet 3085, and the front electrode 3083 installed in the flow channel 3086 conducts electrons to part of the particulate matter.
  • the electric field anode 3082 exerts an attractive force on the charged particles, and the charged particles move to the electric field anode 3082 until the part of the charged particles attach to the electric field anode 3082.
  • An ionizing electric field is formed between the electric field cathode 3081 and the electric field anode 3082 in the electric field channel 3087.
  • the ionizing electric field will charge another part of the uncharged particles so that the other part of the particles will also be attracted by the electric field anode 3082 after being charged. It is finally attached to the electric field anode 3082, so that the above-mentioned electric field device is used to make the particles more efficient and fully charged, thereby ensuring that the electric field anode 3082 can collect more particles, and ensuring that the electric field device of the present invention has a higher collection efficiency for particles in the gas .
  • the cross-sectional area of the front electrode 3083 refers to the sum of the area of the front electrode 3083 along the solid part of the cross-section.
  • the ratio of the cross-sectional area of the front electrode 3083 to the cross-sectional area of the flow channel 3086 may be 99%-10%, or 90-10%, or 80-20%, or 70-30%, or 60-40%, or 50%.
  • the front electrode 3083 and the electric field cathode 3081 are electrically connected to the cathode of the DC power supply, and the electric field anode 3082 is electrically connected to the anode of the DC power supply.
  • the front electrode 3083 and the electric field cathode 3081 both have a negative electric potential, and the electric field anode 3082 has a positive electric potential.
  • the front electrode 3083 in this embodiment may have a mesh shape, that is, a plurality of through holes are provided.
  • the structural feature of the front electrode 3083 with through holes is used to facilitate the flow of gas and particles through the front electrode 3083, and make the particles in the gas contact the front electrode 3083 more fully.
  • the front electrode 3083 can conduct electrons to more particles, and the charging efficiency of the particles is higher.
  • the electric field anode 3082 is tubular, the electric field cathode 3081 is rod-shaped, and the electric field cathode 3081 penetrates the electric field anode 3082.
  • the electric field anode 3082 and the electric field cathode 3081 have an asymmetric structure.
  • the ionizing electric field formed between the electric field cathode 3081 and the electric field anode 3082 will charge the particles when the gas flows into the electric field anode 3082 and collect the charged particles on the inner wall of the electric field anode 3082 under the attractive force exerted by the electric field anode 3082.
  • both the electric field anode 3082 and the electric field cathode 3081 extend in the front-rear direction, and the front end of the electric field anode 3082 is located in front of the front end of the electric field cathode 3081 in the front-rear direction. And as shown in FIG. 9, the rear end of the electric field anode 3082 is located behind the rear end of the electric field cathode 3081 in the front-rear direction.
  • the length of the electric field anode 3082 in the forward and backward directions is longer, so that the adsorption surface area on the inner wall of the electric field anode 3082 is larger, so that the attraction force to the particles with negative potential is greater, and more can be collected. particulates.
  • the electric field cathode 3081 and the electric field anode 3082 constitute an ionization unit.
  • the above-mentioned pollutants include ordinary dust with relatively weak conductivity, and metal dust, mist droplets, aerosols, etc. with relatively strong conductivity.
  • the electric field device in the gas collects ordinary dust with weaker conductivity and pollutants with stronger conductivity: when the gas flows into the flow channel 3086 through the inlet 3085 of the electric field device, the gas has stronger conductivity When the metal dust, droplets, or aerosols are in contact with the front electrode 3083, or when the distance from the front electrode 3083 reaches a certain range, they will be directly negatively charged. Then, all the pollutants will enter the electric field with the air flow.
  • the dust removal electric field anode 3082 exerts attractive force on the negatively charged metal dust, droplets, or aerosols, and collects this part of the pollutants.
  • the dust removal electric field anode 3082 and the dust removal electric field cathode 3081 form an ionization electric field.
  • the ionization electric field obtains oxygen ions by ionizing the oxygen in the gas, and the negatively charged oxygen ions combine with ordinary dust to make the ordinary dust negatively charged.
  • the dust removal electric field anode 3082 exerts an attraction force on this part of the negatively charged dust. This part of the pollutants is collected, so that the pollutants with strong conductivity and weak conductivity in the gas are collected, and the types of substances that can be collected by the electric field device are wider and the collection capacity is stronger.
  • the electric field cathode 3081 is also called a corona charged electrode.
  • the aforementioned DC power supply is specifically a DC high-voltage power supply.
  • a DC high voltage is connected between the front electrode 3083 and the electric field anode 3082 to form a conductive loop; a DC high voltage is connected between the electric field cathode 3081 and the electric field anode 3082 to form an ionization discharge corona electric field.
  • the front electrode 3083 is a densely distributed conductor.
  • the front electrode 3083 When the easily charged dust and other particles pass through the front electrode 3083, the front electrode 3083 directly charges the particles with electrons, and the particles are then adsorbed by the electric field anode 3082 of the opposite electrode; at the same time, the uncharged particles pass the electric field cathode 3081 and the electric field anode 3082.
  • the formed ionization zone, the ionized oxygen formed in the ionization zone will charge the electrons to the particles, so that the particles continue to be charged and absorbed by the electric field anode 3082 of the opposite electrode.
  • the electric field device can form two or more power-on modes.
  • the ionization discharge corona electric field formed between the electric field cathode 3081 and the electric field anode 3082 can be used to charge the particles in the gas, and the electric field anode 3082 can be used to collect the particles; and
  • the front electrode 3083 is used to directly electrify the particles in the gas, so that the particles in the gas are fully charged and then adsorbed by the electric field anode 3082.
  • the electric field device allows the electric field to collect all kinds of dust, and can also be used in various environments with low oxygen content, expands the application range of dust collection electric field to control dust, and improves dust collection efficiency.
  • This embodiment adopts the electric fields of the above-mentioned two charging modes, and can simultaneously collect high-resistance dust that is easy to charge and low-resistance metal dust, aerosol, liquid mist, etc. that are easy to charge.
  • the two power-on methods are used at the same time, and the application range of the electric field is expanded.
  • the electric field generating unit in this embodiment has a structure diagram as shown in FIG. 2 and includes a dust-removing electric field anode 4051 and a dust-removing electric field cathode 4052 for generating an electric field.
  • the dust-removing electric field anode 4051 and the dust-removing electric field cathode 4052 are respectively connected to the two electrodes of the power supply. Electrically connected, the power source is a DC power source, and the dust removal electric field anode 4051 and the dust removal electric field cathode 4052 are electrically connected to the anode and the cathode of the DC power source, respectively.
  • the dedusting electric field anode 4051 has a positive electric potential
  • the dedusting electric field cathode 4052 has a negative electric potential.
  • the DC power supply in this embodiment may specifically be a DC high voltage power supply.
  • a discharge electric field is formed between the anode 4051 of the dust removal electric field and the cathode 4052 of the dust removal electric field, and the discharge electric field is an electrostatic field.
  • the dust removal electric field anode 4051 is a hollow regular hexagonal tube
  • the dust removal electric field cathode 4052 is a rod shape
  • the dust removal electric field cathode 4052 is inserted in the dust removal electric field anode 4051
  • the length of the dust removal electric field anode 4051 is 5 cm
  • the length of the dust removal electric field cathode 4052 is 5 cm
  • the dust removal electric field anode 4051 includes a fluid channel
  • the fluid channel includes an inlet end and an outlet end
  • the dust removal electric field cathode 4052 is placed in the fluid channel
  • the dust removal electric field cathode 4052 extends along the direction of the fluid channel.
  • the inlet end of the dedusting electric field anode 4051 is flush with the near inlet end of the dedusting electric field cathode 4052, and the outlet end of the dedusting electric field anode 4051 is flush with the near outlet end of the dedusting electric field cathode 4052.
  • the distance between the electrodes is 9.9 mm, and under the action of the anode 4051 of the dust removal electric field and the cathode 4052 of the dust removal electric field, it can withstand high temperature impact.
  • the electric field device provided in this embodiment can be used to remove particles in the air, is resistant to high temperature impact, and can collect more granular dust, ensuring higher dust collection efficiency of the electric field generating unit.
  • An electric field temperature of 200°C corresponds to a dust collection efficiency of 99.9%; an electric field temperature of 400°C corresponds to a dust collection efficiency of 90%; an electric field temperature of 500°C corresponds to a dust collection efficiency of 50%.
  • the electric field device includes an electric field stage composed of a plurality of the above-mentioned electric field generating units, and there are multiple electric field stages to effectively improve the dust collection efficiency of the electric field device by using a plurality of dust collecting units.
  • each dedusting electric field anode has the same polarity
  • each dedusting electric field cathode has the same polarity.
  • the electric field generating unit in this embodiment can be applied to an electric field device. As shown in FIG. 2, it includes a dust removal electric field anode 4051 and a dust removal electric field cathode 4052 for generating an electric field.
  • the dust removal electric field anode 4051 and the dust removal electric field cathode 4052 are respectively connected to the power supply.
  • the two electrodes are electrically connected, the power source is a DC power source, and the dust removal electric field anode 4051 and the dust removal electric field cathode 4052 are electrically connected to the anode and the cathode of the DC power source, respectively.
  • the dedusting electric field anode 4051 has a positive electric potential
  • the dedusting electric field cathode 4052 has a negative electric potential.
  • the DC power supply in this embodiment may specifically be a DC high voltage power supply.
  • a discharge electric field is formed between the anode 4051 of the dust removal electric field and the cathode 4052 of the dust removal electric field, and the discharge electric field is an electrostatic field.
  • the dust removal electric field anode 4051 is a hollow regular hexagonal tube
  • the dust removal electric field cathode 4052 is a rod shape
  • the dust removal electric field cathode 4052 is inserted in the dust removal electric field anode 4051
  • the length of the dust removal electric field anode 4051 is 9 cm
  • the length of the dust removal electric field cathode 4052 is 9cm
  • the dust removal electric field anode 4051 includes a fluid channel
  • the fluid channel includes an inlet end and an outlet end
  • the dust removal electric field cathode 4052 is placed in the fluid channel
  • the dust removal electric field cathode 4052 extends along the direction of the fluid channel
  • the inlet end of the dedusting electric field anode 4051 is flush with the near inlet end of the dedusting electric field cathode 4052
  • the outlet end of the dedusting electric field anode 4051 is flush with the near outlet end of the dedusting electric field cathode 4052.
  • the electric field device provided in this embodiment can be used to remove particles in the air, is resistant to high temperature impact, and can collect more granular dust, ensuring that the dust collection efficiency of the electric field generating unit is higher.
  • An electric field temperature of 200°C corresponds to a dust collection efficiency of 99.9%; an electric field temperature of 400°C corresponds to a dust collection efficiency of 90%; an electric field temperature of 500°C corresponds to a dust collection efficiency of 50%.
  • the electric field device includes an electric field stage composed of a plurality of the above-mentioned electric field generating units, and there are multiple electric field stages so as to effectively improve the dust collection efficiency of the electric field device by using a plurality of dust collecting units.
  • each storage electric field anode has the same polarity
  • each dust removal electric field cathode has the same polarity.
  • the electric field generating unit in this embodiment can be applied to an electric field device. As shown in FIG. 2, it includes a dust removal electric field anode 4051 and a dust removal electric field cathode 4052 for generating an electric field.
  • the dust removal electric field anode 4051 and the dust removal electric field cathode 4052 are respectively connected to the power supply.
  • the two electrodes are electrically connected, the power source is a DC power source, and the dust removal electric field anode 4051 and the dust removal electric field cathode 4052 are electrically connected to the anode and the cathode of the DC power source, respectively.
  • the dedusting electric field anode 4051 has a positive electric potential
  • the dedusting electric field cathode 4052 has a negative electric potential.
  • the DC power supply in this embodiment may specifically be a DC high-voltage power supply.
  • a discharge electric field is formed between the dust removal electric field anode 4051 and the dust removal electric field cathode 4052, and the discharge electric field is an electrostatic field.
  • the dust removal electric field anode 4051 is a hollow regular hexagonal tube
  • the dust removal electric field cathode 4052 is a rod shape
  • the dust removal electric field cathode 4052 is inserted in the dust removal electric field anode 4051
  • the length of the dust removal electric field anode 4051 is 1 cm
  • the length of the dust removal electric field cathode 4052 is 1 cm
  • the dust removal electric field anode 4051 includes a fluid channel
  • the fluid channel includes an inlet end and an outlet end
  • the dust removal electric field cathode 4052 is placed in the fluid channel
  • the dust removal electric field cathode 4052 extends along the direction of the fluid channel
  • the inlet end of the dedusting electric field anode 4051 is flush with the near inlet end of the dedusting electric field cathode 4052
  • the outlet end of the dedusting electric field anode 4051 is flush with the near outlet end of the dedusting electric field cathode 4052.
  • the electric field device provided in this embodiment can be used to remove particles in the air, is resistant to high temperature impact, and can collect more granular dust, ensuring higher dust collection efficiency of the electric field generating unit.
  • An electric field temperature of 200°C corresponds to a dust collection efficiency of 99.9%; an electric field temperature of 400°C corresponds to a dust collection efficiency of 90%; an electric field temperature of 500°C corresponds to a dust collection efficiency of 50%.
  • the electric field device includes an electric field stage composed of a plurality of the above-mentioned electric field generating units, and there are multiple electric field stages to effectively improve the dust collection efficiency of the electric field device by using a plurality of dust collecting units.
  • each dedusting electric field anode has the same polarity
  • each dedusting electric field cathode has the same polarity.
  • the electric field stages of the plurality of electric field stages are connected in series, and the series electric field stages are connected by a connecting shell, and the distance between the electric field stages of two adjacent stages is greater than 1.4 times of the pole spacing.
  • the electric field has two levels, that is, the first electric field and the second electric field, and the first electric field and the second electric field are connected in series through the connecting shell.
  • the above-mentioned gas in this embodiment may be the gas intended to enter the engine or the gas discharged from the engine.
  • the electric field generating unit in this embodiment can be applied to an electric field device. As shown in FIG. 2, it includes a dust removal electric field anode 4051 and a dust removal electric field cathode 4052 for generating an electric field.
  • the dust removal electric field anode 4051 and the dust removal electric field cathode 4052 are respectively connected to the power supply.
  • the two electrodes are electrically connected, the power source is a DC power source, and the dust removal electric field anode 4051 and the dust removal electric field cathode 4052 are electrically connected to the anode and the cathode of the DC power source, respectively.
  • the dedusting electric field anode 4051 has a positive electric potential
  • the dedusting electric field cathode 4052 has a negative electric potential.
  • the DC power supply in this embodiment may specifically be a DC high-voltage power supply.
  • a discharge electric field is formed between the dust removal electric field anode 4051 and the dust removal electric field cathode 4052, and the discharge electric field is an electrostatic field.
  • the dust removal electric field anode 4051 in this embodiment is a hollow regular hexagonal tube
  • the dust removal electric field cathode 4052 is a rod shape
  • the dust removal electric field cathode 4052 is inserted in the dust removal electric field anode 4051
  • the length of the dust removal electric field anode 4051 The length of the dust removal electric field cathode 4052 is 2 cm.
  • the dust removal electric field anode 4051 includes a fluid channel.
  • the fluid channel includes an inlet end and an outlet end.
  • the dust removal electric field cathode 4052 is placed in the fluid channel.
  • the cathode 4052 extends in the direction of the fluid channel.
  • the inlet end of the anode 4051 of the dust removal electric field is flush with the near inlet end of the cathode 4052 of the dust removal electric field.
  • ⁇ 90°
  • the distance between the dedusting electric field anode 4051 and the dedusting electric field cathode 4052 is 20mm, and furthermore, under the action of the dedusting electric field anode 4051 and the dedusting electric field cathode 4052, it is resistant to high temperature impact.
  • the electric field device provided in this embodiment can be used to remove particles in the air, is resistant to high temperature impact, and can collect more granular dust, ensuring that the dust collection efficiency of the electric field generating unit is higher.
  • An electric field temperature of 200°C corresponds to a dust collection efficiency of 99.9%; an electric field temperature of 400°C corresponds to a dust collection efficiency of 90%; an electric field temperature of 500°C corresponds to a dust collection efficiency of 50%.
  • the electric field device includes an electric field stage composed of a plurality of the above-mentioned electric field generating units, and there are multiple electric field stages so as to effectively improve the dust collection efficiency of the electric field device by using a plurality of dust collecting units.
  • each electric field anode has the same polarity
  • each electric field cathode has the same polarity.
  • the electric field stages of the plurality of electric field stages are connected in series, and the series electric field stages are connected by a connecting shell.
  • the distance between the electric field stages of two adjacent stages is greater than 1.4 times of the pole spacing.
  • the electric field has two levels, namely the first electric field and the second electric field, and the first electric field and the second electric field are connected in series through the connecting shell.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Treating Waste Gases (AREA)

Abstract

本发明提供一种电场装置，包括电场装置入口、电场装置出口、电场阴极和电场阳极，所述电场阴极和所述电场阳极用于产生电离电场；所述电场阳极长度为10-90mm，所述电场阴极长度为10-90mm。本发明解决了电场发生单元及电场装置耐高温的问题。

Description

一种电场装置 技术领域
本发明属于电场技术领域，具体涉及一种电场装置。
背景技术
通常电场装置包括电场阳极和电场阴极，电场阳极为中空的管，电场阴极穿设于电场阳极，电场阳极和电场阴极的两端均齐平，电场方向基本是从电场阴极到电场阳极，但这种电场结构的放电效率、处理效率通常较低，且能耗较高。现有电场中还存在耦合现象即带电物质会在电场两电极之间反复循环运动形成电场耦合消耗，导致电场处理效率降低、能耗增大。现有电场仅存在一种带电方式，使得容易带电的低比电阻物质荷电后，很快失电，对这部分物质的处理效率较低。而且当温度过高时，电场会出现击穿、出现间歇性失效，导致处理效率降低。
因此，现有电场装置存在体积大、耗能高、处理效率低等缺陷。
发明内容
鉴于以上所述现有技术的缺点，本发明的目的在于提供一种电场装置，用于解决现有电场装置耗电量大、体积大、成本高、处理效率低等中的至少一个技术问题。
为实现上述目的及其他相关目的，本发明提供以下示例：
1.本发明提供的示例1：一种电场装置，包括电场装置入口、电场装置出口、电场阴极和电场阳极，所述电场阴极和所述电场阳极用于产生电离电场。
2.本发明提供的示例2：包括上述示例1，其中，所述电场装置还包括电场装置入口、电场装置出口；所述电场阳极包括第一阳极部和第二阳极部，所述第一阳极部靠近所述电场装置入口，第二阳极部靠近所述电场装置出口，所述第一阳极部和所述第二阳极部之间设置有至少一个阴极支撑板。
3.本发明提供的示例3：包括上述示例1或2，其中，所述电场装置还包括绝缘机构，用于实现所述阴极支撑板和所述电场阳极之间的绝缘。
4.本发明提供的示例4：包括上述示例3，其中，所述电场阳极和所述电场阴极之间形成电场流道，所述绝缘机构设置在所述电场流道外。
5.本发明提供的示例5：包括上述示例3或4，其中，所述绝缘机构包括绝缘部和隔热部；所述绝缘部的材料采用陶瓷材料或玻璃材料。
6.本发明提供的示例6：包括上述示例5，其中，所述绝缘部为伞状串陶瓷柱、伞状串玻璃柱、柱状串陶瓷柱或柱状玻璃柱，伞内外或柱内外挂釉。
7.本发明提供的示例7：包括上述示例6，其中，伞状串陶瓷柱或伞状串玻璃柱的外缘与所述电场阳极的距离是电场距离的1.4倍以上，伞状串陶瓷柱或伞状串玻璃柱的伞突边 间距总和是伞状串陶瓷柱或伞状串玻璃柱的绝缘间距1.4倍以上，伞状串陶瓷柱或伞状串玻璃柱的伞边内深总长是伞状串陶瓷柱或伞状串玻璃柱的绝缘距离1.4倍以上。
8.本发明提供的示例8：包括上述示例2至7中的任一项，其中，所述第一阳极部的长度是所述电场阳极长度的1/10至1/4、1/4至1/3、1/3至1/2、1/2至2/3、2/3至3/4，或3/4至9/10。
9.本发明提供的示例9：包括上述示例2至8中的任一项，其中，所述第一阳极部的长度是足够的长，以清除部分灰尘，减少积累在所述绝缘机构和所述阴极支撑板上的灰尘，减少灰尘造成的电击穿。
10.本发明提供的示例10：包括上述示例1至9中的任一项，其中，所述电场阴极包括至少一根电极棒。
11.本发明提供的示例11：包括上述示例10，其中，所述电极棒的直径不大于3mm。
12.本发明提供的示例12：包括上述示例10或11，其中，所述电极棒的形状呈针状、多角状、毛刺状、螺纹杆状或柱状。
13.本发明提供的示例13：包括上述示例1至12中的任一项，其中，所述电场阳极由中空的管束组成。
14.本发明提供的示例14：包括上述示例13中的任一项，其中，所述中空的管束的管内切圆直径取值范围为5mm-400mm。
15.本发明提供的示例15：包括上述示例13或14，其中，所述电场阳极管束的中空的截面采用圆形或多边形。
16.本发明提供的示例16：包括上述示例15，其中，所述多边形为六边形。
17.本发明提供的示例17：包括上述示例13至16中的任一项，其中，所述电场阳极的管束呈蜂窝状。
18.本发明提供的示例18：包括上述示例1至17中的任一项，其中，所述电场阴极穿射于所述电场阳极内。
19.本发明提供的示例19：包括上述示例1至18中的任一项，其中，所述电场装置还包括辅助电场单元，用于产生与所述电离电场不平行的辅助电场。
20.本发明提供的示例20：包括上述示例1至18中的任一项，其中，所述电场装置还包括辅助电场单元，所述电离电场包括流道，所述辅助电场单元用于产生与所述流道不垂直的辅助电场。
21.本发明提供的示例21：包括上述示例19或20，其中，所述辅助电场单元包括第一电极，所述辅助电场单元的第一电极设置在或靠近所述电离电场的进口。
22.本发明提供的示例22：包括上述示例21，其中，所述第一电极为阴极。
23.本发明提供的示例23：包括上述示例21或22，其中，所述辅助电场单元的第一电极是所述电场阴极的延伸。
24.本发明提供的示例24：包括上述示例21至23中的任一项，其中，所述辅助电场单元的第一电极与所述电场阳极具有夹角α，且0°＜α≤125°、或45°≤α≤125°、或60°≤α≤100°、或α＝90°。
25.本发明提供的示例25：包括上述示例19至24中的任一项，其中，所述辅助电场单元包括第二电极，所述辅助电场单元的第二电极设置在或靠近所述电离电场的出口。
26.本发明提供的示例26：包括上述示例25，其中，所述第二电极为阳极。
27.本发明提供的示例27：包括上述示例25或26，其中，所述辅助电场单元的第二电极是所述电场阳极的延伸。
28.本发明提供的示例28：包括上述示例25至27中的任一项，其中，所述辅助电场单元的第二电极与所述电场阴极具有夹角α，且0°＜α≤125°、或45°≤α≤125°、或60°≤α≤100°、或α＝90°。
29.本发明提供的示例29：包括上述示例19至22中的任一项，其中，所述辅助电场单元的第一电极与所述电离电场的电场阳极、电场阴极独立设置。
30.本发明提供的示例30：包括上述示例19至20、25和26中的任一项，其中，所述辅助电场单元的第二电极与所述电离电场的电场阳极、电场阴极独立设置。
31.本发明提供的示例31：包括上述示例1至30中的任一项，其中，所述电场阳极的工作面积与所述电场阴极的放电面积的比为1.667：1-1680：1。
32.本发明提供的示例32：包括上述示例1至31中的任一项，其中，所述电场阳极的工作面积与所述电场阴极的放电面积的比为6.67：1-56.67：1。
33.本发明提供的示例33：包括上述示例1至32中的任一项，其中，所述电场阴极直径为1-3毫米，所述电场阳极与所述电场阴极的极间距为2.5-139.9毫米；所述电场阳极的工作面积与所述电场阴极的放电面积的比为1.667：1-1680：1。
34.本发明提供的示例34：包括上述示例1至33中的任一项，其中，所述电场阳极和所述电场阴极的极间距小于150mm。
35.本发明提供的示例35：包括上述示例1至34中的任一项，其中，所述电场阳极与所述电场阴极的极间距为2.5-139.9mm。
36.本发明提供的示例36：包括上述示例1至35中的任一项，其中，所述电场阳极与所述电场阴极的极间距为5-100mm。
37.本发明提供的示例37：包括上述示例1至36中的任一项，其中，所述电场阳极长度为10-180mm。
38.本发明提供的示例38：包括上述示例1至37中的任一项，其中，所述电场阳极长度为60-180mm。
39.本发明提供的示例39：包括上述示例1至36中的任一项，其中，所述电场阳极长度为10-90mm。
40.本发明提供的示例40：包括上述示例1至39中的任一项，其中，所述电场阴极长度为30-180mm。
41.本发明提供的示例41：包括上述示例1至40中的任一项，其中，所述电场阴极长度为54-176mm。
42.本发明提供的示例42：包括上述示例1至39中的任一项，其中，所述电场阴极长度为10-90mm。
43.本发明提供的示例43：包括上述示例31至41中的任一项，其中，当运行时，所述电离电场的耦合次数≤3。
44.本发明提供的示例44：包括上述示例19至41中的任一项，其中，当运行时，所述电离电场的耦合次数≤3。
45.本发明提供的示例45：包括上述示例1至41中的任一项，其中，所述电场阳极的工作面积与所述电场阴极的放电面积的比、所述电场阳极与所述电场阴极之间的极间距、所述电场阳极长度以及所述电场阴极长度使所述电离电场的耦合次数≤3。
46.本发明提供的示例46：包括上述示例1至45中的任一项，其中，所述电离电场电压的取值范围为1kv-50kv。
47.本发明提供的示例47：包括上述示例1至46中的任一项，其中，所述电场装置包括若干个电场级，各所述电场级包括若干个电场发生单元，所述电场发生单元可以有一个或多个；所述电场发生单元包括所述电场阳极和所述电场阴极。
48.本发明提供的示例48：包括上述示例47，其中，所述电场级为两个以上时，各电场级之间串联。
49.本发明提供的示例49：包括上述示例1至48中的任一项，其中，所述电场装置还包括若干连接壳体，串联电场级通过所述连接壳体连接。
50.本发明提供的示例50：包括上述示例49，其中，相邻的电场级的距离是所述电场阳极与所述电场阴极之间的极间距的1.4倍以上。
51.本发明提供的示例51：包括上述示例1至50中的任一项，其中，所述电场装置还包括前置电极，所述前置电极在所述电场装置入口与所述电场阳极和所述电场阴极形成的电离电场之间。
52.本发明提供的示例52：包括上述示例51，其中，所述前置电极呈面状、网状、孔 板状、或板状。
53.本发明提供的示例53：包括上述示例51或52，其中，所述前置电极上设有至少一个通孔。
54.本发明提供的示例54：包括上述示例53，其中，所述通孔呈多角形、圆形、椭圆形、正方形、长方形、梯形、或菱形。
55.本发明提供的示例55：包括上述示例53或54，其中，所述通孔的孔径为0.1-3毫米。
56.本发明提供的示例56：包括上述示例51至55中的任一项，其中，所述前置电极为固体、液体、气体分子团、或等离子体中的一种或多种形态的组合。
57.本发明提供的示例57：包括上述示例51至56中的任一项，其中，所述前置电极为导电混合态物质、生物体自然混合导电物质、或物体人工加工形成导电物质。
58.本发明提供的示例58：包括上述示例51至57中的任一项，其中，所述前置电极为304钢或石墨。
59.本发明提供的示例59：包括上述示例51至57中的任一项，其中，所述前置电极为含离子导电液体。
60.本发明提供的示例60：包括上述示例51至59中的任一项，其中，所述前置电极垂直于所述电场阳极。
61.本发明提供的示例61：包括上述示例51至60中的任一项，其中，所述前置电极与所述电场阳极相平行。
62.本发明提供的示例62：包括上述示例51至61中的任一项，其中，所述前置电极采用金属丝网。
63.本发明提供的示例63：包括上述示例51至62中的任一项，其中，所述前置电极与所述电场阳极之间的电压不同于所述电场阴极与所述电场阳极之间的电压。
64.本发明提供的示例64：包括上述示例51至63中的任一项，其中，所述前置电极与所述电场阳极之间的电压小于起始起晕电压。
65.本发明提供的示例65：包括上述示例51至64中的任一项，其中，所述前置电极与所述电场阳极之间的电压为0.1-2kv/mm。
66.本发明提供的示例66：包括上述示例51至65中的任一项，其中，所述电场装置包括流道，所述前置电极位于所述流道中；所述前置电极的截面面积与流道的截面面积比为99％-10％、或90-10％、或80-20％、或70-30％、或60-40％、或50％。
67.本发明提供的示例67：一种减少除尘电场耦合的方法，包括以下步骤：
选择电场阳极参数或/和电场阴极参数以减少电场耦合次数。
68.本发明提供的示例68：包括示例67，其中，包括选择所述电场阳极的工作面积与电场阴极的放电面积的比。
69.本发明提供的示例69：包括示例68，其中，包括选择所述电场阳极的工作面积与所述电场阴极的放电面积的比为1.667：1-1680：1。
70.本发明提供的示例70：包括示例68，其中，包括选择所述电场阳极的工作面积与所述电场阴极的放电面积的比为6.67：1-56.67：1。
71.本发明提供的示例71：包括示例67至70任一项，其中，包括选择所述电场阴极直径为1-3毫米，所述电场阳极与所述电场阴极的极间距为2.5-139.9毫米；所述电场阳极的工作面积与所述电场阴极的放电面积的比为1.667：1-1680：1。
72.本发明提供的示例72：包括示例67至71任一项，其中，包括选择所述电场阳极和所述电场阴极的极间距小于150mm。
73.本发明提供的示例73：包括示例67至71任一项，其中，包括选择所述电场阳极与所述电场阴极的极间距为2.5-139.9mm。
74.本发明提供的示例74：包括示例67至71任一项，其中，包括选择所述电场阳极与所述电场阴极的极间距为5-100mm。
75.本发明提供的示例75：包括示例67至74任一项，其中，包括选择所述电场阳极长度为10-180mm。
76.本发明提供的示例76：包括示例67至74任一项，其中，包括选择所述电场阳极长度为60-180mm。
77.本发明提供的示例77：包括示例67至76任一项，其中，包括选择所述电场阴极长度为30-180mm。
78.本发明提供的示例78：包括示例67至76任一项，其中，包括选择所述电场阴极长度为54-176mm。
79.本发明提供的示例79：包括示例67至78任一项，其中，包括选择所述电场阴极包括至少一根电极棒。
80.本发明提供的示例80：包括示例79，其中，包括选择所述电极棒的直径不大于3mm。
81.本发明提供的示例81：包括示例79或80，其中，包括选择所述电极棒的形状呈针状、多角状、毛刺状、螺纹杆状或柱状。
82.本发明提供的示例82：包括示例67至81任一项，其中，包括选择所述电场阳极由中空的管束组成。
83.本发明提供的示例83：包括示例82，其中，包括选择所述中空的管束的管内切圆直径取值范围为5mm-400mm。
84.本发明提供的示例84：包括示例83，其中，包括选择所述阳极管束的中空的截面采用圆形或多边形。
85.本发明提供的示例85：包括示例84，其中，包括选择所述多边形为六边形。
86.本发明提供的示例86：包括示例82至85任一项，其中，包括选择所述电场阳极的管束呈蜂窝状。
87.本发明提供的示例87：包括示例67至86任一项，其中，包括选择所述电场阴极穿射于所述电场阳极内。
88.本发明提供的示例88：包括示例67至87任一项，其中，包括选择的所述电场阳极或/和电场阴极尺寸使电场耦合次数≤3。
本发明具有如下有益效果：
采用本发明提供的电场装置可应用于气体除尘技术领域，可有效脱除空气中纳米颗粒。
附图说明
图1为本发明实施例1中电场装置的结构示意图。
图2为本发明实施例2-11、实施例24-27中电场发生单元结构示意图。
图3为本发明实施例2、实施例5、实施例27中图2电场发生单元的A-A视图。
图4为本发明实施例2和实施例5中标注长度和角度的图2电场发生单元的A-A视图。
图5为本发明实施例2、实施例5、实施例27中两个电场级的电场装置结构示意图。
图6为本发明实施例12中电场装置的结构示意图。
图7为本发明实施例14中电场装置的结构示意图。
图8为本发明实施例15中电场装置的结构示意图。
图9为本发明实施例16中电场装置的结构示意图。
具体实施方式
以下由特定的具体实施例说明本发明的实施方式，熟悉此技术的人士可由本说明书所揭露的内容轻易地了解本发明的其他优点及功效。
须知，本说明书所附图式所绘示的结构、比例、大小等，均仅用以配合说明书所揭示的内容，以供熟悉此技术的人士了解与阅读，并非用以限定本发明可实施的限定条件，故不具技术上的实质意义，任何结构的修饰、比例关系的改变或大小的调整，在不影响本发明所能产生的功效及所能达成的目的下，均应仍落在本发明所揭示的技术内容得能涵盖的范围内。同时，本说明书中所引用的如“上”、“下”、“左”、“右”、“中间”及“一”等的用语，亦仅为便于叙述的明了，而非用以限定本发明可实施的范围，其相对关系的改变或调整，在无实质变更技术内容下，当亦视为本发明可实施的范畴。
本发明一实施例中，提供一种电场装置，包括电场装置入口、电场装置出口、电场阴 极和电场阳极，所述电场阴极和所述电场阳极用于产生电离电场。
于本发明一实施例中，所述电场阴极包括若干根阴极丝。阴极丝的直径可为0.1mm-20mm，该尺寸参数根据应用场合及处理要求做调整。于本发明一实施例中阴极丝的直径不大于3mm。于本发明一实施例中阴极丝使用容易放电的金属丝或合金丝，耐温且能支撑自身重量，电化学稳定。于本发明一实施例中阴极丝的材质选用钛。阴极丝的具体形状根据电场阳极的形状调整，例如，若电场阳极的工作面是平面，则阴极丝的截面呈圆形；若电场阳极的工作面是圆弧面，阴极丝需要设计成多面形。阴极丝的长度根据电场阳极进行调整。
于本发明一实施例中，所述电场阴极包括若干阴极棒。于本发明一实施例中，所述阴极棒的直径不大于3mm。于本发明一实施例中阴极棒使用容易放电的金属棒或合金棒。阴极棒的形状可以为针状、多角状、毛刺状、螺纹杆状或柱状等。阴极棒的形状可以根据电场阳极的形状进行调整，例如，若电场阳极的工作面是平面，则阴极棒的截面需要设计成圆形；若电场阳极的工作面是圆弧面，则阴极棒需要设计成多面形。
于本发明一实施例中，电场阴极穿设于电场阳极内。
于本发明一实施例中，电场阳极包括一个或多个并行设置的中空阳极管。当中空阳极管有多个时，全部中空阳极管构成蜂窝状的电场阳极。于本发明一实施例中，中空阳极管的截面可呈圆形或多边形。于本发明一实施例中，中空阳极管的截面为多边形，所述多边形为六边形。若中空阳极管的截面呈圆形，电场阳极和电场阴极之间能形成均匀电场。于本发明一实施例中，中空阳极管的管内切圆直径取值范围为5mm-400mm。
于本发明一实施例中，电场阴极安装在阴极支撑板上，阴极支撑板与电场阳极通过绝缘机构相连接。所述绝缘机构用于实现所述阴极支撑板和所述电场阳极之间的绝缘。于本发明一实施例中，电场阳极包括第一阳极部和第二阳极部，即所述第一阳极部靠近电场装置入口，第二阳极部靠近电场装置出口。阴极支撑板和绝缘机构在第一阳极部和第二阳极部之间，即绝缘机构安装在电离电场中间、或电场阴极中间，可以对电场阴极起到良好的支撑作用，并对电场阴极起到相对于电场阳极的固定作用，使电场阴极和电场阳极之间保持设定的距离。而现有技术中，阴极的支撑点在阴极的端点，难以保持阴极和阳极之间的距离。于本发明一实施例中绝缘机构设置在电场流道外、即电场流道外，以防止或减少气体中的灰尘等聚集在绝缘机构上，导致绝缘机构击穿或导电。
于本发明一实施例中，绝缘机构采用耐高压陶瓷绝缘子，对电场阴极和电场阳极之间进行绝缘。电场阳极也称作一种外壳。
于本发明一实施例中绝缘机构包括绝缘瓷柱。于本发明一实施例中第一阳极部长度占电场阳极总长度的1/10至1/4、1/4至1/3、1/3至1/2、1/2至2/3、2/3至3/4，或3/4至9/10。
于本发明一实施例中，第二阳极部在气体流动方向上位于阴极支撑板和绝缘机构之后。于本发明一实施例中，第一阳极部和第二阳极部可使用不同的电源。
于本发明一实施例中，由于电场阴极和电场阳极之间存在极高电位差，为了防止电场阴极和电场阳极导通，绝缘机构设置在电场阴极和电场阳极之间的电场流道之外。因此，绝缘机构外悬于电场阳极的外侧。于本发明一实施例中绝缘机构可采用非导体耐温材料，比如陶瓷、玻璃等。于本发明一实施例中，完全密闭无空气的材料绝缘要求绝缘隔离厚度>0.3mm/kv；空气绝缘要求>1.4mm/kv。可根据电场阴极和电场阳极之间的极间距的1.4倍以上设置绝缘距离。于本发明一实施例中绝缘机构使用陶瓷，表面上釉；不能使用胶粘或有机材料填充连接，耐温大于350摄氏度。
于本发明一实施例中，绝缘机构包括绝缘部和隔热部。为了使绝缘机构具有抗污功能，绝缘部的材料采用陶瓷材料或玻璃材料。于本发明一实施例中，绝缘部可为伞状串陶瓷柱或玻璃柱，伞内外挂釉。伞状串陶瓷柱或玻璃柱的外缘与电场阳极的距离大于或等于电场距离的1.4倍、即大于或等于极间距的1.4倍。伞状串陶瓷柱或玻璃柱的伞突边间距总和大于或等于伞状串陶瓷柱的绝缘间距的1.4倍。伞状串陶瓷柱或玻璃柱的伞边内深总长大于或等于伞状串陶瓷柱的绝缘距离1.4倍。绝缘部还可为柱状串陶瓷柱或玻璃柱，柱内外挂釉。于本发明一实施例中绝缘部还可呈塔状。
于本发明一实施例中，绝缘部内设置加热棒，当绝缘部周围温度接近露点时，加热棒启动并进行加热。由于使用中绝缘部的内外存在温差，绝缘部的内外、外部容易产生凝露。绝缘部的外表面可能自发或被气体加热产生高温，需要必要的隔离防护，防烫伤。隔热部包括位于绝缘部外部的防护围挡板。于本发明一实施例中绝缘部的尾部需要凝露位置同样需要隔热，防止环境以及散热高温加热凝露组件。
于本发明一实施例中电场装置的电源的引出线使用伞状串陶瓷柱或玻璃柱过墙式连接，墙内使用弹性碰头连接阴极支撑板，墙外使用密闭绝缘防护接线帽插拔连接，引出线过墙导体与墙绝缘距离大于伞状串陶瓷柱或玻璃柱的陶瓷绝缘距离。于本发明一实施例中高压部分取消引线，直接安装在端头上，确保安全，高压模块整体外绝缘使用ip68防护，使用介质换热散热。
于本发明一实施例中电场阳极和电场阴极分别与电源的两个电极电性连接。加载在电场阳极和电场阴极上的电压需选择适当的电压等级，具体选择何种电压等级取决于电场装置的体积、耐温、容尘率等。例如，电压从1kv至50kv；设计时首先考虑耐温条件，极间距与温度的参数：1MM<30度，工作面积大于0.1平方/千立方米/小时，电场长度大于单管内切圆的5倍，控制电场气流流速小于9米/秒。于本发明一实施例中电场阳极由中空阳极管构成、并呈蜂窝状。中空阳极管端口的形状可以为圆形或多边形。于本发明一实施例中 中空阳极管的管内切圆取值范围在5-400mm，对应电压在0.1-120kv之间，中空阳极管对应电流在0.1-30A之间；不同的内切圆对应不同的电晕电压，约为1KV/1MM。
于本发明一实施例中电场装置包括电场级，该电场级包括若干个电场发生单元，电场发生单元可以有一个或多个。电场发生单元包括上述电场阳极和电场阴极，电场发生单元有一个或多个。电场级有多个时，能有效提高电场装置的电离效率。同一电场级中，各电场阳极为相同极性，各电场阴极为相同极性。且电场级有多个时，各电场级之间串联。于本发明一实施例中电场装置还包括若干个连接壳体，串联电场级通过连接壳体连接；相邻两级的电场级的距离是极间距的1.4倍以上。
本发明的发明人研究发现，现有电场装置电离效率差、能耗高的缺点是由上述电场耦合现象引起的。本发明某些实施例通过减小电场耦合次数，可以显著减小电场装置的尺寸(即体积)。
由于发明人发现了电场耦合的作用，并且找到了减少电场耦合次数的方法，本发明获得了预料不到的结果。
本发明提供的减少电场耦合次数的方案如下：
于本发明一实施例中电场阴极和电场阳极之间采用非对称结构。在对称电场中极性粒子受到一个相同大小而方向相反的作用力，极性粒子在电场中往复运动；在非对称电场中，极性粒子受到两个大小不同的作用力，极性粒子向作用力大的方向移动，可以避免产生耦合。
于本发明一实施例中，提供一种电场装置，包括电场装置入口、电场装置出口、电场阴极和电场阳极，所述电场阴极和所述电场阳极用于产生电离电场；
所述电场阳极的工作面积与所述电场阴极的放电面积的比为1.667：1-1680：1。
于本发明一实施例中，所述电场阳极的工作面积与所述电场阴极的放电面积的比为6.67：1-56.67：1。
于本发明一实施例中，所述电场阳极的工作面积与所述电场阴极的放电面积的比使所述电离电场的耦合次数≤3。
于本发明一实施例中，所述电场阳极的工作面积与所述电场阴极的放电面积的比、所述电场阳极与所述电场阴极之间的极间距、所述电场阳极长度以及所述电场阴极长度使所述电离电场的耦合次数≤3。
本发明的电场装置的电场阴极和电场阳极之间形成电离电场。为了减少电离电场发生电场耦合，于本发明一实施例中，减少电场耦合的方法包括如下步骤：选择电场阳极的工作面积与电场阴极的放电面积的比，使电场耦合次数≤3。于本发明一实施例中电场阳极的工作面积与电场阴极的放电面积的比可以为：1.667：1-1680：1；3.334：1-113.34：1；6.67： 1-56.67：1；13.34：1-28.33：1。该实施例选择相对大面积的电场阳极的工作面积和相对极小的电场阴极的放电面积，具体选择上述面积比，可以减少电场阴极的放电面积，减小吸力，扩大电场阳极的面积，扩大吸力，即电场阴极和电场阳极间产生不对称的电极吸力，使负离子或带负离子的物质落入电场阳极的表面，虽极性改变但无法再被电场阴极吸走，并减少电场耦合，实现电场耦合次数≤3。即在电场极间距小于150mm时电场耦合次数≤3，电场能耗低，能够减少电场对负离子或带负离子的物质的耦合消耗，节省电场电能30-50％。工作面积是指电场阳极工作面的面积，比如，若电场阳极呈中空的正六边形管状，工作面积即为中空的正六边形管状的内表面积。放电面积指电场阴极工作面的面积，比如，若电场阴极呈棒状，放电面积即为棒状的外表面积。负离子包括氧气被电离子后得到的氧离子、氮气被电离后得到的氮离子等任何负离子或荷负离子的物质。
于本发明一实施例中，提供一种电场装置，包括电场装置入口、电场装置出口、电场阴极和电场阳极，所述电场阴极和所述电场阳极用于产生电离电场；所述电场阳极长度为10-180mm。
于本发明一实施例中，所述电场阳极长度为60-180mm。
于本发明一实施例中，所述电场阳极长度使所述电离电场的耦合次数≤3。
于本发明一实施例中，提供一种电场装置，包括电场装置入口、电场装置出口、电场阴极和电场阳极，所述电场阴极和所述电场阳极用于产生电离电场；所述电场阴极长度为30-180mm。
于本发明一实施例中，所述电场阴极长度为54-176mm。
于本发明一实施例中，所述电场阳极长度使所述电离电场的耦合次数≤3。
于本发明一实施例中，提供一种电场装置，包括电场装置入口、电场装置出口、电场阴极和电场阳极，所述电场阴极和所述电场阳极用于产生电离电场；所述电场阳极和所述电场阴极的极间距小于150mm。
于本发明一实施例中，所述电场阳极和所述电场阴极的极间距为2.5-139.9mm。
于本发明一实施例中，所述电场阳极和所述电场阴极的极间距为5-100mm。
于本发明一实施例中，所述电场阳极和所述电场阴极的极间距使所述电离电场的耦合次数≤3。
于本发明一实施例中电场阳极的长度可以为10-180mm、10-20mm、20-30mm、60-180mm、30-40mm、40-50mm、50-60mm、60-70mm、70-80mm、80-90mm、90-100mm、100-110mm、110-120mm、120-130mm、130-140mm、140-150mm、150-160mm、160-170mm、170-180mm、60mm、180mm、10mm或30mm。电场阳极的长度是指电场阳极工作面的一端至另一端的最小长度。电场阳极选择此种长度，可以有效减少电场耦合。
于本发明一实施例中电场阳极的长度可以为10-90mm、15-20mm、20-25mm、25-30mm、30-35mm、35-40mm、40-45mm、45-50mm、50-55mm、55-60mm、60-65mm、65-70mm、70-75mm、75-80mm、80-85mm或85-90mm，此种长度的设计可以使电场阳极及电场装置具有耐高温特性，并使得电场装置在高温冲击下具有高效率的处理能力。
于本发明一实施例中电场阴极的长度可以为30-180mm、54-176mm、30-40mm、40-50mm、50-54mm、54-60mm、60-70mm、70-80mm、80-90mm、90-100mm、100-110mm、110-120mm、120-130mm、130-140mm、140-150mm、150-160mm、160-170mm、170-176mm、170-180mm、54mm、180mm、或30mm。电场阴极的长度是指电场阴极工作面的一端至另一端的最小长度。电场阴极选择此种长度，可以有效减少电场耦合。
于本发明一实施例中电场阴极的长度可以为10-90mm、15-20mm、20-25mm、25-30mm、30-35mm、35-40mm、40-45mm、45-50mm、50-55mm、55-60mm、60-65mm、65-70mm、70-75mm、75-80mm、80-85mm或85-90mm，此种长度的设计可以使电场阴极及电场装置具有耐高温特性，并使得电场装置在高温冲击下具有高效率的处理能力。
于本发明一实施例中电场阳极和电场阴极之间的距离可以为5-30mm、2.5-139.9mm、9.9-139.9mm、2.5-9.9mm、9.9-20mm、20-30mm、30-40mm、40-50mm、50-60mm、60-70mm、70-80mm、80-90mm、90-100mm、100-110mm、110-120mm、120-130mm、130-139.9mm、9.9mm、139.9mm、或2.5mm。电场阳极和电场阴极之间的距离也称作极间距。极间距具体是指电场阳极、电场阴极工作面之间的最小垂直距离。此种极间距的选择可以有效减少电场耦合，并使电场装置具有耐高温特性。
于本发明一实施例中，所述电场阴极直径为1-3毫米，所述电场阳极与所述电场阴极的极间距为2.5-139.9毫米；所述电场阳极的工作面积与所述电场阴极的放电面积的比为1.667：1-1680：1。
于一实施例中，本发明提供一种减少电场耦合的方法，包括以下步骤：
使空气通过电场阳极和电场阴极产生的电离电场；
选择所述电场阳极或/和电场阴极。
于本发明一实施例中，选择的所述电场阳极或/和电场阴极尺寸使电场耦合次数≤3。
具体地，选择所述电场阳极的工作面积与电场阴极的放电面积的比。优选地，选择所述电场阳极的工作面积与所述电场阴极的放电面积的比为1.667：1-1680：1。
更为优选地，选择所述电场阳极的工作面积与所述电场阴极的放电面积的比为6.67-56.67：1。
于本发明一实施例中，所述电场阴极直径为1-3毫米，所述电场阳极与所述电场阴极的极间距为2.5-139.9毫米；所述电场阳极的工作面积与所述电场阴极的放电面积的比为 1.667：1-1680：1。
优选地，选择所述电场阳极和所述电场阴极的极间距小于150mm。
优选地，选择所述电场阳极与所述电场阴极的极间距为2.5-139.9mm。更为优选地，选择所述电场阳极与所述电场阴极的极间距为5.0-100mm。
优选地，选择所述电场阳极长度为10-180mm。更为优选地，选择所述电场阳极长度为60-180mm。
优选地，选择所述电场阴极长度为30-180mm。更为优选地，选择所述电场阴极长度为54-176mm。
于本发明一实施例中，所述电场装置还包括辅助电场单元，用于产生与所述电离电场不平行的辅助电场。
于本发明一实施例中，所述电场装置还包括辅助电场单元，所述电离电场包括流道，所述辅助电场单元用于产生与所述流道不垂直的辅助电场。
于本发明一实施例中，所述辅助电场单元包括第一电极，所述辅助电场单元的第一电极设置在或靠近所述电离电场的进口。
于本发明一实施例中，所述第一电极为阴极。
于本发明一实施例中，所述辅助电场单元的第一电极是所述电场阴极的延伸。
于本发明一实施例中，所述辅助电场单元的第一电极与所述电场阳极具有夹角α，且0°＜α≤125°、或45°≤α≤125°、或60°≤α≤100°、或α＝90°。
于本发明一实施例中，所述辅助电场单元包括第二电极，所述辅助电场单元的第二电极设置在或靠近所述电离电场的出口。
于本发明一实施例中，所述第二电极为阳极。
于本发明一实施例中，所述辅助电场单元的第二电极是所述电场阳极的延伸。
于本发明一实施例中，所述辅助电场单元的第二电极与所述电场阴极具有夹角α，且0°＜α≤125°、或45°≤α≤125°、或60°≤α≤100°、或α＝90°。
于本发明一实施例中，所述辅助电场的电极与所述电离电场的电极独立设置。
电场阳极和电场阴极之间的电离电场也称作第一电场。于本发明一实施例中电场阳极和电场阴极之间还形成有与第一电场不平行的第二电场。于本发明另一实施例中，所述第二电场与所述电离电场的流道不垂直。第二电场也称作辅助电场，可以通过一个或两个辅助电极形成当第二电场由一个辅助电极形成时，该辅助电极可以放在电离电场的进口或出口，该辅助电极可以带负电势、或正电势。其中，当所述辅助电极为阴极时，设置在或靠近所述电离电场的进口；所述辅助电极与所述电场阳极具有夹角α，且0°＜α≤125°、或45°≤α≤125°、或60°≤α≤100°、或α＝90°。当所述辅助电极为阳极时，设置在或靠近所述电 离电场的出口；所述辅助电极与所述电场阴极具有夹角α，且0°＜α≤125°、或45°≤α≤125°、或60°≤α≤100°、或α＝90°。当第二电场由两个辅助电极形成时，其中一个辅助电极可以带负电势，另一个辅助电极可以带正电势；一个辅助电极可以放在电离电场的进口，另一个辅助电极放在电离电场的出口。另外，辅助电极可以是电场阴极或电场阳极的一部分，即辅助电极可以是由电场阴极或电场阳极的延伸段构成，此时电场阴极和电场阳极的长度不一样。辅助电极也可以是一个单独的电极，也就是说辅助电极可以不是电场阴极或电场阳极的一部分，此时，第二电场的电压和第一电场的电压不一样，可以根据工作状况单独地控制。所述辅助电极包括所述辅助电场单元中第一电极和/或第二电极。
于本发明一实施例中电场装置包括前置电极，该前置电极在电场装置入口与电场阳极和电场阴极形成的电离电场之间。当气体由电场装置入口流经前置电极时，气体中的颗粒物等将带电。
于本发明一实施例中前置电极的形状可以为面状、网状、孔板状、板状、针棒状、球笼状、盒状、管状、物质自然形态、或物质加工形态。本发明中网状为包括任何有孔结构的形状。当前置电极呈板状、球笼状、盒状或管状时，前置电极可以是无孔结构，也可以是有孔结构。当前置电极为有孔结构时，前置电极上设有一个或多个通孔。于本发明一实施例中通孔的形状可以为多角形、圆形、椭圆形、正方形、长方形、梯形、或菱形。于本发明一实施例中通孔的轮廓大小可以为0.1-3mm、0.1-0.2mm、0.2-0.5mm、0.5-1mm、1-1.2mm、1.2-1.5mm、1.5-2mm、2-2.5mm、2.5-2.8mm、或2.8-3mm。
于本发明一实施例中前置电极的形态可以为固体、液体、气体分子团、等离子体、导电混合态物质、生物体自然混合导电物质、或物体人工加工形成导电物质中的一种或多种形态的组合。当前置电极为固体时，可采用固态金属，比如304钢，或其它固态的导体、比如石墨等。当前置电极为液体时，可以是含离子导电液体。
于本发明一实施例中前置电极垂直于电场阳极。于本发明一实施例中前置电极与电场阳极相平行。于本发明一实施例中前置电极采用金属丝网。于本发明一实施例中前置电极与电场阳极之间的电压不同于电场阴极和电场阳极之间的电压。于本发明一实施例中前置电极与电场阳极之间的电压小于起始起晕电压。起始起晕电压为电场阴极和电场阳极之间的电压的最小值。于本发明一实施例中前置电极与电场阳极之间的电压可以为0.1-2kv/mm。
于本发明一实施例中电场装置包括流道，前置电极位于流道中。于本发明一实施例中前置电极的截面面积与流道的截面面积比为99％-10％、或90-10％、或80-20％、或70-30％、或60-40％、或50％。前置电极的截面面积是指前置电极沿截面上实体部分的面积之和。于本发明一实施例中前置电极带负电势。
本发明提供的电场装置可应用于气体除尘技术领域例如静电除尘装置，还可作为等离 子发生器(日光灯)、臭氧发生器等任何需要电场参与的装置。
下面以本发明提供的电场装置作为静电除尘装置为例进行实施说明，该静电除尘装置的结构与上述电场装置结构相同：
目前还采用电场装置对含尘气体所包含的颗粒进行除尘净化，其基本原理为，利用高压放电产生等离子，使颗粒带电，然后将带电的颗粒吸附至集尘电极上，实现电场除尘。但是现有静电除尘装置存在占用空间较大、耗能高、处理效率低等问题，
本发明提供的电场装置体积小、能耗低，可应用于气体除尘技术领域，某些实施例可有效脱除气体中颗粒物。
于本发明一实施例中电场装置可包括电场阴极和电场阳极，电场阴极与电场阳极之间形成电离电场。气体进入电离电场，气体中的氧气将被电离，并形成大量带有电荷的氧离子，氧离子与气体中粉尘等颗粒物结合，使得颗粒物荷电，电场阳极给带负电荷的颗粒物施加吸附力，使得颗粒物被吸附在电场阳极上，以清除掉气体中的颗粒物。
于本发明一实施例中，电场阳极可包括一个或多个并行设置的中空阳极管。当中空阳极管有多个时，全部中空阳极管构成蜂窝状的电场阳极。于本发明一实施例中，中空阳极管的截面可呈圆形或多边形。若中空阳极管的截面呈圆形，电场阳极和电场阴极之间能形成均匀电场，中空阳极管的内壁不容易积尘。若中空阳极管的截面为三边形时，中空阳极管的内壁上可以形成3个积尘面，3个远角容尘角，此种结构的中空阳极管的容尘率最高。若中空阳极管的截面为四边形，可以获得4个积尘面，4个容尘角，但拼组结构不稳定。若中空阳极管的截面为六边形，可以形成6个积尘面，6个容尘角，积尘面和容尘率达到平衡。若中空阳极管的截面呈更多边形时，可以获得更多的积尘边，但损失容尘率。
于本发明一实施例中绝缘机构设置在电场流道外、即电场流道外，以防止或减少气体中的灰尘等聚集在绝缘机构上，导致绝缘机构击穿或导电。
于本发明一实施例中，第一阳极部在气体流动方向上位于阴极支撑板和绝缘机构之前，第一阳极部能够除去气体中的水，防止水进入绝缘机构，造成绝缘机构短路、打火。另外，第一阳级部能够除去气体中相当一部分的灰尘，当气体通过绝缘机构时，相当一部分的灰尘已被消除，减少灰尘造成绝缘机构短路的可能性。于本发明一实施例中绝缘机构包括绝缘瓷柱。第一阳极部的设计主要是为了保护绝缘瓷柱不被气体中颗粒物等污染，一旦气体污染绝缘瓷柱将会造成电场阳极和电场阴极导通，从而使电场阳极的积尘功能失效，故第一阳极部的设计，能有效减少绝缘瓷柱被污染，提高产品的使用时间。在气体流经电场流道过程中，第一阳极部和电场阴极先接触具有污染性的气体，绝缘机构后接触气体，达到先除尘后经过绝缘机构的目的，减少对绝缘机构造成的污染，延长清洁维护周期，对应电极使用后绝缘支撑。所述第一阳极部的长度是足够的长，以清除部分灰尘，减少积累在所 述绝缘机构和所述阴极支撑板上的灰尘，减少灰尘造成的电击穿。
现有工业静电集尘电场由集尘极、放电极组成，电场各极由极板组成，平行排列为电场各极，电极对荷电粉尘有异性吸附力。但荷电为负极性就被正极吸附，荷电为正极性就被负极板吸附。但吸附后，荷电性就出现反转，趋于和极板同性，即正极板上粉尘会再次趋向负极、负极板上粉尘会趋向正极，这种运动和力是反复无休止产生，就形成电场耦合消耗。电场耦合消耗致使静电吸附粘附力弱的颗粒、液雾等出现效率下滑或失效。从而集尘效率低，且能耗较高。
本发明的发明人研究发现，现有电场装置去除效率差、能耗高的缺点是由电场耦合引起的。本发明通过减小电场耦合次数，可以显著减小电场除尘装置的尺寸(即体积)。比如，将本发明提供的电场装置应用于静电除尘的情况下，本发明的电场除尘装置的尺寸约为现有电离除尘装置尺寸的五分之一。原因是，为了获得可接受的颗粒去除率，现有电场除尘装置中将气体流速设为1m/s左右，而本发明在将气体流速提高到6m/s的情况下，仍能获得较高的颗粒去除率。当处理一给定流量的气体时，随着气体速度的提高，电场除尘装置的尺寸可以减小。
另外，本发明可以显著提高颗粒去除效率。例如，在气体流速为1m/s左右时，现有技术电场除尘装置可以去除发动机排气中大约70％的颗粒物，但是本发明可以去除大约99％的颗粒物，即使在气体流速为6m/s时。
由于发明人发现了电场耦合的作用，并且找到了减少电场耦合次数的方法，本发明获得了上述预料不到的结果。
通常静电集尘电场的除尘效率通常较低，且能耗较高。为解决除尘效率低下等问题，现有技术中集尘电场往往选择多段串联，以提高整体集尘效率。此种多电场串联的方式又会导致集尘装置整体占用空间较大，能耗更高，且单电场的除尘效率实质上仍然很低。
于本发明一实施例中，所述电场装置包括与电场阳极和电场阴极之间不平行的辅助电场。
于本发明一实施例中，所述电场装置还包括辅助电场，所述电离电场包括流道，所述辅助电场与所述流道不垂直。
于本发明一实施例中，辅助电场给电场阳极和电场阴极之间带负电荷的氧离子流施加向后的力，使得电场阳极和电场阴极间带负电荷的氧离子流具有向后的移动速度。当含有待处理物质的气体由前向后流入电离电场的流道，带负电荷的氧离子在向电场阳极且向后移动过程中将与待处理物质相结合，由于氧离子具有向后的移动速度，氧离子在与待处理物质相结合时，两者间不会产生较强的碰撞，从而避免因较强碰撞而造成较大的能量消耗，使得氧离子易于与待处理物质相结合，并使得气体中待处理物质的荷电效率更高，进而在 电场阳极作用下，能将更多的待处理物质收集起来，保证本发明提供的电场装置的除尘效率更高。
电场在应用中，往往会遇到因为氧气含量低而使粉尘荷电不充分，以及粉尘为容易导电物质，荷电后容易失去电子等现象。这些现象直接导致电场集尘失效。为避免这类事情发生，人们普遍认为除尘电场不能应用于氧气稀薄的尾气以及不能荷电成功的低电阻粉尘。比如氧气耗尽的汽车尾气中氧含量极低，最低只有0.3％，几乎无氧可电离，就无法产生氧离子，不能传递电子，粉尘就不能带电。另外对于水雾以及金属粉尘，由于容易带电，也容易失电，使用氧电离后荷电，很快就失效，电场也不能收集这类粉尘。另外，现有技术中静电集尘电场对粉尘等待处理物质的收集效率也较低。
于本发明一实施例中电场装置包括前置电极，该前置电极在电场装置入口与电场阳极和电场阴极形成的电离电场之间。当气体由电场装置入口流经前置电极时，气体中的颗粒物等将带电。
于本发明一实施例中前置电极上设有一个或多个通孔，气体通过所述前置电极上的通孔时，使气体中的颗粒物带电。本发明中当带颗粒物的气体通过前置电极上的通孔时，带颗粒物的气体穿过所述前置电极，提高带颗粒物的气体与前置电极的接触面积，增加带电效率。本发明中前置电极上的通孔为任何允许物质流过前置电极的孔。
于本发明一实施例中，在工作时，在带污染物的气体进入电场阳极和电场阴极形成的电离电场之前，且带颗粒物的气体通过前置电极时，前置电极使气体中的颗粒物带电。当带颗粒物的气体进入电离电场时，电场阳极给带电颗粒物施加吸引力，使所述带电颗粒物向电场阳极移动，直至带电颗粒物附着在电场阳极上。
于本发明一实施例中，所述前置电极将电子导入气体中的颗粒物，电子在位于前置电极和电场阳极之间进行传递，使更多气体中的颗粒物带电。
于本发明一实施例中，所述前置电极和电场阳极之间通过带电颗粒物传导电子、并形成电流。
于本发明一实施例中，所述前置电极通过与气体中的颗粒物接触的方式使气体中颗粒物带电。于本发明一实施例中前置电极通过与气体中的颗粒物接触的方式将电子转移到气体中的颗粒物上，并使气体中的颗粒物带电。
通常静电场耐受气体温度为200℃，超过200℃会引发电场击穿，特别是小型化高效电场，电场长度400毫米、通径300毫米蜂窝管束电场耐受温度为90℃。在90℃以下，这个电场集尘效率达到99％，但温度上升到120℃，电场会出现击穿、出现间歇性失效，引发集尘效率明显下降至50％以下。现有技术解决电场耐高温的方法通常为增大电场阳极和电场阴极的极间距、增大电场阳极和电场阴极的长度，防止电场击穿，而本发明提出减 小电场阳极和电场阴极的长度即缩短电场阳极和电场阴极的长度：电场阳极长度为1-9cm，电场阴极长度为1-9cm，解决电场发生单元及电场装置耐高温的问题，显然，现有技术给出相反的技术启示，本发明克服了技术偏见(增大电场阳极和电场阴极的极间距、增大电场阳极和电场阴极的长度)，采用了人们由于技术偏见而舍弃的技术手段，从而解决了本发明要解决的技术问题。
进一步，本发明提出减小电场阳极和电场阴极的长度即缩短电场阳极和电场阴极的长度：电场阳极长度为1-9cm，电场阴极长度为1-9cm，当200℃烟尘进入后，由于停留时间短，活跃分子串联机会少，不能形成击穿电流，同时电场热变形引发极间短路变形量由于短而减小，更不容易引发击穿，电场装置耐受温度能达到500℃甚至大于500℃，且集尘效率高，高达50％，即本申请的电场发生单元和电场装置兼具高的耐受温度和高的集尘效率，与现有技术相比，本申请的技术效果产生“量”的变化，对于本领域技术人员来说，事先无法预测或推理出来，本申请取得了预料不到的技术效果，当发明产生了预料不到的技术效果时，一方面说明发明具有显著的进步，同时也反映出发明的技术方案是非显而易见的。
本发明一些实施例中，当电场温度为200℃时，对应的集尘效率为99.9％；电场温度为400℃时，对应的集尘效率为90％；当电场温度为500℃时，对应的集尘效率为50％。
下面通过具体实施例来进一步阐述本发明的电场装置及其减少耦合的方法。
实施例1
请参阅图1，显示为本实施例中电场装置的结构示意图。所述电场装置包括电场装置入口1011、前置电极1013、绝缘机构1015。
所述电场装置包括电场阳极10141和设置于电场阳极10141内的电场阴极10142，电场阳极10141与电场阴极10142之间形成电场。所述前置电极1013设置于所述电场装置入口1011处，所述前置电极1013为一导电网板。
具体地，所述电场阳极10141的内部由呈蜂窝状、且中空的阳极管束组组成，阳极管束的端口的形状为六边形。
所述电场阴极10142包括若干根电极棒，其一一对应地穿设所述阳极管束组中的每一阳极管束，其中，所述电极棒的形状呈针状、多角状、毛刺状、螺纹杆状或柱状。所述电场阳极10141的工作面积与电场阴极10142的放电面积的比为1680：1，所述电场阳极10141和电场阴极10142的极间距为9.9mm，电场阳极10141长度为60mm，电场阴极10142长度为54mm。
在本实施例中，所述电场阴极10142的出气端低于所述电场阳极10141的出气端，且所述电场阴极10142的进气端与所述电场阳极10141的进气端齐平，电场阳极10141的出 口端与电场阴极10142的近出口端之间具有夹角α，且α＝90°。
如图1所示，于本发明一实施例中，电场阴极10142安装在阴极支撑板10143上，阴极支撑板10143与电场阳极10141通过绝缘机构1015相连接。所述绝缘机构1015用于实现所述阴极支撑板10143和所述电场阳极10141之间的绝缘。于本发明一实施例中，电场阳极10141包括第一阳极部101412和第二阳极部101411，即所述第一阳极部101412靠近电场装置入口，第二阳极部101411靠近电场装置出口。阴极支撑板和绝缘机构在第一阳极部101412和第二阳极部101411之间，即绝缘机构1015安装在电离电场中间、或电场阴极10142中间，可以对电场阴极10142起到良好的支撑作用，并对电场阴极10142起到相对于电场阳极10141的固定作用，使电场阴极10142和电场阳极10141之间保持设定的距离。
所述绝缘机构1015包括绝缘部和隔热部。所述绝缘部的材料采用陶瓷材料或玻璃材料。所述绝缘部为伞状串陶瓷柱或玻璃柱，或柱状串陶瓷柱或玻璃柱，伞内外或柱内外挂釉。
实施例2
本实施例中电场发生单元可应用于本发明的电场装置，本实施例的电场发生单元结构示意图参见图2，本实施例电场发生单元的A-A视图参见图3，本实施例电场发生单元标注长度和角度的电场发生单元的A-A视图参见图4。
如图2所示，包括用于发生电场的电场阳极4051和电场阴极4052，所述电场阳极4051和电场阴极4052分别与电源的两个电极电性连接，所述电源为直流电源，所述电场阳极4051和电场阴极4052分别与直流电源的阳极和阴极电性连接。本实施例中电场阳极4051具有正电势，电场阴极4052具有负电势。
本实施例中直流电源具体可为直流高压电源。上述电场阳极4051和电场阴极4052之间形成放电电场，该放电电场是一种静电场。
如图2、图3和图4所示，本实施例中电场阳极4051呈中空的正六边形管状，电场阴极4052呈棒状，电场阴极4052穿设在电场阳极4051中。
本实施例还提供一种减少电场耦合的方法，包括如下步骤：选择电场阳极4051的工作面积与电场阴极4052的放电面积的比为6.67：1，电场阳极4051和电场阴极4052的极间距L3为9.9mm，电场阳极4051长度L1为60mm，电场阴极4052长度L2为54mm，所述电场阳极4051包括流体通道，所述流体通道包括进口端与出口端，所述电场阴极4052置于所述流体通道中，所述电场阴极4052沿流体通道的方向延伸，电场阳极4051的进口端与电场阴极4052的近进口端齐平，电场阳极4051的出口端与电场阴极4052的近出口端之间具有夹角α，且α＝118°，进而在电场阳极4051和电场阴极4052的作用下，实现电场 耦合次数≤3，能够减少电场的耦合消耗，节省电场电能30-50％。
本实施例中电场装置包括由多个上述电场发生单元构成的电场级，所述电场级有多个，以利用多个电场发生单元有效提高本电场装置的处理效率。同一电场级中，各电场阳极为相同极性，各电场阴极为相同极性。
多个电场级中各电场级之间串联，串联电场级通过连接壳体连接，相邻两级的电场级的距离大于极间距的1.4倍。本实施例中两个电场级的电场装置结构示意图参见图5，如图5所示，所述电场级为两级即第一级电场4053和第二级电场4054，第一级电场4053和第二级电场4054通过连接壳体4055串联连接。
本实施例采用现有电场耦合次数的检测方法，具体如下：
将红色标记的水雾通入电场中，水雾浓度200毫克/m 3，风速<1.5m/s，从电场阴极运动至电场阳极再运动至电场阴极为一次折返，记为一次耦合，视觉观察水雾折返次数，即为耦合次数。
本实施例提供的电场装置可用来脱除空气中的颗粒物，本实施例在电场阳极4051和电场阴极4052的作用下，能将更多的颗粒物收集起来，实现电场耦合次数≤3，能够减少电场对空气中气溶胶、水雾、油雾、松散光滑颗粒物的耦合消耗，节省电场电能30-50％。本实施例中利用多个电场发生单元科有效提高本电场装置的除尘效率。
实施例3
本实施例中电场发生单元可应用于本发明的电场装置，如图2所示，包括用于发生电场的电场阳极4051和电场阴极4052，所述电场阳极4051和电场阴极4052分别与电源的两个电极电性连接，所述电源为直流电源，所述电场阳极4051和电场阴极4052分别与直流电源的阳极和阴极电性连接。本实施例中电场阳极4051具有正电势，电场阴极4052具有负电势。
本实施例中直流电源具体可为直流高压电源。上述电场阳极4051和电场阴极4052之间形成放电电场，该放电电场是一种静电场。
本实施例中电场阳极4051呈中空的正六边形管状，电场阴极4052呈棒状，电场阴极4052穿设在电场阳极4051中。
本实施例还提供一种减少电场耦合的方法，包括如下步骤：选择电场阳极4051的工作面积与电场阴极4052的放电面积的比为1680：1，电场阳极4051和电场阴极4052的极间距为139.9mm，电场阳极4051长度为180mm，电场阴极4052长度为180mm，所述电场阳极4051包括流体通道，所述流体通道包括进口端与出口端，所述电场阴极4052置于所述流体通道中，所述电场阴极4052沿流体通道的方向延伸，电场阳极4051的进口端与电场阴极4052的近进口端齐平，电场阳极4051的出口端与电场阴极4052的近出口端齐 平，进而在电场阳极4051和电场阴极4052的作用下，实现电场耦合次数≤3，能够减少电场的耦合消耗，节省电场电能20-40％。
本实施例提供的电场装置可用来脱除空气中的颗粒物，本实施例在电场阳极4051和电场阴极4052的作用下，能将更多的颗粒物收集起来，实现电场耦合次数≤3，能够减少电场对空气中气溶胶、水雾、油雾、松散光滑颗粒物的耦合消耗，节省电场电能20-40％。
实施例4
本实施例中电场发生单元可应用于本发明的电场装置，如图2所示，包括用于发生电场的电场阳极4051和电场阴极4052，所述电场阳极4051和电场阴极4052分别与电源的两个电极电性连接，所述电源为直流电源，所述电场阳极4051和电场阴极4052分别与直流电源的阳极和阴极电性连接。本实施例中电场阳极4051具有正电势，电场阴极4052具有负电势。
本实施例中直流电源具体可为直流高压电源。上述电场阳极4051和电场阴极4052之间形成放电电场，该放电电场是一种静电场。
本实施例中电场阳极4051呈中空的正六边形管状，电场阴极4052呈棒状，电场阴极4052穿设在电场阳极4051中。
本实施例还提供一种减少电场耦合的方法，包括如下步骤：选择电场阳极4051的工作面积与电场阴极4052的放电面积的比为1.667：1，电场阳极4051和电场阴极4052的极间距为2.4mm，电场阳极4051长度为30mm，电场阴极4052长度为30mm，所述电场阳极4051包括流体通道，所述流体通道包括进口端与出口端，所述电场阴极4052置于所述流体通道中，所述电场阴极4052沿流体通道的方向延伸，电场阳极4051的进口端与电场阴极4052的近进口端齐平，电场阳极4051的出口端与电场阴极4052的近出口端齐平，进而在电场阳极4051和电场阴极4052的作用下，实现电场耦合次数≤3，能够减少电场的耦合消耗，节省电场电能10-30％。
本实施例提供的电场装置可用来脱除空气中的颗粒物，本实施例在电场阳极4051和电场阴极4052的作用下，能将更多的颗粒物收集起来，实现电场耦合次数≤3，能够减少电场对空气中气溶胶、水雾、油雾、松散光滑颗粒物的耦合消耗，节省电场电能10-30％。
实施例5
本实施例中电场发生单元可应用于本发明半导体制造洁净室系统的电场除尘系统中的电场装置，如图2所示，包括用于发生电场的电场阳极4051和电场阴极4052，所述电场阳极4051和电场阴极4052分别与电源的两个电极电性连接，所述电源为直流电源，所述电场阳极4051和电场阴极4052分别与直流电源的阳极和阴极电性连接。本实施例中电场阳极4051具有正电势，电场阴极4052具有负电势。
本实施例中直流电源具体可为直流高压电源。上述电场阳极4051和电场阴极4052之间形成放电电场，该放电电场是一种静电场。
如图2、图3和图4所示，本实施例中电场阳极4051呈中空的正六边形管状，电场阴极4052呈棒状，电场阴极4052穿设在电场阳极4051中，电场阳极4051的工作面积与电场阴极4052的放电面积的比为6.67：1，所述电场阳极4051和电场阴极4052的极间距L3为9.9mm，电场阳极4051长度L1为60mm，电场阴极4052长度L2为54mm，所述电场阳极4051包括流体通道，所述流体通道包括进口端与出口端，所述电场阴极4052置于所述流体通道中，所述电场阴极4052沿流体通道的方向延伸，电场阳极4051的进口端与电场阴极4052的近进口端齐平，电场阳极4051的出口端与电场阴极4052的近出口端之间具有夹角α，且α＝118°。
本实施例中电场装置包括由多个上述电场发生单元构成的电场级，所述电场级有多个，以利用多个集尘单元有效提高本电场装置的集尘效率。同一电场级中，各电场阳极为相同极性，各电场阴极为相同极性。
多个电场级中各电场级之间串联，串联电场级通过连接壳体连接，相邻两级的电场级的距离大于极间距的1.4倍。如图5示，所述电场级为两级即第一级电场4053和第二级电场4054，第一级电场4053和第二级电场4054通过连接壳体4055串联连接。
本实施例提供的电场装置可用来脱除空气中的颗粒物，在电场阳极4051和电场阴极4052的作用下，能将更多的待处理物质收集起来，保证本电场发生单元的集尘效率更高，典型颗粒pm0.23集尘效率为99.99％以上。
实施例6
本实施例中电场发生单元可应用于本发明的电场装置，如图2所示，包括用于发生电场的电场阳极4051和电场阴极4052，所述电场阳极4051和电场阴极4052分别与电源的两个电极电性连接，所述电源为直流电源，所述电场阳极4051和电场阴极4052分别与直流电源的阳极和阴极电性连接。本实施例中电场阳极4051具有正电势，电场阴极4052具有负电势。
本实施例中直流电源具体可为直流高压电源。上述电场阳极4051和电场阴极4052之间形成放电电场，该放电电场是一种静电场。
本实施例中电场阳极4051呈中空的正六边形管状，电场阴极4052呈棒状，电场阴极4052穿设在电场阳极4051中，电场阳极4051的工作面积与电场阴极4052的放电面积的比为1680：1，所述电场阳极4051和电场阴极4052的极间距为139.9mm，电场阳极4051长度为180mm，电场阴极4052长度为180mm，所述电场阳极4051包括流体通道，所述流体通道包括进口端与出口端，所述电场阴极4052置于所述流体通道中，所述电场阴极 4052沿流体通道的方向延伸，电场阳极4051的进口端与电场阴极4052的近进口端齐平，电场阳极4051的出口端与电场阴极4052的近出口端齐平。
本实施例中电场装置包括由多个上述电场发生单元构成的电场级，所述电场级有多个，以利用多个电场发生单元有效提高本电场装置的集尘效率。同一电场级中，各电场阳极为相同极性，各电场阴极为相同极性。
本实施例提供的电场装置可用来脱除空气中的颗粒物，在电场阳极4051和电场阴极4052的作用下，能将更多的待处理物质收集起来，保证本电场发生单元的集尘效率更高，典型颗粒pm0.23集尘效率为99.99％以上。
实施例7
本实施例中电场发生单元可应用于本发明的电场装置，如图2所示，包括用于发生电场的电场阳极4051和电场阴极4052，所述电场阳极4051和电场阴极4052分别与电源的两个电极电性连接，所述电源为直流电源，所述电场阳极4051和电场阴极4052分别与直流电源的阳极和阴极电性连接。本实施例中电场阳极4051具有正电势，电场阴极4052具有负电势。
本实施例中直流电源具体可为直流高压电源。上述电场阳极4051和电场阴极4052之间形成放电电场，该放电电场是一种静电场。
本实施例中电场阳极4051呈中空的正六边形管状，电场阴极4052呈棒状，电场阴极4052穿设在电场阳极4051中，电场阳极4051的工作面积与电场阴极4052的放电面积的比为1.667：1，所述电场阳极4051和电场阴极4052的极间距为2.4mm。电场阳极4051长度为30mm，电场阴极4052长度为30mm，所述电场阳极4051包括流体通道，所述流体通道包括进口端与出口端，所述电场阴极4052置于所述流体通道中，所述电场阴极4052沿流体通道的方向延伸，电场阳极4051的进口端与电场阴极4052的近进口端齐平，电场阳极4051的出口端与电场阴极4052的近出口端齐平。
本实施例中电场阳极4051及电场阴极4052构成电场发生单元，且该电场发生单元有多个，以利用多个电场发生单元有效提高本电场装置的集尘效率。
本实施例提供的电场装置可用来脱除空气中的颗粒物，在电场阳极4051和电场阴极4052的作用下，能将更多的待处理物质收集起来，保证本电场发生单元的集尘效率更高，典型颗粒pm0.23集尘效率为99.99％以上。
实施例8
本实施例中电场发生单元可应用于本发明的电场装置，如图2所示，包括用于发生电场的电场阳极4051和电场阴极4052，所述电场阳极4051和电场阴极4052分别与电源的两个电极电性连接，所述电源为直流电源，所述电场阳极4051和电场阴极4052分别与直 流电源的阳极和阴极电性连接。本实施例中电场阳极4051具有正电势，电场阴极4052具有负电势。
本实施例中直流电源具体可为直流高压电源。上述电场阳极4051和电场阴极4052之间形成放电电场，该放电电场是一种静电场。
本实施例中电场阳极4051呈中空的正六边形管状，电场阴极4052呈棒状，电场阴极4052穿设在电场阳极4051中。
减少电场耦合的方法，包括如下步骤：选择电场阳极4051的工作面积与电场阴极4052的放电面积的比为27.566:1，电场阳极4051和电场阴极4052的极间距为2.3mm，电场阳极4051长度为5mm，电场阴极4052长度为4mm，所述电场阳极4051包括流体通道，所述流体通道包括进口端与出口端，所述电场阴极4052置于所述流体通道中，所述电场阴极4052沿流体通道的方向延伸，电场阳极4051的进口端与电场阴极4052的近进口端齐平，电场阳极4051的出口端与电场阴极4052的近出口端齐平，进而在电场阳极4051和电场阴极4052的作用下，实现电场耦合次数≤3，能够减少电场的耦合消耗。
本实施例提供的电场装置可用来脱除空气中的颗粒物，在电场阳极4051和电场阴极4052的作用下，能将更多的待处理物质收集起来，保证本电场发生单元的集尘效率更高。
实施例9
本实施例中电场发生单元可应用于本发明的电场装置，如图2所示，包括用于发生电场的电场阳极4051和电场阴极4052，所述电场阳极4051和电场阴极4052分别与电源的两个电极电性连接，所述电源为直流电源，所述电场阳极4051和电场阴极4052分别与直流电源的阳极和阴极电性连接。本实施例中电场阳极4051具有正电势，电场阴极4052具有负电势。
本实施例中直流电源具体可为直流高压电源。上述电场阳极4051和电场阴极4052之间形成放电电场，该放电电场是一种静电场。
本实施例中电场阳极4051呈中空的正六边形管状，电场阴极4052呈棒状，电场阴极4052穿设在电场阳极4051中。
减少电场耦合的方法，包括如下步骤：选择电场阳极4051的工作面积与电场阴极4052的放电面积的比为1.108:1，电场阳极4051和电场阴极4052的极间距为2.3mm，电场阳极051长度为60mm，电场阴极4052长度为200mm，所述电场阳极4051包括流体通道，所述流体通道包括进口端与出口端，所述电场阴极4052置于所述流体通道中，所述电场阴极4052沿流体通道的方向延伸，电场阳极4051的进口端与电场阴极4052的近进口端齐平，电场阳极4051的出口端与电场阴极4052的近出口端齐平，进而在电场阳极4051和电场阴极4052的作用下，实现电场耦合次数≤3，能够减少电场的耦合消耗。
本实施例提供的电场装置可用来脱除空气中的颗粒物，在电场阳极4051和电场阴极4052的作用下，能将更多的待处理物质收集起来，保证本电场发生单元的集尘效率更高。
实施例10
本实施例中电场发生单元可应用于本发明的电场装置，如图2所示，包括用于发生电场的电场阳极4051和电场阴极4052，所述电场阳极4051和电场阴极4052分别与电源的两个电极电性连接，所述电源为直流电源，所述电场阳极4051和电场阴极4052分别与直流电源的阳极和阴极电性连接。本实施例中电场阳极4051具有正电势，电场阴极4052具有负电势。
本实施例中直流电源具体可为直流高压电源。上述电场阳极4051和电场阴极4052之间形成放电电场，该放电电场是一种静电场。
本实施例中电场阳极4051呈中空的正六边形管状，电场阴极4052呈棒状，电场阴极4052穿设在电场阳极4051中。
减少电场耦合的方法，包括如下步骤：选择电场阳极4051的工作面积与电场阴极4052的放电面积的比为3065：1，电场阳极4051和电场阴极4052的极间距为249mm，电场阳极4051长度为2000mm，电场阴极4052长度为180mm，所述电场阳极4051包括流体通道，所述流体通道包括进口端与出口端，所述电场阴极4052置于所述流体通道中，所述电场阴极4052沿流体通道的方向延伸，电场阳极4051的进口端与电场阴极4052的近进口端齐平，电场阳极4051的出口端与电场阴极4052的近出口端齐平，进而在电场阳极4051和电场阴极4052的作用下，实现电场耦合次数≤3。
本实施例提供的电场装置可用来脱除空气中的颗粒物，在电场阳极4051和电场阴极4052的作用下，能将更多的待处理物质收集起来，保证本电场发生单元的集尘效率更高。
实施例11
本实施例中电场发生单元可应用于本发明的电场装置，如图2所示，包括用于发生电场的电场阳极4051和电场阴极4052，所述电场阳极4051和电场阴极4052分别与电源的两个电极电性连接，所述电源为直流电源，所述电场阳极4051和电场阴极4052分别与直流电源的阳极和阴极电性连接。本实施例中电场阳极4051具有正电势，电场阴极4052具有负电势。
本实施例中直流电源具体可为直流高压电源。上述电场阳极4051和电场阴极4052之间形成放电电场，该放电电场是一种静电场。
本实施例中电场阳极4051呈中空的正六边形管状，电场阴极4052呈棒状，电场阴极4052穿设在电场阳极4051中。
减少电场耦合的方法，包括如下步骤：选择电场阳极4051的工作面积与电场阴极4052 的放电面积的比为1.338:1，电场阳极4051和电场阴极4052的极间距为5mm，电场阳极4051长度为2mm，电场阴极4052长度为10mm，所述电场阳极4051包括流体通道，所述流体通道包括进口端与出口端，所述电场阴极4052置于所述流体通道中，所述电场阴极4052沿流体通道的方向延伸，电场阳极4051的进口端与电场阴极4052的近进口端齐平，电场阳极4051的出口端与电场阴极4052的近出口端齐平，进而在电场阳极4051和电场阴极4052的作用下，实现电场耦合次数≤3。
本实施例提供的电场装置可用来脱除空气中的颗粒物，在电场阳极4051和电场阴极4052的作用下，能将更多的待处理物质收集起来，保证本电场发生单元的集尘效率更高。
实施例12
本实施例提供的电场装置的结构示意图参见图6。如图6所示，所述电场装置包括电场阴极5081和电场阳极5082分别与直流电源的阴极和阳极电性连接，辅助电极5083与直流电源的阳极电性连接。本实施例中电场阴极5081具有负电势，电场阳极5082和辅助电极5083均具有正电势。
同时，如图6所示，本实施例中辅助电极5083与电场阳极5082固接。在电场阳极5082与直流电源的阳极电性连接后，也实现了辅助电极5083与直流电源的阳极电性连接，且辅助电极5083与电场阳极5082具有相同的正电势。
如图6所示，本实施例中辅助电极5083可沿前后方向延伸，即辅助电极5083的长度方向可与电场阳极5082的长度方向相同。
如图6所示，本实施例中电场阳极5082呈管状，电场阴极5081呈棒状，电场阴极5081穿设在电场阳极5082中。同时本实施例中上述辅助电极5083也呈管状，辅助电极5083与电场阳极5082构成阳极管5084。阳极管5084的前端与电场阴极5081齐平，阳极管5084的后端向后超出了电场阴极5081的后端，该阳极管5084相比于电场阴极5081向后超出的部分为上述辅助电极5083。即本实施例中电场阳极5082和电场阴极5081的长度相同，电场阳极5082和电场阴极5081在前后方向上位置相对；辅助电极5083位于电场阳极5082和电场阴极5081的后方。这样，辅助电极5083与电场阴极5081之间形成辅助电场。
本实施例提供的电场装置可用于脱除空气中的颗粒物，上述辅助电场给电场阳极5082和电场阴极5081之间带负电荷的氧离子流施加向后的力。当含有待处理物质的气体由前向后流入阳极管5084，带负电荷的氧离子在向电场阳极5082且向后移动过程中将与待处理物质相结合，由于氧离子具有向后的移动速度，氧离子在与待处理物质相结合时，两者间不会产生较强的碰撞，从而避免因较强碰撞而造成较大的能量消耗，使得氧离子易于与待处理物质相结合，并使得气体中待处理物质的荷电效率更高，进而在电场阳极5082及阳极管5084的作用下，能将更多的待处理物质收集起来，保证本电场装置的除尘效率更 高。
另外，如图6所示，本实施例中阳极管5084的后端与电场阴极5081的后端之间具有夹角α，且0°＜α≤125°、或45°≤α≤125°、或60°≤α≤100°、或α＝90°。
本实施例中电场阳极5082、辅助电极5083、及电场阴极5081构成除尘单元，且该除尘单元有多个，以利用多个除尘单元有效提高本电场装置的除尘效率。
本实施例中直流电源具体可为直流高压电源。上述电场阴极5081和电场阳极5082之间形成放电电场，该放电电场是一种静电场。在无上述辅助电极5083的情况下，电场阴极5081和电场阳极5082之间电场中离子流沿垂直于电极方向，且在两电极间折返流动，并导致离子在电极间来回折返消耗。为此，本实施例利用辅助电极5083使电极相对位置错开，形成电场阳极5082和电场阴极5081间相对不平衡，这个不平衡会使电场中离子流发生偏转。本电场装置利用辅助电极5083形成能使离子流具有方向性的电场。本电场装置对顺离子流方向进入电场的颗粒物的收集率比对逆离子流方向进入电场的颗粒物的收集率提高近一倍，从而提高电场积尘效率，减少电场电耗。另外，现有技术中集尘电场的除尘效率较低的主要原因也是粉尘进入电场方向与电场内离子流方向相反或垂直交叉，从而导致粉尘与离子流相互冲撞剧烈并产生较大能量消耗，同时也影响荷电效率，进而使现有技术中电场集尘效率下降，且能耗增加。
本实施例中电场装置在用于收集气体中的粉尘时，气体及粉尘顺离子流方向进入电场，粉尘荷电充分，电场消耗小；单极电场集尘效率会达到99.99％以上。当气体及粉尘逆离子流方向进入电场，粉尘荷电不充分，电场电耗也会增加，集尘效率会在40％-75％。另外，本实施例中电场装置形成的离子流有利于无动力风扇流体输送、增氧、热量交换等。
实施例13
本实施例提供的电场装置，包括电场阴极和电场阳极分别与直流电源的阴极和阳极电性连接，辅助电极与直流电源的阴极电性连接。本实施例中辅助电极和电场阴极均具有负电势，电场阳极具有正电势。
本实施例中辅助电极可与电场阴极固接。这样，在实现电场阴极与直流电源的阴极电性连接后，也实现了辅助电极与直流电源的阴极电性连接。同时，本实施例中辅助电极沿前后方向延伸。
本实施例中电场阳极呈管状，电场阴极呈棒状，电场阴极穿设在电场阳极中。同时本实施例中上述辅助电极也棒状，且辅助电极和电场阴极构成阴极棒。该阴极棒的前端向前超出电场阳极的前端，该阴极棒与电场阳极相比向前超出的部分为上述辅助电极。即本实施例中电场阳极和电场阴极的长度相同，电场阳极和电场阴极在前后方向上位置相对；辅助电极位于电场阳极和电场阴极的前方。这样，辅助电极与电场阳极之间形成辅助电场， 该辅助电场给电场阳极和电场阴极之间带负电荷的氧离子流施加向后的力，使得电场阳极和电场阴极间带负电荷的氧离子流具有向后的移动速度。
本实施例提供的电场装置可用于脱除空气中的颗粒物，当含有待处理物质的气体由前向后流入管状的电场阳极，带负电荷的氧离子在向电场阳极且向后移动过程中将与待处理物质相结合，由于氧离子具有向后的移动速度，氧离子在与待处理物质相结合时，两者间不会产生较强的碰撞，从而避免因较强碰撞而造成较大的能量消耗，使得氧离子易于与待处理物质相结合，并使得气体中待处理物质的荷电效率更高，进而在电场阳极作用下，能将更多的待处理物质收集起来，保证本电场装置的除尘效率更高。
本实施例中电场阳极、辅助电极、及电场阴极构成除尘单元，且该除尘单元有多个，以利用多个除尘单元有效提高本电场装置的除尘效率。
实施例14
本实施例中电场装置的结构示意图参见图7。如图7所示，辅助电极5083沿左右方向延伸。本实施例中辅助电极5083的长度方向与电场阳极5082和电场阴极5081的长度方向不同。且辅助电极5083具体可与电场阳极5082相垂直。
本实施例中电场阴极5081和电场阳极5082分别与直流电源的阴极和阳极电性连接，辅助电极5083与直流电源的阳极电性连接。本实施例中电场阴极5081具有负电势，电场阳极5082和辅助电极5083均具有正电势。
如图7所示，本实施例中电场阴极5081和电场阳极5082在前后方向上位置相对，辅助电极5083位于电场阳极5082和电场阴极5081的后方。这样，辅助电极5083与电场阴极5081之间形成辅助电场，该辅助电场给电场阳极5082和电场阴极5081之间带负电荷的氧离子流施加向后的力。
本实施例提供的电场装置可用于用来脱除空气中的颗粒物，当含有待处理物质的气体由前向后流入电场阳极5082和电场阴极5081之间的电场，带负电荷的氧离子在向电场阳极5082且向后移动过程中将与待处理物质相结合，由于氧离子具有向后的移动速度，氧离子在与待处理物质相结合时，两者间不会产生较强的碰撞，从而避免因较强碰撞而造成较大的能量消耗，使得氧离子易于与待处理物质相结合，并使得气体中待处理物质的荷电效率更高，进而在电场阳极5082的作用下，能将更多的待处理物质收集起来，保证本电场装置的除尘效率更高。
实施例15
本实施例中电场装置的结构示意图参见图8。如图8所示，辅助电极5083沿左右方向延伸。本实施例中辅助电极5083的长度方向与电场阳极5082和电场阴极5081的长度方向不同。且辅助电极5083具体可与电场阴极5081相垂直。
本实施例中电场阴极5081和电场阳极5082分别与直流电源的阴极和阳极电性连接，辅助电极5083与直流电源的阴极电性连接。本实施例中电场阴极5081和辅助电极5083均具有负电势，电场阳极5082具有正电势。
如图8所示，本实施例中电场阴极5081和电场阳极5082在前后方向上位置相对，辅助电极5083位于电场阳极5082和电场阴极5081的前方。这样，辅助电极5083与电场阳极5082之间形成辅助电场，该辅助电场给电场阳极5082和电场阴极5081之间带负电荷的氧离子流施加向后的力，使得电场阳极5082和电场阴极5081间带负电荷的氧离子流具有向后的移动速度。当含有待处理物质的气体由前向后流入电场阳极5082和电场阴极5081之间的电场，带负电荷的氧离子在向电场阳极5082且向后移动过程中将与待处理物质相结合，由于氧离子具有向后的移动速度，氧离子在与待处理物质相结合时，两者间不会产生较强的碰撞，从而避免因较强碰撞而造成较大的能量消耗，使得氧离子易于与待处理物质相结合，并使得气体中待处理物质的荷电效率更高，进而在电场阳极5082的作用下，能将更多的待处理物质收集起来，保证本电场装置的除尘效率更高。
实施例16
本实施例中电场装置的结构示意图参见图9。如图9所示，该电场装置包括依次相通的电场装置入口3085、流道3086、电场流道3087、及电场装置出口3088，流道3086中安装有前置电极3083，前置电极3083的截面面积与流道3086的截面面积比为99％-10％，电场装置还包括电场阴极3081和电场阳极3082，电场流道3087位于电场阴极3081和电场阳极3082之间。
本实施例提供的电场装置可用于脱除空气中的颗粒物，含颗粒物的气体通过电场装置入口3085进入流道3086，安装在流道3086中的前置电极3083将电子传导给部分颗粒物，部分颗粒物带电，当颗粒物由流道3086进入电场流道3087后，电场阳极3082给已带电的颗粒物施加吸引力，带电的颗粒物向电场阳极3082移动，直至该部分带电颗粒物附着在电场阳极3082上，同时，电场流道3087中电场阴极3081和电场阳极3082之间形成电离电场，该电离电场将使另一部分未带电的颗粒物带电，这样另一部分颗粒物在带电后同样会受到电场阳极3082施加的吸引力，并最终附着在电场阳极3082，从而利用上述电场装置使颗粒物带电效率更高，带电更充分，进而保证电场阳极3082能收集更多的颗粒物，并保证本发明电场装置对气体中颗粒物的收集效率更高。
前置电极3083的截面面积是指前置电极3083沿截面上实体部分的面积之和。另外，前置电极3083的截面面积与流道3086的截面面积比可以为99％-10％、或90-10％、或80-20％、或70-30％、或60-40％、或50％。
如图9所示，本实施例中前置电极3083和电场阴极3081均与直流电源的阴极电性连 接，电场阳极3082与直流电源的阳极电性连接。本实施例中前置电极3083和电场阴极3081均具有负电势，电场阳极3082具有正电势。
如图9所示，本实施例中前置电极3083具体可呈网状，即设有若干通孔。这样，当气体流经流道3086时，利用前置电极3083设有通孔的结构特点，便于气体及颗粒物流过前置电极3083，并使气体中颗粒物与前置电极3083接触更加充分，从而使前置电极3083能将电子传导给更多的颗粒物，并使颗粒物的带电效率更高。
如图9所示，本实施例中电场阳极3082呈管状，电场阴极3081呈棒状，电场阴极3081穿设在电场阳极3082中。本实施例中电场阳极3082和电场阴极3081呈非对称结构。当气体流入电场阴极3081和电场阳极3082之间形成的电离电场将使颗粒物带电，且在电场阳极3082施加的吸引力作用下，将带电的颗粒物收集在电场阳极3082的内壁上。
另外，如图9所示，本实施例中电场阳极3082和电场阴极3081均沿前后方向延伸，电场阳极3082的前端沿前后方向上位于电场阴极3081的前端的前方。且如图9所示，电场阳极3082的后端沿前后方向上位于电场阴极3081的后端的后方。本实施例中电场阳极3082沿前后方向上的长度更长，使得位于电场阳极3082内壁上的吸附面面积更大，从而对带有负电势的颗粒物的吸引力更大，并能收集更多的颗粒物。
如图9所示，本实施例中电场阴极3081和电场阳极3082构成电离单元，电离单元有多个，以利用多个电离单元收集更多的颗粒物，并使得本电场装置对颗粒物的收集能力更强，且收集效率更高。
本实施例中上述污染物包括导电性较弱的普通粉尘等、及导电性较强的金属粉尘、雾滴、气溶胶等。本实施例中电场装置，对气体中导电性较弱的普通粉尘，及导电性较强的污染物的收集过程为：当气体通过电场装置入口3085流入流道3086中，气体中导电性较强的金属粉尘、雾滴、或气溶胶等污染物在与前置电极3083相接触时，或与前置电极3083的距离达到一定范围时会直接带负电，随后，全部污染物随气流进入电场流道3087，除尘电场阳极3082给已带负电的金属粉尘、雾滴、或气溶胶等施加吸引力，并将该部分污染物收集起来，同时，除尘电场阳极3082与除尘电场阴极3081形成电离电场，该电离电场通过电离气体中的氧获得氧离子，且带负电荷的氧离子在与普通粉尘结合后，使普通粉尘带负电荷，除尘电场阳极3082给该部分带负电荷的粉尘施加吸引力，并将该部分污染物收集起来，从而将气体中导电性较强和导电性较弱的污染物均收集起来，并使得本电场装置所能收集物质的种类更广泛，且收集能力更强。
本实施例中上述电场阴极3081也称作电晕荷电电极。上述直流电源具体为直流高压电源。前置电极3083和电场阳极3082之间通入直流高压，形成导电回路；电场阴极3081和电场阳极3082之间通入直流高压，形成电离放电电晕电场。本实施例中前置电极3083 为密集分布的导体。当容易带电的粉尘等颗粒物经过前置电极3083时，前置电极3083直接将电子给颗粒物，颗粒物带电，随后被异极的电场阳极3082吸附；同时未带电的颗粒物经过电场阴极3081和电场阳极3082形成的电离区，电离区形成的电离氧会把电子荷电给颗粒物，这样颗粒物继续带电，并被异极的电场阳极3082吸附。
本实施例中电场装置能形成两种及两种以上的上电方式。比如，在气体中氧气充足情况下，可利用电场阴极3081和电场阳极3082之间形成的电离放电电晕电场，电离氧，来使气体中的颗粒物荷电，再利用电场阳极3082收集颗粒物；而在气体中氧气含量过低、或无氧状态、或颗粒物为导电尘雾等时，利用前置电极3083直接使气体中的颗粒物上电，让气体中的颗粒物充分带电后被电场阳极3082吸附。本电场装置让电场可以收集各类粉尘同时，也可以应用在各种含氧量低的环境中，扩大了集尘电场治理粉尘应用范围，提高了集尘效率。本实施例采用上述两种带电方式的电场，可以同时收集容易荷电的高阻值粉尘以及容易上电的低阻值金属粉尘、气溶胶、液雾等。两种上电方式同时使用，电场适用范围扩大。
实施例24
本实施例中电场发生单元，结构示意图如图2所示，包括用于发生电场的除尘电场阳极4051和除尘电场阴极4052，所述除尘电场阳极4051和除尘电场阴极4052分别与电源的两个电极电性连接，所述电源为直流电源，所述除尘电场阳极4051和除尘电场阴极4052分别与直流电源的阳极和阴极电性连接。本实施例中除尘电场阳极4051具有正电势，除尘电场阴极4052具有负电势。
本实施例中直流电源具体可为直流高压电源。上述除尘电场阳极4051和除尘电场阴极4052之间形成放电电场，该放电电场是一种静电场。
本实施例中除尘电场阳极4051呈中空的正六边形管状，除尘电场阴极4052呈棒状，除尘电场阴极4052穿设在除尘电场阳极4051中，除尘电场阳极4051长度为5cm，除尘电场阴极4052长度为5cm，所述除尘电场阳极4051包括流体通道，所述流体通道包括进口端与出口端，所述除尘电场阴极4052置于所述流体通道中，所述除尘电场阴极4052沿流体通道的方向延伸，除尘电场阳极4051的进口端与除尘电场阴极4052的近进口端齐平，除尘电场阳极4051的出口端与除尘电场阴极4052的近出口端齐平，所述除尘电场阳极4051和除尘电场阴极4052的极间距为9.9mm，进而在除尘电场阳极4051和除尘电场阴极4052的作用下，使得其耐高温冲击。
本实施例提供的电场装置可用于用来脱除空气中的颗粒物，耐高温冲击，而且能将更多的呈颗粒状的粉尘收集起来，保证本电场发生单元的集尘效率更高。电场温度为200℃对应的集尘效率为99.9％；电场温度为400℃对应的集尘效率为90％；电场温度为500℃对 应的集尘效率为50％。
本实施例中电场装置包括由多个上述电场发生单元构成的电场级，所述电场级有多个，以利用多个集尘单元有效提高本电场装置的集尘效率。同一电场级中，各除尘电场阳极为相同极性，各除尘电场阴极为相同极性。
实施例25
本实施例中电场发生单元可应用于电场装置，如图2所示，包括用于发生电场的除尘电场阳极4051和除尘电场阴极4052，所述除尘电场阳极4051和除尘电场阴极4052分别与电源的两个电极电性连接，所述电源为直流电源，所述除尘电场阳极4051和除尘电场阴极4052分别与直流电源的阳极和阴极电性连接。本实施例中除尘电场阳极4051具有正电势，除尘电场阴极4052具有负电势。
本实施例中直流电源具体可为直流高压电源。上述除尘电场阳极4051和除尘电场阴极4052之间形成放电电场，该放电电场是一种静电场。
本实施例中除尘电场阳极4051呈中空的正六边形管状，除尘电场阴极4052呈棒状，除尘电场阴极4052穿设在除尘电场阳极4051中，除尘电场阳极4051长度为9cm，除尘电场阴极4052长度为9cm，所述除尘电场阳极4051包括流体通道，所述流体通道包括进口端与出口端，所述除尘电场阴极4052置于所述流体通道中，所述除尘电场阴极4052沿流体通道的方向延伸，除尘电场阳极4051的进口端与除尘电场阴极4052的近进口端齐平，除尘电场阳极4051的出口端与除尘电场阴极4052的近出口端齐平，所述除尘电场阳极4051和除尘电场阴极4052的极间距为139.9mm，进而在除尘电场阳极4051和除尘电场阴极4052的作用下，使得其耐高温冲击。
本实施例提供的电场装置可用于用来脱除空气中的颗粒物，耐高温冲击，而且能将更多的呈颗粒状的粉尘收集起来，保证本电场发生单元的集尘效率更高。电场温度为200℃对应的集尘效率为99.9％；电场温度为400℃对应的集尘效率为90％；电场温度为500℃对应的集尘效率为50％。
本实施例中电场装置包括由多个上述电场发生单元构成的电场级，所述电场级有多个，以利用多个集尘单元有效提高本电场装置的集尘效率。同一电场级中，各存储电场阳极为相同极性，各除尘电场阴极为相同极性。
实施例26
本实施例中电场发生单元可应用于电场装置，如图2所示，包括用于发生电场的除尘电场阳极4051和除尘电场阴极4052，所述除尘电场阳极4051和除尘电场阴极4052分别与电源的两个电极电性连接，所述电源为直流电源，所述除尘电场阳极4051和除尘电场阴极4052分别与直流电源的阳极和阴极电性连接。本实施例中除尘电场阳极4051具有正 电势，除尘电场阴极4052具有负电势。
本实施例中直流电源具体可为直流高压电源。上述除尘电场阳极4051和除尘电场阴极4052之间形成放电电场，该放电电场是一种静电场。
本实施例中除尘电场阳极4051呈中空的正六边形管状，除尘电场阴极4052呈棒状，除尘电场阴极4052穿设在除尘电场阳极4051中，除尘电场阳极4051长度为1cm，除尘电场阴极4052长度为1cm，所述除尘电场阳极4051包括流体通道，所述流体通道包括进口端与出口端，所述除尘电场阴极4052置于所述流体通道中，所述除尘电场阴极4052沿流体通道的方向延伸，除尘电场阳极4051的进口端与除尘电场阴极4052的近进口端齐平，除尘电场阳极4051的出口端与除尘电场阴极4052的近出口端齐平，所述除尘电场阳极4051和除尘电场阴极4052的极间距为2.4mm，进而在除尘电场阳极4051和除尘电场阴极4052的作用下，使得其耐高温冲击。
本实施例提供的电场装置可用于用来脱除空气中的颗粒物，耐高温冲击，而且能将更多的呈颗粒状的粉尘收集起来，保证本电场发生单元的集尘效率更高。电场温度为200℃对应的集尘效率为99.9％；电场温度为400℃对应的集尘效率为90％；电场温度为500℃对应的集尘效率为50％。
本实施例中电场装置包括由多个上述电场发生单元构成的电场级，所述电场级有多个，以利用多个集尘单元有效提高本电场装置的集尘效率。同一电场级中，各除尘电场阳极为相同极性，各除尘电场阴极为相同极性。
多个电场级中各电场级之间串联，串联电场级通过连接壳体连接，相邻两级的电场级的距离大于极间距的1.4倍。所述电场级为两级即第一级电场和第二级电场，第一级电场和第二级电场通过连接壳体串联连接。
本实施例中上述气体可以是欲进入发动机的气体，或发动机排出的气体。
实施例27
本实施例中电场发生单元可应用于电场装置，如图2所示，包括用于发生电场的除尘电场阳极4051和除尘电场阴极4052，所述除尘电场阳极4051和除尘电场阴极4052分别与电源的两个电极电性连接，所述电源为直流电源，所述除尘电场阳极4051和除尘电场阴极4052分别与直流电源的阳极和阴极电性连接。本实施例中除尘电场阳极4051具有正电势，除尘电场阴极4052具有负电势。
本实施例中直流电源具体可为直流高压电源。上述除尘电场阳极4051和除尘电场阴极4052之间形成放电电场，该放电电场是一种静电场。
如图2和图3所示，本实施例中除尘电场阳极4051呈中空的正六边形管状，除尘电场阴极4052呈棒状，除尘电场阴极4052穿设在除尘电场阳极4051中，除尘电场阳极4051 长度为3cm，除尘电场阴极4052长度为2cm，所述除尘电场阳极4051包括流体通道，所述流体通道包括进口端与出口端，所述除尘电场阴极4052置于所述流体通道中，所述除尘电场阴极4052沿流体通道的方向延伸，除尘电场阳极4051的进口端与除尘电场阴极4052的近进口端齐平，除尘电场阳极4051的出口端与除尘电场阴极4052的近出口端之间具有夹角α，且α＝90°，所述除尘电场阳极4051和除尘电场阴极4052的极间距为20mm，进而在除尘电场阳极4051和除尘电场阴极4052的作用下，使得其耐高温冲击。
本实施例提供的电场装置可用于用来脱除空气中的颗粒物，耐高温冲击，而且能将更多的呈颗粒状的粉尘收集起来，保证本电场发生单元的集尘效率更高。电场温度为200℃对应的集尘效率为99.9％；电场温度为400℃对应的集尘效率为90％；电场温度为500℃对应的集尘效率为50％。
本实施例中电场装置包括由多个上述电场发生单元构成的电场级，所述电场级有多个，以利用多个集尘单元有效提高本电场装置的集尘效率。同一电场级中，各电场阳极为相同极性，各电场阴极为相同极性。
多个电场级中各电场级之间串联，串联电场级通过连接壳体连接，相邻两级的电场级的距离大于极间距的1.4倍。如图5所示，所述电场级为两级即第一级电场和第二级电场，第一级电场和第二级电场通过连接壳体串联连接。综上所述，本发明有效克服了现有技术中的种种缺点而具高度产业利用价值。
上述实施例仅例示性说明本发明的原理及其功效，而非用于限制本发明。任何熟悉此技术的人士皆可在不违背本发明的精神及范畴下，对上述实施例进行修饰或改变。因此，举凡所属技术领域中具有通常知识者在未脱离本发明所揭示的精神与技术思想下所完成的一切等效修饰或改变，仍应由本发明的权利要求所涵盖。

Claims (12)

  1. 一种电场装置，其特征在于，包括电场装置入口、电场装置出口、电场阴极和电场阳极，所述电场阴极和所述电场阳极用于产生电离电场；所述电场阳极长度为10-90mm，所述电场阴极长度为10-90mm。
  2. 根据权利要求1任一项所述的电场装置，其特征在于，所述电场阳极的工作面积与所述电场阴极的放电面积的比为1.667：1-1680：1。
  3. 根据权利要求1或2所述的电场装置，其特征在于，所述电场阳极的工作面积与所述电场阴极的放电面积的比为6.67：1-56.67：1。
  4. 根据权利要求1至3任一项所述的电场装置，其特征在于，所述电场阳极和所述电场阴极的极间距小于150mm。
  5. 根据权利要求1至4任一项所述的电场装置，其特征在于，所述电场阳极与所述电场阴极的极间距为2.5-139.9mm。
  6. 根据权利要求1至5任一项所述的电场装置，其特征在于，所述电场阳极与所述电场阴极的极间距为5-100mm。
  7. 根据权利要求1至6任一项所述的电场装置，其特征在于，所述电场阴极直径为1-3毫米，所述电场阳极与所述电场阴极的极间距为2.5-139.9毫米；所述电场阳极的工作面积与所述电场阴极的放电面积的比为1.667：1-1680：1。
  8. 根据权利要求1至7任一项所述的电场装置，其特征在于，所述电场阳极长度为10-180mm。
  9. 根据权利要求1至8任一项所述的电场装置，其特征在于，所述电场阳极长度为60-180mm。
  10. 根据权利要求1至9任一项所述的电场装置，其特征在于，所述电场阴极长度为30-180mm。
  11. 根据权利要求1至10任一项所述的电场装置，其特征在于，所述电场阴极长度为54-176mm。
  12. 根据权利要求1至11任一项所述的电场装置，其特征在于，当运行时，所述电离电场的耦合次数≤3。
PCT/CN2020/092672 2019-05-27 2020-05-27 一种电场装置 WO2020238974A1 (zh)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202090000584.1U CN218834819U (zh) 2019-05-27 2020-05-27 一种电场装置

Applications Claiming Priority (12)

Application Number Priority Date Filing Date Title
CN201910446294 2019-05-27
CN201910446294.3 2019-05-27
CN201910465124 2019-05-30
CN201910465124.X 2019-05-30
CN201910522488.7 2019-06-17
CN201910522488 2019-06-17
CN201910521796.8 2019-06-17
CN201910521793 2019-06-17
CN201910521793.4 2019-06-17
CN201910521796 2019-06-17
PCT/CN2019/111813 WO2020083096A1 (zh) 2018-10-22 2019-10-18 一种发动机排放处理系统和方法
CNPCT/CN2019/111813 2019-10-18

Publications (1)

Publication Number Publication Date
WO2020238974A1 true WO2020238974A1 (zh) 2020-12-03

Family

ID=73552468

Family Applications (7)

Application Number Title Priority Date Filing Date
PCT/CN2020/092678 WO2020238979A1 (zh) 2019-05-27 2020-05-27 一种电场装置及减少电场耦合方法
PCT/CN2020/092672 WO2020238974A1 (zh) 2019-05-27 2020-05-27 一种电场装置
PCT/CN2020/092675 WO2020238976A1 (zh) 2019-05-27 2020-05-27 一种电场装置及减少电场耦合方法
PCT/CN2020/092679 WO2020238980A1 (zh) 2019-05-27 2020-05-27 一种电场装置
PCT/CN2020/092673 WO2020238975A1 (zh) 2019-05-27 2020-05-27 一种电场装置
PCT/CN2020/092676 WO2020238977A1 (zh) 2019-05-27 2020-05-27 一种电场装置及减少电场耦合方法
PCT/CN2020/092677 WO2020238978A1 (zh) 2019-05-27 2020-05-27 一种电场装置及减少电场耦合方法

Family Applications Before (1)

Application Number Title Priority Date Filing Date
PCT/CN2020/092678 WO2020238979A1 (zh) 2019-05-27 2020-05-27 一种电场装置及减少电场耦合方法

Family Applications After (5)

Application Number Title Priority Date Filing Date
PCT/CN2020/092675 WO2020238976A1 (zh) 2019-05-27 2020-05-27 一种电场装置及减少电场耦合方法
PCT/CN2020/092679 WO2020238980A1 (zh) 2019-05-27 2020-05-27 一种电场装置
PCT/CN2020/092673 WO2020238975A1 (zh) 2019-05-27 2020-05-27 一种电场装置
PCT/CN2020/092676 WO2020238977A1 (zh) 2019-05-27 2020-05-27 一种电场装置及减少电场耦合方法
PCT/CN2020/092677 WO2020238978A1 (zh) 2019-05-27 2020-05-27 一种电场装置及减少电场耦合方法

Country Status (2)

Country Link
CN (6) CN113891763A (zh)
WO (7) WO2020238979A1 (zh)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103817007A (zh) * 2014-03-05 2014-05-28 武汉钢铁(集团)公司 横向极板双极静电凝并除尘装置及其除尘方法
KR101596872B1 (ko) * 2015-05-06 2016-02-23 한국산업기술시험원 전기집진장치
CN107747774A (zh) * 2017-11-10 2018-03-02 苏州甫腾智能科技有限公司 一种室内空气净化装置
CN111068916A (zh) * 2018-10-22 2020-04-28 上海必修福企业管理有限公司 一种气体处理系统及方法
WO2020083254A1 (zh) * 2018-10-22 2020-04-30 上海必修福企业管理有限公司 一种空气除尘系统及方法

Family Cites Families (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2205248Y (zh) * 1994-09-13 1995-08-16 郑天安 高效静电除尘器
JP3485729B2 (ja) * 1996-07-31 2004-01-13 アマノ株式会社 電気集塵機用集塵電極部
JP2004167453A (ja) * 2002-11-22 2004-06-17 Mitsubishi Heavy Ind Ltd 除塵装置
US7514047B2 (en) * 2003-01-15 2009-04-07 Toyota Jidosha Kabushiki Kaisha Exhaust gas purifying apparatus
US7025806B2 (en) * 2003-11-25 2006-04-11 Stri{dot over (o)}nAir, Inc. Electrically enhanced air filtration with improved efficacy
CN1827223A (zh) * 2005-03-04 2006-09-06 张寅啸 场效应磁约束除尘器
EP2434112A4 (en) * 2009-05-19 2014-10-22 Univ Utsunomiya DEVICE AND METHOD FOR COMBUSING PARTICULAR SUBSTANCES
CN103566753B (zh) * 2013-11-18 2017-01-18 沈阳工业大学 餐饮油烟一体化处理系统及方法
CN104525376A (zh) * 2014-12-22 2015-04-22 上海龙净环保科技工程有限公司 一种湿式电除尘器分区供电系统及分区供电方法
KR101651034B1 (ko) * 2015-02-02 2016-08-24 원효식 전기집진기 및 그 전기집진기를 포함하는 공기청정 시스템
CN204503331U (zh) * 2015-03-25 2015-07-29 郑尔历 消除和控制pm2.5-pm0.5范围颗粒物的装置
CN204974205U (zh) * 2015-07-04 2016-01-20 佛山市南方丽特克能净科技有限公司 多通道片式静电除尘器
CN205146447U (zh) * 2015-11-25 2016-04-13 珠海格力电器股份有限公司 电极结构及空气净化器
CN105689140B (zh) * 2016-04-15 2018-04-10 湖北强达环保科技股份有限公司 一种高效静电除尘器
CN105855056A (zh) * 2016-05-26 2016-08-17 北票市波迪机械制造有限公司 电除尘器微单元横流式阳极装置
CN106269256A (zh) * 2016-08-10 2017-01-04 福建龙净环保股份有限公司 一种用于烟气净化的电除雾器
CN205949064U (zh) * 2016-08-15 2017-02-15 中冶京诚工程技术有限公司 立式湿式电除尘器及其分级冲洗装置
CN106568126A (zh) * 2016-10-25 2017-04-19 珠海格力电器股份有限公司 一种空气净化装置及方法
CN206444733U (zh) * 2016-12-05 2017-08-29 江苏博际环境工程科技有限公司 一种转炉一次烟气湿式静电深度净化装置
CN206492611U (zh) * 2017-01-18 2017-09-15 青岛鲁德邦大气污染控制研究院有限公司 一种带预荷电电场的静电除雾器
CN107198907A (zh) * 2017-06-16 2017-09-26 江苏科行环保科技有限公司 多管旋流耦合除尘除雾设备
CN107309087A (zh) * 2017-08-10 2017-11-03 环球国合（北京）低碳环保科技有限公司 一种电磁清灰式电除尘
CN107486334A (zh) * 2017-08-10 2017-12-19 环球国合（北京）低碳环保科技有限公司 一种离子风式电除尘
US20220016641A1 (en) * 2018-10-22 2022-01-20 Shanghai Bixiufu Enterprise Management Co., Ltd. Engine emission treatment system and method

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103817007A (zh) * 2014-03-05 2014-05-28 武汉钢铁(集团)公司 横向极板双极静电凝并除尘装置及其除尘方法
KR101596872B1 (ko) * 2015-05-06 2016-02-23 한국산업기술시험원 전기집진장치
CN107747774A (zh) * 2017-11-10 2018-03-02 苏州甫腾智能科技有限公司 一种室内空气净化装置
CN111068916A (zh) * 2018-10-22 2020-04-28 上海必修福企业管理有限公司 一种气体处理系统及方法
WO2020083254A1 (zh) * 2018-10-22 2020-04-30 上海必修福企业管理有限公司 一种空气除尘系统及方法

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
PEI YAN ET AL.,: "Characteristics of negative DC corona discharge in a wire-plate configuration at high temperatures,", SEPARATION AND PURIFICATION TECHNOLOGY,, vol. 139, 8 November 2014 (2014-11-08), XP029116092, ISSN: 1383-5866, DOI: 10.1016/j.seppur.2014.10.026 *

Also Published As

Publication number Publication date
WO2020238975A1 (zh) 2020-12-03
CN113950376A (zh) 2022-01-18
CN218834819U (zh) 2023-04-11
CN113905826A (zh) 2022-01-07
CN114390949A (zh) 2022-04-22
WO2020238978A1 (zh) 2020-12-03
WO2020238979A1 (zh) 2020-12-03
WO2020238977A1 (zh) 2020-12-03
CN113891763A (zh) 2022-01-04
WO2020238980A1 (zh) 2020-12-03
CN114072237A (zh) 2022-02-18
WO2020238976A1 (zh) 2020-12-03

Similar Documents

Publication Publication Date Title
WO2020083257A1 (zh) 一种空气除尘系统及方法
WO2020083173A1 (zh) 车载尾气和空气除尘系统、车辆及方法
WO2020216359A1 (zh) 一种用于半导体制造的洁净室系统及其电场除尘方法
WO2020238974A1 (zh) 一种电场装置
CN114761135A (zh) 一种电场装置及减少电场耦合方法

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 20814943

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 20814943

Country of ref document: EP

Kind code of ref document: A1