WO2020083143A1 - 一种发动机进气除尘系统及方法 - Google Patents

一种发动机进气除尘系统及方法 Download PDF

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Publication number
WO2020083143A1
WO2020083143A1 PCT/CN2019/112109 CN2019112109W WO2020083143A1 WO 2020083143 A1 WO2020083143 A1 WO 2020083143A1 CN 2019112109 W CN2019112109 W CN 2019112109W WO 2020083143 A1 WO2020083143 A1 WO 2020083143A1
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Prior art keywords
electric field
intake
dust removal
anode
cathode
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PCT/CN2019/112109
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English (en)
French (fr)
Inventor
唐万福
段志军
邹永安
奚勇
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上海必修福企业管理有限公司
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Publication of WO2020083143A1 publication Critical patent/WO2020083143A1/zh

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    • 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
    • B03C2201/00—Details of magnetic or electrostatic separation
    • B03C2201/04—Ionising electrode being a wire
    • 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
    • B03C2201/00—Details of magnetic or electrostatic separation
    • B03C2201/08—Ionising electrode being a rod
    • 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
    • B03C2201/00—Details of magnetic or electrostatic separation
    • B03C2201/12—Cleaning the device by burning the trapped particles
    • 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
    • B03C2201/00—Details of magnetic or electrostatic separation
    • B03C2201/22—Details of magnetic or electrostatic separation characterised by the magnetical field, special shape or generation
    • 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
    • B03C2201/00—Details of magnetic or electrostatic separation
    • B03C2201/30—Details of magnetic or electrostatic separation for use in or with vehicles
    • 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
    • B03C3/74—Cleaning the electrodes
    • 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
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00—Road transport of goods or passengers
    • Y02T10/10—Internal combustion engine [ICE] based vehicles
    • Y02T10/12—Improving ICE efficiencies

Definitions

  • the invention belongs to the field of environmental protection and relates to an engine air intake dust removal system and method.
  • the engine air intake system is essential to the function of the engine. It directs air to each cylinder of the engine.
  • Existing engine air intake systems include air filters to remove pollutants from the air. Depending on the location, climate, and season, the air may also contain many pollutants, such as soot, pollen, dust, dirt, leaves, and insects. These contaminants may cause excessive wear of engine parts and may also cause blockage of the intake system.
  • the screen of the engine air intake system usually removes most of the larger particles, such as insects and leaves, while the air filter traps finer particles, such as dust, dirt, and pollen. Generally speaking, air filters can capture 80% to 90% of particles below 5 ⁇ m.
  • an object of the present invention is to provide an engine air intake and dust removal system and method for overcoming at least one shortcoming of the prior art.
  • the present invention uses an ionization dust removal method to remove dust from the engine intake air. This method has no pressure difference and does not cause resistance to air entering the engine.
  • the present study found that the amount of particulate matter such as dust, dirt and pollen in the engine intake has a certain effect on the amount of particulate matter in the exhaust gas emitted by the engine. Reducing the particulate matter content in the engine intake can significantly reduce the particulate matter content in the engine exhaust To ensure that exhaust gas meets emission standards.
  • an auxiliary electric field that is not parallel to the ionizing electric field is provided between the anode and the cathode of the ionizing electric field.
  • the auxiliary electric field can apply a force toward the outlet of the ionizing electric field to the cation, so that the flow rate of oxygen ions to the outlet is greater than the air flow rate. Oxygen-increasing effect, the oxygen content in the intake air of the engine increases, which in turn greatly improves the power of the engine.
  • An intake air dedusting system includes an intake air dedusting system inlet, an intake air dedusting system outlet, and an intake electric field device.
  • Example 2 provided by the present invention includes the above example 1, wherein the intake electric field device includes an intake electric field device inlet, an intake electric field device outlet, an intake dust electric field cathode and an intake dust electric field anode, the inlet The cathode of the gas dedusting electric field and the anode of the air inlet dedusting electric field are used to generate an air inlet ionization dedusting electric field.
  • the intake electric field device includes an intake electric field device inlet, an intake electric field device outlet, an intake dust electric field cathode and an intake dust electric field anode, the inlet The cathode of the gas dedusting electric field and the anode of the air inlet dedusting electric field are used to generate an air inlet ionization dedusting electric field.
  • Example 3 provided by the present invention includes the above example 2, wherein the anode of the intake dust removal electric field includes a first anode portion and a second anode portion, the first anode portion is near the inlet of the intake electric field device, The two anode portions are close to the outlet of the intake electric field device, and at least one cathode support plate is provided between the first anode portion and the second anode portion.
  • Example 4 provided by the present invention includes the above example 3, wherein the intake electric field device further includes an intake insulation mechanism for achieving insulation between the cathode support plate and the anode of the intake dust removal electric field.
  • Example 5 provided by the present invention includes the above example 3, wherein an electric field flow path is formed between the anode of the intake air dust removal electric field and the cathode of the intake air dust removal electric field, and the intake air insulation mechanism is provided on the electric field flow Outside the road.
  • Example 6 provided by the present invention includes the above example 4 or 5, wherein the intake insulation mechanism includes an insulating portion and a heat insulating portion; the material of the insulating portion is a ceramic material or a glass material.
  • Example 7 provided by the present invention includes the above example 6, wherein the insulating portion is an umbrella-shaped string ceramic column, an umbrella-shaped string glass column, a column-shaped string ceramic column or a column-shaped glass column, and the glaze is hung on the inside or outside of the umbrella.
  • the insulating portion is an umbrella-shaped string ceramic column, an umbrella-shaped string glass column, a column-shaped string ceramic column or a column-shaped glass column, and the glaze is hung on the inside or outside of the umbrella.
  • Example 8 provided by the present invention includes the above example 7, wherein the distance between the outer edge of the umbrella-shaped string ceramic column or the umbrella-shaped string glass column and the anode of the intake dust removal electric field is greater than 1.4 times the electric field distance, and the umbrella-shaped string ceramic The sum of the distance between the edge of the umbrella or the glass string of the umbrella-shaped string is 1.4 times greater than the insulation distance of the ceramic string of the umbrella-shaped string or the glass string of the umbrella-shaped string. The insulation distance of the string-shaped ceramic column or the umbrella-shaped string glass column is 1.4 times.
  • Example 9 provided by the present invention: including any one of the above examples 3 to 8, wherein the length of the first anode portion is 1/10 to 1/4, 1 of the length of the anode of the intake dust removal electric field / 4 to 1/3, 1/3 to 1/2, 1/2 to 2/3, 2/3 to 3/4, or 3/4 to 9/10.
  • Example 10 provided by the present invention: including any one of the above examples 3 to 9, wherein the length of the first anode portion is sufficiently long to remove part of dust and reduce accumulation in the intake insulation mechanism And the dust on the cathode support plate to reduce the electrical breakdown caused by the dust.
  • Example 11 provided by the present invention includes any one of the above examples 3 to 10, wherein the second anode portion includes a dust accumulation section and a reserved dust accumulation section.
  • Example 12 provided by the present invention: including any one of the above examples 2 to 11, wherein the cathode of the electric field for dedusting the intake air includes at least one electrode rod.
  • Example 13 provided by the present invention: including the above example 12, wherein the diameter of the electrode rod is not greater than 3 mm.
  • Example 14 provided by the present invention includes the above example 12 or 13, wherein the electrode rod has a needle shape, a polygonal shape, a burr shape, a threaded rod shape or a column shape.
  • Example 15 provided by the present invention includes any one of the above examples 2 to 14, wherein the anode of the intake dust removal electric field is composed of a hollow tube bundle.
  • Example 16 provided by the present invention includes the above Example 15, wherein the hollow cross-section of the anode tube bundle of the intake air dedusting electric field adopts a circle or a polygon.
  • Example 17 provided by the present invention includes the above Example 16, wherein the polygon is a hexagon.
  • Example 18 provided by the present invention: including any one of the above examples 14 to 17, wherein the tube bundle of the anode of the intake air dedusting electric field has a honeycomb shape.
  • Example 19 provided by the present invention includes any one of the above examples 2 to 18, wherein the cathode of the intake air dedusting electric field penetrates into the anode of the intake air dedusting electric field.
  • Example 20 provided by the present invention includes any one of the above examples 2 to 19, wherein when the electric field accumulates dust to a certain degree, the intake electric field device performs a dust removal process.
  • Example 21 provided by the present invention includes the above example 20, wherein the intake electric field device detects an electric field current to determine whether dust accumulation has reached a certain level, and a dust removal process is required.
  • Example 22 provided by the present invention includes the above example 20 or 21, wherein the intake electric field device increases the electric field voltage to perform the dust removal process.
  • Example 23 provided by the present invention: including the above example 20 or 21, wherein the intake electric field device uses the electric field reverse corona discharge phenomenon to perform the dust removal process.
  • Example 24 provided by the present invention includes the above example 20 or 21, wherein the intake electric field device utilizes the phenomenon of electric field counter-corona discharge to increase the electric field voltage, limit the injection current, and cause the sharp occurrence of carbon deposition at the anode The discharge generates plasma that deeply oxidizes the organic components of the dust, breaks the polymer bonds, and forms small-molecule carbon dioxide and water for dust removal.
  • the intake electric field device utilizes the phenomenon of electric field counter-corona discharge to increase the electric field voltage, limit the injection current, and cause the sharp occurrence of carbon deposition at the anode
  • the discharge generates plasma that deeply oxidizes the organic components of the dust, breaks the polymer bonds, and forms small-molecule carbon dioxide and water for dust removal.
  • Example 25 provided by the present invention includes any one of the above examples 2 to 24, wherein the intake electric field device further includes an auxiliary electric field unit for generating an auxiliary that is not parallel to the electric field of the intake ionization and dedusting electric field.
  • Example 26 provided by the present invention includes any one of the above examples 2 to 24, wherein the intake electric field device further includes an auxiliary electric field unit, and the intake ionization and dust removal electric field includes a flow channel, and the auxiliary electric field The unit is used to generate an auxiliary electric field that is not perpendicular to the flow channel.
  • Example 27 provided by the present invention includes the above example 25 or 26, wherein 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 inlet of the intake ionization and dust removal electric field .
  • Example 28 provided by the present invention includes the above example 27, wherein the first electrode is a cathode.
  • Example 29 provided by the present invention: including the above example 27 or 28, wherein the first electrode of the auxiliary electric field unit is an extension of the cathode of the intake dust removal electric field.
  • Example 31 provided by the present invention: including any one of the above examples 25 to 30, wherein 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 intake air The outlet of the ionization dust removal electric field.
  • Example 32 provided by the present invention: including the above example 31, wherein the second electrode is an anode.
  • Example 33 provided by the present invention: including the above example 31 or 32, wherein the second electrode of the auxiliary electric field unit is an extension of the anode of the intake dust removal electric field.
  • Example 35 provided by the present invention includes any one of the above examples 25 to 28, 31 and 32, wherein the electrode of the auxiliary electric field and the electrode of the intake ionization and dedusting electric field are provided independently.
  • Example 36 provided by the present invention includes any one of the above Examples 2 to 35, wherein the ratio of the dust accumulation area of the intake air dedusting electric field anode to the discharge area of the intake air dedusting electric field cathode is 1.667: 1-1680: 1.
  • Example 37 provided by the present invention includes any one of the above Examples 2 to 35, wherein the ratio of the dust accumulation area of the intake air dedusting electric field anode to the discharge area of the intake air dedusting electric field cathode is 6.67: 1-56.67: 1.
  • Example 38 provided by the present invention includes any one of the above Examples 2 to 37, wherein the cathode of the intake air dust removal electric field has a diameter of 1-3 mm, and the anode of the intake air dust removal electric field and the intake air dust removal
  • the pole pitch of the electric field cathode is 2.5-139.9 mm; the ratio of the dust accumulation area of the anode of the intake air dedusting electric field to the discharge area of the cathode of the intake air dedusting electric field is 1.667: 1-1680: 1.
  • Example 39 provided by the present invention: including any one of the above examples 2 to 37, wherein the pole separation between the anode of the intake air dust removal electric field and the cathode of the intake air dust removal electric field is less than 150 mm.
  • Example 40 provided by the present invention includes any one of the above examples 2 to 37, wherein the electrode separation distance between the anode of the intake air dust removal electric field and the cathode of the intake air dust removal electric field is 2.5-139.9 mm.
  • Example 41 provided by the present invention: including any one of the above examples 2 to 37, wherein the pole separation between the anode of the intake air dust removal electric field and the cathode of the intake air dust removal electric field is 5-100 mm.
  • Example 42 provided by the present invention: including any one of the above examples 2 to 41, wherein the anode length of the intake air dust removal electric field is 10-180 mm.
  • Example 43 provided by the present invention: including any one of the above examples 2 to 41, wherein the length of the anode of the intake dust removal electric field is 60-180 mm.
  • Example 44 provided by the present invention: including any one of the above examples 2 to 43, wherein the cathode length of the intake dust removal electric field is 30-180 mm.
  • Example 45 provided by the present invention: including any one of the above examples 2 to 43, wherein the length of the cathode of the intake air dust removal electric field is 54-176 mm.
  • Example 46 provided by the present invention: includes any one of the above examples 36 to 45, wherein, during operation, the coupling number of the electric field of the ionization and dust removal of the intake air is ⁇ 3.
  • Example 47 provided by the present invention includes any one of the above examples 25 to 45, wherein, during operation, the coupling number of the electric field of the ionization and dust removal of the intake air is ⁇ 3.
  • Example 48 provided by the present invention: including any one of the above examples 2 to 47, wherein the value range of the electric field voltage of the intake ionization and dust removal is 1kv-50kv.
  • Example 49 provided by the present invention includes any one of the above examples 2 to 48, wherein the intake electric field device further includes several connection housings, and the series electric field stages are connected through the connection housings.
  • Example 50 provided by the present invention includes the above example 49, wherein the distance between adjacent electric field levels is greater than 1.4 times the pole pitch.
  • Example 51 provided by the present invention includes any one of the above examples 2 to 50, wherein the intake electric field device further includes an intake front electrode, the intake front electrode is in the intake electric field Between the inlet of the device and the intake ionization and dust removal electric field formed by the anode of the intake dust removal electric field and the cathode of the intake dust removal electric field.
  • Example 52 provided by the present invention includes the above example 51, wherein the intake front electrode is dot-shaped, linear, mesh-shaped, orifice-shaped, plate-shaped, needle-rod-shaped, ball cage-shaped, box-shaped, Tube, natural form of material, or material processing form.
  • Example 53 provided by the present invention includes the above example 51 or 52, wherein the intake front electrode is provided with an intake through hole.
  • Example 54 provided by the present invention includes the above example 53, wherein the air intake through hole is polygonal, circular, elliptical, square, rectangular, trapezoidal, or rhombic.
  • Example 55 provided by the present invention includes the above example 53 or 54, wherein the size of the air intake through hole is 0.1-3 mm.
  • Example 56 provided by the present invention: including any one of the above examples 51 to 55, wherein the gas inlet front electrode is in one or more forms of solid, liquid, gas molecular cluster, or plasma The combination.
  • Example 57 provided by the present invention: including any one of the above examples 51 to 56, wherein the intake front electrode is a conductive mixed state substance, a biological natural mixed conductive substance, or an object is artificially processed to form a conductive substance .
  • Example 58 provided by the present invention includes any one of the above examples 51 to 57, wherein the intake front electrode is 304 steel or graphite.
  • Example 59 provided by the present invention: including any one of the above examples 51 to 57, wherein the intake front electrode is an ion-containing conductive liquid.
  • Example 60 provided by the present invention: including any one of the above examples 51 to 59, wherein, during operation, when the gas with pollutants enters the cathode of the intake dust removal electric field and the anode formed by the anode of the intake dust removal electric field Before the gas ionizes the dedusting electric field and the gas with pollutants passes through the intake air front electrode, the intake air front electrode charges the pollutants in the gas.
  • Example 61 provided by the present invention includes the above example 60, wherein, when the gas carrying pollutants enters the intake ionization and dust removal electric field, the anode of the intake dust removal electric field exerts an attractive force on the charged pollutants to cause pollution The object moves toward the anode of the intake dust removal electric field until pollutants adhere to the anode of the intake dust removal electric field.
  • Example 62 provided by the present invention includes the above example 60 or 61, wherein the intake front electrode introduces electrons into pollutants, and the electrons are located between the intake front electrode and the intake dust removal electric field anode The pollutants are transferred between them, so that more pollutants are charged.
  • Example 63 provided by the present invention includes any one of the above examples 60 to 62, wherein between the intake front electrode and the intake dust removal electric field anode, electrons are conducted through pollutants and an electric current is formed.
  • Example 64 provided by the present invention: including any one of the above examples 60 to 63, wherein the intake front electrode charges the pollutant by contact with the pollutant.
  • Example 65 provided by the present invention: including any one of the above examples 60 to 64, wherein the intake front electrode charges pollutants by way of energy fluctuation.
  • Example 66 provided by the present invention includes any one of the above examples 60 to 65, wherein the intake front electrode is provided with an intake through hole.
  • Example 67 provided by the present invention includes any one of the above examples 51 to 66, wherein the intake front electrode is linear and the intake dust removal electric field anode is planar.
  • Example 68 provided by the present invention includes any one of the above examples 51 to 67, wherein the intake front electrode is perpendicular to the intake dust removal electric field anode.
  • Example 69 provided by the present invention includes any one of the above examples 51 to 68, wherein the intake front electrode is parallel to the intake dust removal electric field anode.
  • Example 70 provided by the present invention includes any one of the above examples 50 to 68, wherein the intake front electrode is curved or arc-shaped.
  • Example 71 provided by the present invention includes any one of the above examples 51 to 70, wherein the intake front electrode adopts a wire mesh.
  • Example 72 provided by the present invention includes any one of the above examples 51 to 71, wherein the voltage between the intake front electrode and the intake dust removal electric field anode is different from the intake dust removal electric field The voltage between the cathode and the anode of the intake dust removal electric field.
  • Example 73 provided by the present invention includes any one of the above examples 51 to 72, wherein the voltage between the intake front electrode and the intake dust removal electric field anode is less than the initial halo voltage.
  • Example 74 provided by the present invention: including any one of the above examples 51 to 73, wherein the voltage between the intake front electrode and the intake dust removal electric field anode is 0.1 kv / mm-2 kv / mm.
  • Example 75 provided by the present invention includes any one of the above examples 51 to 74, wherein the intake electric field device includes an intake runner, and the intake front electrode is located in the intake runner;
  • the ratio of the cross-sectional area of the intake front electrode to the cross-sectional area of the intake runner is 99% -10%, or 90-10%, or 80-20%, or 70-30%, or 60-40%, or 50% .
  • Example 76 provided by the present invention includes any one of Examples 2 to 75 above, wherein the intake electric field device includes an intake electret element.
  • Example 77 provided by the present invention includes the above example 76, wherein, when the anode of the intake air electric field and the cathode of the intake air electric field are turned on, the intake electret element is ionized at the intake In the dust removal electric field.
  • Example 78 provided by the present invention includes the above example 76 or 77, wherein the intake electret element is close to the outlet of the intake electric field device, or the intake electret element is provided at the inlet Gas field device outlet.
  • Example 79 provided by the present invention: including any one of the above examples 77 to 78, wherein the anode of the intake air dedusting electric field and the cathode of the intake air dedusting electric field form an intake flow path, and the intake electret The element is arranged in the intake flow channel.
  • Example 80 provided by the present invention includes the above example 79, wherein the intake runner includes an intake runner outlet, the intake electret element is close to the intake runner outlet, or the intake The polar body element is provided at the outlet of the intake flow channel.
  • Example 81 provided by the present invention includes the above example 79 or 80, wherein the cross-section of the intake electret element in the intake flow passage occupies 5% -100% of the cross-section of the intake flow passage.
  • Example 82 provided by the present invention: including the above example 81, wherein the cross section of the intake electret element in the intake flow passage accounts for 10% -90%, 20% -80% of the cross section of the intake flow passage , Or 40% -60%.
  • Example 83 provided by the present invention includes any one of the above examples 76 to 82, wherein the intake air ionization and dust removal electric field charges the intake electret element.
  • Example 84 provided by the present invention includes any one of the above examples 76 to 83, wherein the intake electret element has a porous structure.
  • Example 85 provided by the present invention includes any one of the above examples 76 to 84, wherein the intake electret element is a fabric.
  • Example 86 provided by the present invention: includes any one of the above examples 76 to 85, wherein the inside of the anode of the intake dust removal electric field is tubular, and the exterior of the intake electret element is tubular, the intake The electret element is externally sheathed inside the anode of the air intake dust removal electric field.
  • Example 87 provided by the present invention includes any one of the above examples 76 to 86, wherein the intake electret element and the intake dust removal electric field anode are detachably connected.
  • Example 88 provided by the present invention: including any one of the above examples 76 to 87, wherein the material of the intake electret element includes an inorganic compound having electret properties.
  • Example 89 provided by the present invention includes the above Example 88, wherein the inorganic compound is selected from one or more combinations of oxygen-containing compounds, nitrogen-containing compounds, or glass fibers.
  • Example 90 provided by the present invention includes the above Example 89, wherein the oxygen-containing compound is selected from one or more combinations of metal-based oxides, oxygen-containing complexes, and oxygen-containing inorganic heteropoly acid salts.
  • Example 91 provided by the present invention: including the above example 90, wherein the metal-based oxide is selected from aluminum oxide, zinc oxide, zirconium oxide, titanium oxide, barium oxide, tantalum oxide, silicon oxide, lead oxide, tin oxide One or more combinations.
  • the metal-based oxide is selected from aluminum oxide, zinc oxide, zirconium oxide, titanium oxide, barium oxide, tantalum oxide, silicon oxide, lead oxide, tin oxide One or more combinations.
  • Example 92 provided by the present invention: including the above example 90, wherein the metal-based oxide is alumina.
  • Example 93 provided by the present invention includes the above Example 90, wherein the oxygen-containing composite is selected from one or more combinations of titanium-zirconium composite oxide or titanium-barium composite oxide.
  • Example 94 provided by the present invention includes the above Example 90, wherein the oxygen-containing inorganic heteropoly acid salt is selected from one or more combinations of zirconium titanate, lead zirconate titanate, or barium titanate.
  • Example 95 provided by the present invention: including the above example 89, wherein the nitrogen-containing compound is silicon nitride.
  • Example 96 provided by the present invention: including any one of the above examples 76 to 95, wherein the material of the intake electret element includes an organic compound having electret properties.
  • Example 97 provided by the present invention includes the above example 96, wherein the organic compound is selected from one or more combinations of fluoropolymer, polycarbonate, PP, PE, PVC, natural wax, resin, and rosin .
  • Example 98 provided by the present invention includes the above example 97, wherein the fluoropolymer is selected from one or more of polytetrafluoroethylene, polyperfluoroethylene propylene, soluble polytetrafluoroethylene, and polyvinylidene fluoride Kinds of combinations.
  • Example 99 provided by the present invention: including the above example 97, wherein the fluoropolymer is polytetrafluoroethylene.
  • Example 100 includes any one of the above examples 1 to 99, and further includes an air intake equalizing device.
  • Example 101 provided by the present invention includes the above example 100, wherein the inlet air equalization device forms an inlet formed at the inlet of the inlet dust removal system with the anode of the inlet dust removal electric field and the cathode of the inlet dust removal electric field. Between the gas ionization and dust removal electric field, when the anode of the air intake and dust removal electric field is a cuboid, the air intake equalizing device includes: an air intake pipe provided on one side of the anode of the air intake and dust removal electric field, and an air intake pipe provided on the other side Side air outlet pipe; wherein, the air inlet pipe is opposite to the air outlet pipe.
  • Example 102 provided by the present invention includes the above example 100, wherein the intake air equalization device forms an inlet formed at the entrance of the intake dust removal system with the anode of the intake dust removal electric field and the cathode of the intake dust removal electric field. Between the gas ionization and dedusting electric field, when the anode of the air intake and dust removing electric field is a cylinder, the air intake and air distribution device is composed of several rotatable air distribution blades.
  • Example 103 provided by the present invention includes the above example 100, wherein the first venturi plate air equalizing mechanism of the intake air equalization device and the second venturi plate provided at the outlet end of the anode of the intake dust removal electric field are both Wind mechanism, the first venturi plate air equalizing mechanism is provided with an air inlet hole, the second venturi plate air equalizing mechanism is provided with an air outlet hole, and the air inlet hole and the air outlet hole are arranged in a staggered arrangement, And the front side air intake and side air exhaust, forming a cyclone structure.
  • Example 104 includes any one of the above examples 1 to 103, wherein it further includes an ozone removing device for removing or reducing ozone generated by the intake electric field device, the ozone removing device Between the outlet of the intake electric field device and the outlet of the intake dust removal system.
  • Example 105 provided by the present invention includes the above example 104, wherein the ozone removing device further includes an ozone digester.
  • Example 106 provided by the present invention includes the above example 105, wherein the ozone digester is selected from at least one of an ultraviolet ozone digester and a catalytic ozone digester.
  • Example 107 provided by the present invention: includes any one of the above examples 1 to 106, wherein it further includes a centrifugal separation mechanism.
  • Example 108 provided by the present invention includes the above example 107, wherein the centrifugal separation mechanism includes an airflow turning channel, and the airflow turning channel can change the flow direction of the airflow.
  • Example 109 provided by the present invention includes the above example 108, wherein the gas flow turning channel can guide the gas to flow in the circumferential direction.
  • Example 110 provided by the present invention includes the above example 107 or 108, wherein the air flow turning channel is spiral or conical.
  • Example 111 provided by the present invention: includes any one of the above examples 107 to 110, wherein the centrifugal separation mechanism includes a separation cylinder.
  • Example 112 provided by the present invention includes the above example 111, wherein the airflow turning channel is provided in the separation cylinder, and a dust outlet is provided at the bottom of the separation cylinder.
  • Example 113 provided by the present invention includes the above example 111 or 112, wherein an air inlet communicating with the first end of the air flow turning channel is provided on the side wall of the separation cylinder.
  • Example 114 provided by the present invention includes any one of the above examples 111 to 113, wherein the top of the separation cylinder is provided with an air outlet that communicates with the second end of the air flow turning channel.
  • Example 115 provided by the present invention: includes any one of the above examples 1 to 114, wherein it further includes an engine.
  • Example 116 provided by the present invention: a method for dedusting an engine intake electric field, including the following steps:
  • Example 117 provided by the present invention: The engine intake electric field dust removal method including Example 116, wherein the dust removal process is completed using the electric field back-corona discharge phenomenon.
  • Example 118 provided by the present invention: The engine intake electric field dust removal method including Example 116, wherein the electric field reverse corona discharge phenomenon is used to increase the voltage, limit the injection current, and complete the dust removal process.
  • Example 119 provided by the present invention: The engine intake electric field dust removal method including Example 116, wherein the electric field reverse corona discharge phenomenon is used to increase the voltage and limit the injection current to cause the rapid discharge occurring at the position of the anode dust to generate plasma The plasma oxidizes the organic components of the dust deeply, breaks the polymer bonds, and forms small molecules of carbon dioxide and water to complete the dust removal process.
  • Example 120 provided by the present invention: The engine intake electric field dust removal method including any one of Examples 116 to 119, wherein when the electric field device detects that the electric field current increases to a given value, the electric field device performs dust removal deal with.
  • Example 121 provided by the present invention: The engine intake electric field dust removal method including any one of Examples 116 to 120, wherein the dust removal electric field cathode includes at least one electrode rod.
  • Example 122 provided by the present invention: The engine intake electric field dust removal method including Example 121, wherein the diameter of the electrode rod is not greater than 3 mm.
  • Example 123 provided by the present invention: An engine intake electric field dust removal method including Example 121 or 122, wherein the electrode rod has a needle shape, a polygonal shape, a burr shape, a threaded rod shape, or a column shape.
  • Example 124 provided by the present invention: An engine intake electric field dust removal method including any one of Examples 116 to 123, wherein the dust removal electric field anode is composed of a hollow tube bundle.
  • Example 125 provided by the present invention: The engine intake electric field dust removal method including Example 124, wherein the hollow cross section of the anode tube bundle adopts a circle or a polygon.
  • Example 126 provided by the present invention: An engine intake electric field dust removal method including Example 125, wherein the polygon is a hexagon.
  • Example 127 provided by the present invention: The engine intake electric field dust removal method including any one of Examples 124 to 126, wherein the tube bundle of the dust removal electric field anode is honeycomb-shaped.
  • Example 128 provided by the present invention: The engine intake electric field dust removal method including any one of Examples 116 to 127, wherein the dust removal electric field cathode penetrates the dust removal electric field anode.
  • Example 129 provided by the present invention: The engine intake electric field dust removal method including any one of Examples 116 to 128, wherein when the detected electric field current increases to a given value, the dust removal process is performed.
  • Example 130 provided by the present invention: a method for adding oxygen to the intake air of an engine, including the following steps:
  • An electric field is generated in the flow channel, the electric field is not perpendicular to the flow channel, and the electric field includes an inlet and an outlet.
  • Example 131 provided by the present invention: a method of adding oxygen to engine intake air including Example 130, wherein the electric field includes a first anode and a first cathode, the first anode and the first cathode forming the flow path , The flow channel connects the inlet and the outlet.
  • Example 132 provided by the present invention: The method of adding oxygen to an intake air of an engine including any of Examples 130 to 131, wherein the first anode and the first cathode ionize oxygen in the intake air.
  • Example 133 provided by the present invention: The method of adding oxygen to engine intake air including any one of Examples 130 to 132, wherein the electric field includes a second electrode disposed at or near the inlet.
  • Example 134 provided by the present invention: the method of adding oxygen to the intake air of the engine including Example 133, wherein the second electrode is a cathode.
  • Example 135 provided by the present invention: a method of adding oxygen to engine intake air including example 133 or 134, wherein the second electrode is an extension of the first cathode.
  • Example 137 provided by the present invention: The method of adding oxygen to engine intake air including any one of Examples 130 to 136, wherein the electric field includes a third electrode disposed at or near the outlet.
  • Example 138 provided by the present invention: the method of adding oxygen to the intake air of the engine including Example 137, wherein the third electrode is an anode.
  • Example 139 provided by the present invention: a method of adding oxygen to engine intake air including example 137 or 138, wherein the third electrode is an extension of the first anode.
  • Example 141 provided by the present invention: The method for adding oxygen to engine intake air according to any one of Examples 135 to 140, wherein the third electrode is provided separately from the first anode and the first cathode.
  • Example 142 provided by the present invention: The method for adding oxygen to the intake air of an engine including any one of Examples 133 to 141, wherein the second electrode is provided separately from the first anode and the first cathode.
  • Example 143 provided by the present invention: The method of adding oxygen to the intake air of an engine including any one of Examples 131 to 142, wherein the first cathode includes at least one electrode rod.
  • Example 144 provided by the present invention: The method for adding oxygen to intake air of an engine including any one of Examples 131 to 143, wherein the first anode is composed of a hollow tube bundle.
  • Example 145 provided by the present invention: The method of adding oxygen to the intake air of the engine including Example 144, wherein the hollow cross section of the anode tube bundle adopts a circle or a polygon.
  • Example 146 provided by the present invention: the method of adding oxygen to the intake air of the engine including Example 145, wherein the polygon is a hexagon.
  • Example 147 provided by the present invention: The method for adding oxygen to engine intake air according to any one of Examples 144 to 146, wherein the tube bundle of the first anode is honeycomb-shaped.
  • Example 148 provided by the present invention: The method of adding oxygen to the intake air of an engine, including any one of Examples 131 to 147, wherein the first cathode penetrates the first anode.
  • Example 149 provided by the present invention: a method for adding oxygen to engine intake air including any one of examples 131 to 148, wherein the electric field acts on oxygen ions in the flow channel to increase the flow of oxygen ions and increase the Oxygen content in the outlet intake.
  • Example 150 provided by the present invention: a method for reducing electric field coupling of engine intake dust removal, including the following steps:
  • Example 151 provided by the present invention: a method for reducing coupling of an engine intake dust removal electric field including Example 150, which includes selecting a ratio of a dust collecting area of the intake dust removal electric field anode to a discharge area of the intake dust removal electric field cathode.
  • Example 152 provided by the present invention: A method for reducing coupling of an engine intake dust removal electric field including Example 151, which includes selecting a dust accumulation area of the intake dust removal electric field anode and a discharge area of the intake dust removal electric field cathode The ratio is 1.667: 1-1680: 1.
  • Example 153 provided by the present invention: The method for reducing the electric field coupling of the engine intake dust removal field including Example 151, which includes selecting the dust accumulation area of the anode of the intake dust removal electric field and the discharge area of the cathode of the intake dust removal electric field The ratio is 6.67: 1-56.67: 1.
  • Example 154 provided by the present invention: The method for reducing the electric field coupling of the engine intake dust removal including any one of Examples 150 to 153, wherein the method includes selecting the cathode diameter of the intake dust removal electric field to be 1-3 mm, and the intake air
  • the pole spacing between the anode of the dust removal electric field and the cathode of the intake dust removal electric field is 2.5-139.9 mm; the ratio of the dust accumulation area of the anode of the intake dust removal electric field to the discharge area of the cathode of the intake dust removal electric field is 1.667: 1-1680 :1.
  • Example 155 provided by the present invention: A method including any one of Examples 150 to 154 for reducing the coupling of an engine intake dust removal electric field, including selecting the pole spacing of the intake dust removal electric field anode and the intake dust removal electric field cathode Less than 150mm.
  • Example 156 provided by the present invention: A method including any one of Examples 150 to 154 to reduce coupling of an engine intake dust removal electric field, including selecting a pole spacing between the intake dust removal electric field anode and the intake dust removal electric field cathode It is 2.5-139.9mm.
  • Example 157 provided by the present invention: A method for reducing coupling of an engine intake dust removal electric field including any one of Examples 150 to 154, including selecting a pole interval between the intake dust removal electric field anode and the intake dust removal electric field cathode 5-100mm.
  • Example 158 provided by the present invention: A method including any one of Examples 150 to 157, for reducing the electric field coupling of the engine intake dust removal field, including selecting the anode length of the intake dust removal electric field to be 10-180 mm.
  • Example 159 provided by the present invention: A method for reducing coupling of an engine intake dust removal electric field including any one of examples 150 to 157, wherein the method includes selecting the intake dust removal electric field anode length to be 60-180 mm.
  • Example 160 provided by the present invention: A method for reducing coupling of an electric field of an engine's intake dust removal field including any one of Examples 150 to 159, wherein the method includes selecting the cathode length of the intake dust removal electric field to be 30-180 mm.
  • Example 161 provided by the present invention: A method for reducing coupling of an engine intake dust electric field including any one of Examples 150 to 159, which includes selecting the cathode length of the intake dust electric field to be 54-176 mm.
  • Example 162 provided by the present invention: The method for reducing the electric field coupling of the engine intake dust removal including any one of Examples 150 to 161, wherein the method includes selecting the cathode of the intake dust removal electric field to include at least one electrode rod.
  • Example 163 provided by the present invention: a method for reducing electric field coupling of engine intake dust removal including Example 162, which includes selecting that the diameter of the electrode rod is not greater than 3 mm.
  • Example 164 provided by the present invention: A method for reducing electric field coupling of engine intake dust removal including Example 162 or 163, which includes selecting the shape of the electrode rod to be needle, polygon, burr, threaded rod or column .
  • Example 165 provided by the present invention: A method including any one of Examples 150 to 164, for reducing an electric field coupling of an engine intake dust removal electric field, including selecting the anode of the intake dust removal electric field to be composed of a hollow tube bundle.
  • Example 166 provided by the present invention: The method for reducing the electric field coupling of the engine intake dust removal including Example 165, wherein the hollow cross section including the anode tube bundle is selected to adopt a circular or polygonal shape.
  • Example 167 provided by the present invention: the method for reducing electric field coupling of engine intake dust removal including Example 166, wherein the method includes selecting the polygon to be a hexagon.
  • Example 168 provided by the present invention: The method for reducing the electric field coupling of engine intake dust removal including any one of Examples 165 to 167, wherein the tube bundle including selecting the anode of the intake dust removal electric field is honeycomb-shaped.
  • Example 169 provided by the present invention: A method including any one of Examples 150 to 168 for reducing the coupling of an engine intake dust removal electric field, including selecting the cathode of the intake dust removal electric field to penetrate the anode of the intake dust removal electric field .
  • Example 170 provided by the present invention: A method for reducing coupling of an engine intake dust removal electric field including any one of Examples 150 to 169, wherein the size of the intake dust removal electric field anode or / and the intake dust removal electric field cathode is selected such that The number of electric field couplings ⁇ 3.
  • Example 171 provided by the present invention an engine intake dust removal method, including the following steps:
  • Example 172 provided by the present invention: An engine intake dust removal method including Example 171, wherein the intake electret element is close to an intake electric field device outlet, or the intake electret element is provided at the intake Electric field device outlet.
  • Example 173 provided by the present invention: The engine intake dust removal method including Example 171, wherein the intake dust removal electric field anode and the intake dust removal electric field cathode form an intake flow path, and the intake electret element is provided In the intake runner.
  • Example 174 provided by the present invention: The engine intake dust removal method including Example 173, wherein the intake runner includes an intake runner outlet, and the intake electret element is close to the intake runner outlet, or, The intake electret element is provided at the outlet of the intake runner.
  • Example 175 provided by the present invention: The engine intake dust removal method including any one of Examples 171 to 174, wherein when the intake ionization dust removal electric field has no electrified driving voltage, the charged intake electret element is used to adsorb Particulate matter in the air.
  • Example 176 provided by the present invention: The engine intake dust removal method including Example 174, wherein after the charged intake electret element adsorbs certain particulate matter in the intake, it is replaced with a new intake electret ⁇ ⁇ Body components.
  • Example 177 provided by the present invention: The engine intake dust removal method including Example 176, in which the intake air ionization dust removal electric field is restarted after being replaced with a new intake electret element to adsorb particulate matter in the intake air and give a new The air intake electret element is charged.
  • Example 178 provided by the present invention: The engine intake dust removing method including any one of Examples 171 to 177, wherein the material of the intake electret element includes an inorganic compound having electret properties.
  • Example 179 provided by the present invention: The engine intake dust removal method including Example 178, wherein the inorganic compound is selected from one or more combinations of oxygen-containing compounds, nitrogen-containing compounds, or glass fibers.
  • Example 180 provided by the present invention: The engine intake dust removal method including Example 179, wherein the oxygen-containing compound is selected from one of metal-based oxides, oxygen-containing composites, and oxygen-containing inorganic heteropoly acid salts Or multiple combinations.
  • the oxygen-containing compound is selected from one of metal-based oxides, oxygen-containing composites, and oxygen-containing inorganic heteropoly acid salts Or multiple combinations.
  • Example 181 provided by the present invention: an engine intake dust removal method including Example 180, wherein the metal-based oxide is selected from aluminum oxide, zinc oxide, zirconium oxide, titanium oxide, barium oxide, tantalum oxide, silicon oxide, One or more combinations of lead oxide and tin oxide.
  • the metal-based oxide is selected from aluminum oxide, zinc oxide, zirconium oxide, titanium oxide, barium oxide, tantalum oxide, silicon oxide, One or more combinations of lead oxide and tin oxide.
  • Example 182 provided by the present invention: The engine intake dust removal method including Example 180, wherein the metal-based oxide is alumina.
  • Example 183 provided by the present invention: The engine intake dust removal method including Example 180, wherein the oxygen-containing composite is selected from one or more combinations of titanium-zirconium composite oxide or titanium-barium composite oxide.
  • Example 184 provided by the present invention: The engine intake dust removal method including Example 180, wherein the oxygen-containing inorganic heteropoly acid salt is selected from one of zirconium titanate, lead zirconate titanate, or barium titanate or Various combinations.
  • Example 185 provided by the present invention: The engine intake dust removal method including Example 179, wherein the nitrogen-containing compound is silicon nitride.
  • Example 186 provided by the present invention: The engine intake dust removal method including any one of Examples 171 to 177, wherein the material of the intake electret element includes an organic compound having electret properties.
  • Example 187 provided by the present invention: an engine intake dust removal method including Example 186, wherein the organic compound is selected from one of fluoropolymer, polycarbonate, PP, PE, PVC, natural wax, resin, and rosin One or more combinations.
  • Example 188 provided by the present invention: The engine intake dust removal method including Example 187, wherein the fluoropolymer is selected from polytetrafluoroethylene, polyperfluoroethylene propylene, soluble polytetrafluoroethylene, and polyvinylidene fluoride One or more combinations.
  • the fluoropolymer is selected from polytetrafluoroethylene, polyperfluoroethylene propylene, soluble polytetrafluoroethylene, and polyvinylidene fluoride One or more combinations.
  • Example 189 provided by the present invention: An engine intake dust removal method including Example 187, wherein the fluoropolymer is polytetrafluoroethylene.
  • Example 190 provided by the present invention: An engine intake dust removal method, characterized in that it includes the following steps: the intake air is subjected to intake air ionization and dust removal to remove or reduce ozone generated by the intake air ionization and dust removal.
  • Example 191 provided by the present invention: An engine intake dust removal method including Example 190, wherein ozone generated by intake ionization dust removal is subjected to ozone digestion.
  • Example 192 provided by the present invention: The engine intake dust removal method including Example 190, wherein the ozone digestion is selected from at least one of ultraviolet digestion and catalytic digestion.
  • FIG. 1 is a schematic structural diagram of an intake dust removal system in an engine intake dust removal system of the present invention in an embodiment.
  • FIG. 2 is a structural diagram of another embodiment of a first water filtering mechanism provided in an intake electric field device in an engine intake dust removal system of the present invention.
  • FIG. 3A is an implementation structure diagram of an air intake equalizing device of an air intake electric field device in an engine air intake dust removal system of the present invention.
  • FIG. 3B is another implementation structure diagram of the intake air equalization device of the intake electric field device in the engine intake dust removal system of the present invention.
  • Fig. 3C is another embodiment structure diagram of the intake air equalization device of the intake electric field device in the engine intake dust removal system of the present invention.
  • 3D is a top structural view of the second venturi plate wind equalizing mechanism in the intake electric field device of the engine intake dust removal system of the present invention.
  • FIG. 4 is a schematic diagram of an intake electric field device according to Embodiment 2 of the present invention.
  • FIG. 5 is a schematic diagram of an intake electric field device according to Embodiment 3 of the present invention.
  • FIG. 6 is a top view of the intake electric field device of FIG. 1 of the present invention.
  • FIG. 7 is a schematic diagram of the cross section of the intake electret element in the intake runner in Embodiment 3 occupying the cross section of the intake runner.
  • FIG. 8 is a schematic diagram of an intake dust removal system according to Embodiment 4 of the present invention.
  • FIG. 9 is a schematic diagram of the structure of the electric field generating unit.
  • Fig. 10 is an A-A view of the electric field generating unit of Fig. 9.
  • Fig. 11 is an A-A view of the electric field generating unit of Fig. 9 marked with length and angle.
  • FIG. 12 is a schematic diagram of the structure of an electric field device with two electric field levels.
  • Embodiment 17 is a schematic structural diagram of an electric field device in Embodiment 17 of the present invention.
  • Embodiment 19 is a schematic structural diagram of an electric field device in Embodiment 19 of the present invention.
  • Embodiment 15 is a schematic structural diagram of an electric field device in Embodiment 20 of the present invention.
  • FIG. 16 is a schematic structural diagram of an intake electric field device in Embodiment 22 of the present invention.
  • the engine intake dust removal system includes a centrifugal separation mechanism.
  • the centrifugal separation mechanism includes an airflow turning channel, which can change the flow direction of the airflow.
  • the flow direction of the gas will change; and the particulate matter in the gas will continue to move in the original direction under the action of inertia until it reaches the side wall of the gas flow turning channel, that is, the centrifugal separation mechanism
  • the inner wall of the collision the particles can not continue to move in the original direction, and fall down under the action of gravity, so that the particles are separated from the gas.
  • the gas flow turning channel can guide the gas to flow in the circumferential direction.
  • the air flow turning channel can be spiral or conical.
  • the centrifugal separation mechanism includes a separation cylinder.
  • the air separation channel is provided in the separation cylinder, and a dust outlet can be provided at the bottom of the separation cylinder.
  • An air inlet communicating with the first end of the air flow steering channel may be provided on the side wall of the separation cylinder.
  • the top of the separation cylinder may be provided with an air outlet communicating with the second end of the air flow steering channel.
  • the air outlet is also called an exhaust port, and the size of the exhaust port can be set according to the required amount of intake air.
  • the gas After the gas flows into the separation cylinder from the air inlet and turns into the channel, the gas will change from linear motion to circular motion, and the particles in the gas will continue to move in a linear direction under the action of inertia until the particles collide with the inner wall of the separation cylinder
  • the particulate matter sinks under the force of gravity, so that the particulate matter is separated from the gas, and the particulate matter is finally discharged from the dust outlet at the bottom, and the gas is finally discharged from the exhaust outlet at the top.
  • the inlet of the intake electric field device communicates with the exhaust port of the centrifugal separation mechanism.
  • the air outlet of the separation cylinder is located at the connection between the separation cylinder and the intake electric field device.
  • the centrifugal separation mechanism may have a bent structure.
  • the shape of the centrifugal separation mechanism may be one shape or a combination of multiple shapes among a ring shape, a zigzag shape, a cross shape, a T shape, an L shape, a concave shape, or a folded shape.
  • the air flow steering channel of the centrifugal separation mechanism has at least one turn. When the gas flows through the turn, the flow direction will change, and the particles in the gas will continue to move in the original direction under the inertia until the particles collide with the inner wall of the centrifugal separation mechanism. When sinking, the particles are detached from the gas and finally discharged from the powder outlet at the lower end, and the gas finally flows out from the exhaust outlet.
  • a first filter layer may be provided at the exhaust port of the centrifugal separation mechanism.
  • the first filter layer may include a metal mesh sheet, and the metal mesh sheet may be disposed perpendicular to the airflow direction. The metal mesh will filter the gas discharged from the exhaust port to filter out the particles that have not been separated from the gas.
  • the engine air intake and dust removal system may include an air intake equalizing device.
  • the air intake equalizing device is arranged before the air intake electric field device, and can evenly pass the airflow entering the air intake electric field device.
  • the anode of the air intake electric field device of the air intake electric field device may be a cube
  • the air intake equalization device may include an air intake pipe on one side of the cathode support plate and an outlet on the other side of the cathode support plate
  • the trachea and the cathode support plate are located at the intake end of the anode of the intake dust removal electric field; wherein, the side where the intake pipe is installed is opposite to the side where the outlet pipe is installed.
  • the air intake equalizing device can make the air flow entering the air intake electric field device evenly pass through the electrostatic field.
  • the anode of the air intake dust removal electric field may be a cylinder
  • the air intake equalizing device is located at the inlet of the air intake dust removal system and the air intake formed by the air intake dust removal electric field anode and the air intake dust removal electric field cathode
  • the air inlet air-equalizing device includes several air-equating blades rotating around the inlet center of the air inlet electric field device.
  • the air intake air-equalization device can make various changes of air intake uniformly pass through the electric field generated by the anode of the air intake dust removal electric field. At the same time, it can keep the temperature inside the anode of the air intake dust removal electric field constant, and the oxygen is sufficient.
  • the air intake equalizing device can make the air flow entering the air intake electric field device evenly pass through the electrostatic field.
  • the air intake equalizing device includes an air inlet plate provided at the air inlet end of the anode of the air intake dust removal electric field and an air outlet plate provided at the air outlet end of the anode of the air intake dust removal electric field.
  • the air outlet is provided with air outlet holes, the air inlet holes and the air outlet holes are arranged in a staggered arrangement, and the front air inlet and the side air outlet form a cyclone structure.
  • the air intake equalizing device can make the air flow entering the air intake electric field device evenly pass through the electrostatic field.
  • the engine intake dust removal system may include an intake dust removal system inlet, an intake dust removal system outlet, and an intake electric field device.
  • the intake electric field device may include an intake electric field device inlet, an intake electric field device outlet, and an intake front electrode between the intake electric field device inlet and the intake electric field device outlet. When the inlet electric field device inlet flows through the inlet front electrode, the particulate matter in the gas will be charged.
  • the intake electric field device includes an intake front electrode.
  • the intake front electrode is formed at the inlet of the intake electric field device and the anode of the intake dust removal electric field and the cathode of the intake dust removal electric field. between.
  • the shape of the intake front electrode may be dot-shaped, linear, mesh-shaped, orifice-shaped, plate-shaped, needle-rod-shaped, ball-cage-shaped, box-shaped, tubular, natural form of substance, or substance Processing form.
  • the intake front electrode has a hole structure, one or more intake through holes are provided on the intake front electrode.
  • the shape of the air intake through hole may be polygon, circle, ellipse, square, rectangle, trapezoid, or rhombus.
  • the outline size of the air intake through hole may be 0.1 to 3 mm, 0.1 to 0.2 mm, 0.2 to 0.5 mm, 0.5 to 1 mm, 1 to 1.2 mm, 1.2 to 1.5 mm, 1.5 to 2 mm, 2 to 2.5mm, 2.5 ⁇ 2.8mm, or 2.8 ⁇ 3mm.
  • the shape of the intake front electrode may be one of solid, liquid, gas molecular group, plasma, conductive mixed state substance, biological natural mixed conductive substance, or artificially processed object to form conductive substance Or a combination of multiple forms.
  • the intake front electrode is solid, solid metal, such as 304 steel, or other solid conductors, such as graphite, can be used.
  • the intake front electrode is a liquid, it may be a conductive liquid containing ions.
  • the air intake front electrode Charge the pollutants in the gas.
  • the anode of the intake dust removal electric field exerts an attractive force on the charged pollutants, so that the pollutants move toward the anode of the intake dust removal electric field until the pollutants adhere to the anode of the intake dust removal electric field .
  • the intake front electrode introduces electrons into the pollutants, and the electrons are transferred between the pollutants between the intake front electrode and the anode of the intake dust removal electric field, so that more pollutants are charged. Between the air intake front electrode and the air intake dedusting electric field anode, electrons are conducted through pollutants and an electric current is formed.
  • the intake front electrode charges the pollutants by contact with the pollutants. In an embodiment of the invention, the intake front electrode charges pollutants by means of energy fluctuations. In an embodiment of the present invention, the intake front electrode transfers electrons to the pollutant by contacting the pollutant and charges the pollutant. In an embodiment of the present invention, the intake front electrode transfers electrons to the pollutants by means of energy fluctuations, and charges the pollutants.
  • the intake front electrode is linear, and the anode of the intake dust removal electric field is planar. In an embodiment of the present invention, the intake front electrode is perpendicular to the anode of the intake dust removal electric field. In an embodiment of the present invention, the intake front electrode is parallel to the anode of the intake dust removal electric field. In an embodiment of the invention, the intake front electrode is curved or arc-shaped. In an embodiment of the present invention, the air intake front electrode uses a wire mesh. In an embodiment of the present invention, the voltage between the intake front electrode and the anode of the intake dust removal electric field is different from the voltage between the cathode of the intake dust removal electric field and the anode of the intake dust removal electric field.
  • the voltage between the air intake front electrode and the air intake dust removal electric field anode is less than the initial halo voltage.
  • the initial halo voltage is the minimum value of the voltage between the cathode of the intake dust removal electric field and the anode of the intake dust removal electric field.
  • the voltage between the air intake front electrode and the air intake dust removal electric field anode may be 0.1-2 kV / mm.
  • the intake electric field device includes an intake runner, and the intake front electrode is located in the intake runner.
  • the ratio of the cross-sectional area of the intake front electrode to the cross-sectional area of the intake runner is 99% -10%, or 90-10%, or 80-20%, or 70-30%, or 60 ⁇ 40%, or 50%.
  • the cross-sectional area of the air intake front electrode refers to the sum of the areas of the air intake front electrode along the solid part of the cross section.
  • the intake front electrode has a negative potential.
  • the metal powder, mist, or aerosol pollutants with strong conductivity in the gas are in contact with the intake front electrode. Or when the distance to the front electrode of the intake air reaches a certain range, it will be directly negatively charged. Then, all pollutants will enter the intake ionization and dust removal electric field with the airflow. The anode of the intake air removal electric field will give negatively charged metal dust, mist droplets, or air. The sol, etc.
  • the intake ionization and dust removal electric field formed between the anode and the cathode of the intake dust removal electric field obtains oxygen ions by ionizing the oxygen in the gas.
  • the anode of the electric field exerts an attractive force on the negatively charged dust and other pollutants, so that the dust and other pollutants move to the anode of the air intake dust removal electric field until this part
  • the pollutants are attached to the anode of the air intake dust removal electric field, so that some common dust and other pollutants are also collected, thereby collecting the pollutants with stronger conductivity and weaker conductivity in the gas, and making the air intake dust removal electric field
  • the anode can collect a wider range of pollutants in the gas, and the collection ability is stronger and the collection efficiency is higher.
  • the inlet of the intake electric field device communicates with the exhaust port of the separation mechanism.
  • the air intake electric field device may include an air intake dust removal electric field cathode and an air intake dust removal electric field anode, and an ionization dust removal electric field is formed between the air intake dust removal electric field cathode and the air intake dust removal electric field anode.
  • an ionization dust removal electric field is formed between the air intake dust removal electric field cathode and the air intake dust removal electric field anode.
  • the cathode of the air intake dust removal electric field 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 dust accumulation requirements. In an embodiment of the 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 anode of the intake dust removal electric field.
  • the cross section of the cathode wire is circular;
  • the cathode wire needs to be designed into a polyhedron shape. The length of the cathode wire is adjusted according to the anode of the intake dust removal electric field.
  • the cathode of the air intake dust removal electric field includes a plurality of cathode rods.
  • the diameter of the cathode rod is not greater than 3 mm.
  • a metal rod or an alloy rod that is easy to discharge is used as the cathode rod.
  • the shape of the cathode rod may be needle-shaped, polygonal, burr-shaped, threaded rod-shaped, columnar or the like. The shape of the cathode rod can be adjusted according to the shape of the anode of the intake air dedusting electric field.
  • the cross section of the cathode rod needs to be designed to be circular;
  • the dust surface is a circular arc surface, and the cathode rod needs to be designed into a polyhedron shape.
  • the cathode of the intake air dedusting electric field passes through the anode of the intake air dedusting electric field.
  • the anode of the air intake dust removal electric field includes one or more hollow anode tubes arranged in parallel. When there are a plurality of hollow anode tubes, all the hollow anode tubes constitute a honeycomb-shaped anode for the electric field of air intake dust removal.
  • the hollow anode tube may have a circular or polygonal cross section. If the cross section of the hollow anode tube is circular, a uniform electric field can be formed between the anode of the air intake dust removal electric field and the cathode of the air intake dust removal electric field, and the inner wall of the hollow anode tube is not easy to accumulate dust.
  • the cross section of the hollow anode tube is a triangular shape, three dust accumulation surfaces and three distant dust holding angles can be formed on the inner wall of the hollow anode tube.
  • This structure of the hollow anode tube has the highest dust holding rate. If the cross section of the hollow anode tube is quadrangular, 4 dust-collecting surfaces and 4 dust-holding angles can be obtained, but the grouping structure is unstable. If the cross section of the hollow anode tube is hexagonal, 6 dust accumulation surfaces and 6 dust accumulation angles can be formed, and the dust accumulation surface and the dust accumulation 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 diameter of the inscribed circle diameter of the hollow anode tube ranges from 5 mm to 400 mm.
  • the cathode of the intake air dust removal electric field is installed on a cathode support plate, and the cathode support plate and the anode of the intake air dust removal electric field are connected by an intake insulation mechanism.
  • the intake air insulation mechanism is used to achieve insulation between the cathode support plate and the anode of the intake dust removal electric field.
  • the anode of the intake dust removal electric field includes a first anode part and a second anode part, that is, the first anode part is close to the inlet of the intake electric field device, and the second anode part is close to the outlet of the intake electric field device.
  • the cathode support plate and the intake insulation mechanism are between the first anode part and the second anode part, that is, the intake insulation mechanism is installed in the middle of the ionization electric field or the cathode of the intake dust removal electric field, which can play a good role in the intake dust removal electric field cathode It supports the cathode of the intake air dedusting electric field relative to the anode of the intake air dedusting electric field anode, and maintains the set distance between the intake air dedusting electric field cathode and the intake air dedusting electric field anode.
  • 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 intake air insulation mechanism is provided outside the electric field flow path, that is, outside the second-stage flow path, to prevent or reduce the accumulation of dust in the gas on the intake air insulation mechanism, resulting in breakdown or conduction of the intake air insulation mechanism .
  • the intake air insulation mechanism uses a high-voltage resistant ceramic insulator to insulate the intake air dedusting electric field cathode and the intake air dedusting electric field anode.
  • the anode of the air intake dust removal electric field is also called a kind of shell.
  • the first anode portion is located before the cathode support plate and the intake insulation mechanism in the gas flow direction, and the first anode portion can remove water from the gas and prevent water from entering the intake insulation mechanism, causing intake air Insulation mechanism short circuit and fire.
  • the first positive stage can remove a considerable part of the dust in the gas. When the gas passes through the intake insulation mechanism, a considerable part of the dust has been eliminated, reducing the possibility of the dust causing the intake insulation mechanism to short circuit.
  • the air intake insulation mechanism includes an insulating ceramic post. The design of the first anode part is mainly to protect the insulating ceramic column from being polluted by particles in the gas.
  • the gas pollutes the insulating ceramic column it will cause the anode of the intake air dedusting electric field and the cathode of the intake air dedusting electric field to conduct, thus making the intake air dedusting
  • the dust accumulation function of the anode of the electric field fails, so the design of the first anode part can effectively reduce the pollution of the insulating ceramic column and improve the service time of the product.
  • the first anode part and the cathode of the intake dust removal electric field first contact with the polluting gas, and the intake insulation mechanism contacts the gas, so as to achieve the purpose of removing dust first and then passing through the intake insulation mechanism.
  • the length of the first anode portion is long enough to remove part of dust, reduce dust accumulated on the insulating mechanism and the cathode support plate, and reduce electrical breakdown caused by dust.
  • the length of the first anode portion accounts for 1/10 to 1/4, 1/4 to 1/3, 1/3 to 1/2, 1/2 to 2 of the total length of the anode of the intake dust removal electric field / 3, 2/3 to 3/4, or 3/4 to 9/10.
  • the second anode portion is located behind the cathode support plate and the intake insulation mechanism in the gas flow direction.
  • the second anode part includes a dust accumulation section and a reserved dust accumulation section.
  • the dust accumulation section utilizes static electricity to adsorb particulate matter in the gas.
  • the dust accumulation section is used to increase the dust accumulation area and prolong the service time of the intake electric field device.
  • the reserved dust accumulation section can provide failure protection for the dust accumulation section.
  • the dust accumulation section is reserved to further increase the dust accumulation area and improve the dust removal effect under the premise of meeting the design dust removal requirements.
  • the dust accumulation section is reserved for supplementing the dust accumulation in the previous section.
  • different power sources can be used for the first anode portion and the second anode portion.
  • the intake air insulation mechanism is provided at The second-stage flow channel between the cathode of the intake air dust removal electric field and the anode of the intake air dust removal electric field. Therefore, the intake insulation mechanism is suspended outside the anode of the intake dust removal electric field.
  • the air intake insulation mechanism may use non-conductor temperature-resistant materials, such as ceramics and glass.
  • completely sealed air-free material insulation requires an insulation thickness of> 0.3 mm / kv; air insulation requires> 1.4 mm / kv.
  • the insulation distance can be set according to 1.4 times the pole spacing between the cathode of the intake air dust removal electric field and the anode of the intake air dust removal electric field.
  • the air intake insulation mechanism uses ceramics and the surface is glazed; the connection cannot be filled with glue or organic materials, and the temperature resistance is greater than 350 degrees Celsius.
  • the intake insulation mechanism includes an insulation portion and a heat insulation portion.
  • the material of the insulation part adopts ceramic material or glass material.
  • the insulating portion may be an umbrella-shaped string ceramic column or a glass column, and the umbrella is glazed inside and outside.
  • the distance between the outer edge of the umbrella-shaped string ceramic column or glass column and the anode of the air intake dust removal electric field is greater than 1.4 times the electric field distance, that is, greater than 1.4 times the pole spacing.
  • the sum of the umbrella flange spacing of the umbrella-shaped string ceramic column or glass column is greater than 1.4 times the insulation spacing of the umbrella-shaped string ceramic column.
  • the total length of the inner depth of the umbrella-shaped string ceramic column or glass column is 1.4 times greater than the insulation distance of the umbrella-shaped string ceramic column.
  • the insulating part can also be a columnar string ceramic column or a glass column with glaze inside and outside. In an embodiment of the present invention, the insulating portion may also have a tower shape.
  • a heating rod is provided in the insulating portion.
  • 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 inside and outside of the insulating part and outside.
  • the outer surface of the insulation may spontaneously or be heated by gas to generate high temperature, which requires necessary isolation and protection to prevent burns.
  • the heat insulation part includes a protective baffle located outside the insulation part and a denitration purification reaction chamber.
  • the tail portion of the insulating portion needs to be insulated at the same location to prevent the environment and heat dissipation from heating the condensation component.
  • the lead-out line of the power supply of the intake electric field device uses an umbrella-shaped string of ceramic columns or glass columns to pass through the wall connection, an elastic contact is used in the wall to connect the cathode support plate, and a sealed insulating protective wiring cap is used for plugging out
  • the insulation distance between the lead-out conductor and the wall is greater than that of the umbrella-shaped string ceramic column or glass column.
  • the high-voltage part is eliminated from the lead, and directly installed on the end to ensure safety.
  • the overall outer insulation of the high-voltage module is protected by ip68, and the medium is used for heat dissipation.
  • an asymmetric structure is adopted between the cathode of the intake air dust removal electric field and the anode of the intake air dust removal electric field.
  • polar particles are subjected to a force of the same size but in opposite directions, and polar particles reciprocate in the electric field; in an asymmetric electric field, polar particles are subjected to two forces of different sizes, and polar particles act Moving in the direction of high force can avoid coupling.
  • the ionization dust removal electric field is formed between the cathode of the air intake dust removal electric field and the anode of the air intake dust removal electric field device of the invention.
  • the method of reducing the electric field coupling includes the following steps: selecting the ratio of the dust collecting area of the intake dust removal electric field anode to the discharge area of the intake dust removal electric field cathode to make Coupling times ⁇ 3.
  • the ratio of the dust collecting area of the intake air dedusting electric field anode to the discharge area of the intake air dedusting electric field cathode can be: 1.667: 1-1680: 1; 3.334: 1-113.34: 1; 6.67: 1- 56.67: 1; 13.34: 1-28.33: 1.
  • This embodiment selects a relatively large area of the intake area of the intake air dust removal electric field anode and a relatively small intake air discharge electric field cathode discharge area.
  • the above area ratio can reduce the discharge area of the intake air dust removal electric field cathode.
  • the dust collection area refers to the area of the anode working surface of the air intake dust removal electric field.
  • the dust collection area is the inner surface area of the hollow regular hexagonal tube, and the dust collection area is also This is called the dust accumulation area.
  • the discharge area refers to the area of the cathode working surface of the intake dust removal electric field. For example, if the cathode of the intake dust removal electric field is rod-shaped, the discharge area is the rod-shaped outer surface area.
  • the length of the anode of the air intake dust removal electric field may be 10 to 180 mm, 10 to 20 mm, 20 to 30 mm, 60 to 180 mm, 30 to 40 mm, 40 to 50 mm, 50 to 60 mm, 60 to 70 mm, 70 to 80mm, 80-90mm, 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 anode of the intake air dedusting electric field refers to the minimum length from one end to the other end of the working surface of the anode of the intake air dedusting electric field. Selecting this length for the anode of the electric field for air intake dust removal can effectively reduce the electric field coupling.
  • the length of the anode of the air intake dust removal electric field may be 10 to 90 mm, 15 to 20 mm, 20 to 25 mm, 25 to 30 mm, 30 to 35 mm, 35 to 40 mm, 40 to 45 mm, 45 to 50 mm, 50 to 55mm, 55-60mm, 60-65mm, 65-70mm, 70-75mm, 75-80mm, 80-85mm or 85-90mm, the design of this length can make the intake air dedusting anode and intake electric field device have high temperature resistance Characteristics, and makes the intake electric field device have high efficiency dust collection capacity under high temperature impact.
  • the length of the cathode of the air intake dust removal electric field may be 30 to 180 mm, 54 to 176 mm, 30 to 40 mm, 40 to 50 mm, 50 to 54 mm, 54 to 60 mm, 60 to 70 mm, 70 to 80 mm, 80 to 90mm, 90-100mm, 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 cathode of the air intake dust removal electric field refers to the minimum length from one end to the other end of the working surface of the dust removal electric field cathode. Choosing this length for the cathode of the air intake dust removal electric field can effectively reduce the electric field coupling.
  • the length of the cathode of the air intake dust removal electric field may be 10 to 90 mm, 15 to 20 mm, 20 to 25 mm, 25 to 30 mm, 30 to 35 mm, 35 to 40 mm, 40 to 45 mm, 45 to 50 mm, 50 to 55mm, 55-60mm, 60-65mm, 65-70mm, 70-75mm, 75-80mm, 80-85mm or 85-90mm, the design of this length can make the air intake dust removal electric field cathode and the air intake electric field device have high temperature resistance Characteristics, and makes the intake electric field device have high efficiency dust collection capacity under high temperature impact.
  • the distance between the anode of the intake air dust removal electric field and the cathode of the intake air dust removal electric field may be 5-30 mm, 2.5-139.9 mm, 9.9-139.9 mm, 2.5-9.9 mm, 9.9-20 mm, 20-30 mm , 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, 139.9 mm, or 2.5mm.
  • the distance between the anode of the intake air dedusting electric field and the cathode of the intake air dedusting electric field is also called the pole spacing.
  • the pole spacing specifically refers to the minimum vertical distance between the anode of the intake air dedusting electric field and the cathode of the intake air dedusting electric field. This choice of pole spacing can effectively reduce the electric field coupling and make the intake electric field device have high temperature resistance characteristics.
  • the diameter of the cathode of the dust-removing electric field is 1-3 mm, and the pole spacing between the anode of the dust-removing electric field and the cathode of the dust-removing electric field is 2.5-139.9 mm;
  • the discharge area ratio of the cathode of the dedusting electric field is 1.667: 1-1680: 1.
  • ionization dust removal can be applied to remove particulate matter in the gas.
  • the existing electric field dust removal device can only remove about 70% of the particulate matter, which cannot meet the needs of many industries.
  • the volume of the electric field dust removal device in the prior art is too large.
  • the inventor of the present invention has found that the disadvantages of the electric field dust removal device in the prior art are caused by electric field coupling.
  • the present invention can significantly reduce the size (ie, volume) of the electric field dust removal device by reducing the number of electric field couplings.
  • the size of the ionization and dust removal device provided by the present invention is about one fifth of the size of the existing ionization and dust removal device.
  • the current ionization dust removal device sets the gas flow rate to about 1 m / s, and the present invention can still obtain a higher gas flow rate when the gas flow rate is increased to 6 m / s. Particle removal rate.
  • the size of the electric field dust collector 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 present invention achieves the above unexpected results.
  • the ionization and dust removal electric field between the anode of the intake dust removal electric field and the cathode of the intake dust removal electric field is also called a first electric field.
  • a second electric field that is not parallel to the first electric field is formed between the anode of the intake air dust removal electric field and the cathode of the intake air dust removal electric field.
  • the second electric field is not perpendicular to the flow path of the ionization and dedusting electric field.
  • the second electric field is also called an auxiliary electric field and can be formed by one or two first auxiliary electrodes.
  • the first auxiliary electrode When the second electric field is formed by a first auxiliary electrode, the first auxiliary electrode can be placed at the inlet or outlet of the ionization dust removal electric field.
  • the first auxiliary electrode may have a negative potential or a positive potential.
  • the second electric field is formed by two first auxiliary electrodes, one of the first auxiliary electrodes can have a negative potential and the other first auxiliary electrode can have a positive potential; one first auxiliary electrode can be placed at the entrance of the ionization electric field, and the other A first auxiliary electrode is placed at the exit of the ionization electric field.
  • the first auxiliary electrode may be part of the cathode of the intake air dedusting electric field or the anode of the intake air dedusting electric field, that is, the first auxiliary electrode may be composed of an extension of the cathode of the intake air dedusting electric field or the anode of the intake air dedusting electric field.
  • the length of the cathode of the dust removal electric field and the anode of the intake dust removal electric field are different.
  • the first auxiliary electrode may also be a separate electrode, which means that the first auxiliary electrode may not be part of the cathode of the intake air dedusting electric field or the anode of the intake air dedusting electric field. In this case, the voltage of the second electric field and the voltage of the first electric field are not Similarly, it can be controlled individually according to the working conditions.
  • the second electric field can exert a force toward the outlet of the ionized electric field between the negatively charged oxygen ion flow between the anode of the intake air dedusting electric field and the cathode of the intake air dedusting electric field, so that the anode between the anode of the air dedusting electric field and the cathode of the air dedusting electric field
  • the flow of charged oxygen ions has a moving speed toward the outlet.
  • the negatively charged oxygen ions When the gas flows into the ionization electric field and flows toward the outlet of the ionization electric field, the negatively charged oxygen ions also move toward the anode of the intake dust removal electric field and toward the outlet of the ionization electric field, and the negatively charged oxygen ions are The anode of the gas dedusting electric field will be combined with the particulate matter in the gas during the movement to the outlet of the ionization electric field. Because the oxygen ions have a moving speed to the outlet, when the oxygen ions are combined with the particulate matter, the two will not be strong.
  • the intake electric field device's collection rate of particulate matter entering the electric field in the direction of ion flow is nearly double that of particulate matter entering the electric field in the direction of counter ion flow, thereby increasing the dust collection efficiency of the electric field and reducing the electric power consumption of the electric field.
  • the main reason for the low dust removal efficiency of the dust collection electric field in the prior art is that the direction of the dust entering the electric field is opposite to or perpendicular to the direction of the ion flow in the electric field, which causes the dust and ion flow to collide violently with each other and produce greater energy consumption. It also affects the charging efficiency, thereby reducing the electric field dust collection efficiency and increasing energy consumption in the prior art.
  • the air intake electric field device collects the 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 unipolar electric field dust collection efficiency will reach 99.99%.
  • the ion flow formed by the air intake electric field device is beneficial to fluid delivery of unpowered fans, air intake oxygenation, or heat exchange.
  • the air intake electric field device detects the electric field current and performs dust cleaning in any of the following ways:
  • the intake electric field device detects that the electric field current increases to a given value, the electric field reverse corona discharge phenomenon is used to increase the electric field voltage, limit the injection current, and complete the dust cleaning.
  • the electric field reverse corona discharge phenomenon is used to increase the electric field voltage and limit the injection current, so that the rapid discharge occurring at the position of the anode carbon deposit generates plasma
  • the plasma oxidizes the organic components of the dust deeply, breaks the polymer bonds, and forms small molecules of carbon dioxide and water to complete the dust cleaning.
  • the anode of the intake air dust removal electric field and the cathode of the intake air dust removal electric field are electrically connected to the two electrodes of the power supply, respectively.
  • the voltage loaded on the anode of the intake air dedusting electric field and the cathode of the intake air dedusting electric field needs to select an appropriate voltage level, and the specific voltage level to be selected depends on the volume, temperature resistance and dust holding rate of the air intake electric field device.
  • the voltage is from 1kv to 50kv; the temperature resistance conditions are first considered in the design, the parameters of the pole spacing and temperature: 1MM ⁇ 30 degrees, the dust accumulation area is greater than 0.1 square / thousand cubic meters / hour, and the electric field length is greater than 5 Times, control the electric field air flow velocity to be less than 9 meters per second.
  • the anode of the air intake dust removal electric field is composed of a first hollow anode tube and has a honeycomb shape.
  • the shape of the first hollow anode tube port may be circular or polygonal.
  • the value of the inscribed circle of the first hollow anode tube ranges from 5-400mm, the corresponding voltage is between 0.1-120kv, and the corresponding current of the first hollow anode tube is between 0.1-30A;
  • the tangent circle corresponds to different corona voltage, about 1KV / 1MM.
  • the intake electric field device includes a first electric field stage.
  • the first electric field stage includes a plurality of first electric field generating units, and there may be one or more first electric field generating units.
  • the first electric field generating unit is also called a first dust collecting unit.
  • the first dust collecting unit includes the anode of the intake air dust removal electric field and the cathode of the intake air dust removal electric field. There are one or more first dust collecting units.
  • the dust collection efficiency of the intake electric field device can be effectively improved.
  • the anodes of each intake dust removal electric field have the same polarity
  • the cathodes of each intake dust removal electric field have the same polarity.
  • the intake electric field device further includes a plurality of connecting housings, and the first electric field stages connected in series are connected through the connecting housings; the distance between the first electric field stages of two adjacent stages is greater than 1.4 times the pole spacing.
  • the electret material is charged with an electric field.
  • the electret material will be used to remove dust.
  • the intake electric field device includes an intake electret element.
  • the air intake electret element is provided in the anode of the air intake dust removal electric field.
  • the anode of the intake air dust removal electric field and the cathode of the intake air dust removal electric field form an intake air ionization dust removal electric field when the power is turned on, and the intake air electret element is at the intake air ionization dust removal electric field in.
  • the intake electret element is close to the outlet of the intake electric field device, or the intake electret element is provided at the outlet of the intake electric field device.
  • the anode of the intake air dust removal electric field and the cathode of the intake air dust removal electric field form an intake air flow channel, and the intake air electret element is provided in the intake air flow channel.
  • the intake runner includes an intake runner outlet, the intake electret element is close to the intake runner outlet, or the intake electret element is provided at the inlet Air outlet.
  • the cross section of the intake electret element in the intake flow channel occupies 5% to 100% of the cross section of the intake flow channel.
  • the cross section of the intake electret element in the intake flow passage accounts for 10% -90%, 20% -80%, or 40% -60% of the cross section of the intake flow passage.
  • the intake ionization and dedusting electric field charges the intake electret element.
  • the intake electret element has a porous structure.
  • the air intake electret element is a fabric.
  • the anode of the intake air dedusting electric field is tubular, the outside of the air intake electret element is tubular, and the outside of the air intake electret element is sleeved on the anode of the intake air dedusting electric field internal.
  • the intake electret element and the anode of the intake dust removal electric field are detachably connected.
  • the material of the intake electret element includes an inorganic compound having electret properties.
  • the electret performance refers to that the intake electret element is charged after being charged by an external power source, and still retains a certain charge when completely disconnected from the power source, thereby acting as an electrode as an electric field electrode.
  • the inorganic compound is selected from one or more combinations of oxygen-containing compounds, nitrogen-containing compounds, or glass fibers.
  • the oxygen-containing compound is selected from one or more combinations of metal-based oxides, oxygen-containing composites, and oxygen-containing inorganic heteropoly acid salts.
  • the metal-based oxide is selected from one or more combinations of aluminum oxide, zinc oxide, zirconium oxide, titanium oxide, barium oxide, tantalum oxide, silicon oxide, lead oxide, and tin oxide .
  • the metal-based oxide is alumina.
  • the oxygen-containing composite is selected from one or more combinations of titanium-zirconium composite oxide or titanium-barium composite oxide.
  • the oxygen-containing inorganic heteropoly acid salt is selected from one or more combinations of zirconium titanate, lead zirconate titanate, or barium titanate.
  • the nitrogen-containing compound is silicon nitride.
  • the material of the intake electret element includes an organic compound having electret properties.
  • the electret performance refers to that the intake electret element is charged after being charged by an external power source, and still retains a certain charge when completely disconnected from the power source, thereby acting as an electrode as an electric field electrode.
  • the organic compound is selected from one or more combinations of fluoropolymer, polycarbonate, PP, PE, PVC, natural wax, resin, and rosin.
  • the fluoropolymer is selected from polytetrafluoroethylene (PTFE), polyperfluoroethylene propylene (Teflon-FEP), soluble polytetrafluoroethylene (PFA), and polyvinylidene fluoride (PVDF) One or more combinations.
  • PTFE polytetrafluoroethylene
  • Teflon-FEP polyperfluoroethylene propylene
  • PFA soluble polytetrafluoroethylene
  • PVDF polyvinylidene fluoride
  • the fluoropolymer is polytetrafluoroethylene.
  • the air intake ionization and dust removal electric field is generated under the condition of power-on driving voltage.
  • the intake air ionization and dust removal electric field is used to ionize part of the to-be-processed objects and adsorb the particulate matter in the intake air, while charging the intake air electret element.
  • the charged intake electret element When there is no power-on driving voltage, the charged intake electret element generates an electric field, and the electric field generated by the charged intake electret element absorbs particulate matter in the intake, that is, the intake ionization dust removal electric field fails Particulate matter can still be adsorbed.
  • the engine intake dust removal system further includes an ozone removal device for removing or reducing ozone generated by the intake electric field device. Between the outlet of the dust removal system.
  • the ozone removing device includes an ozone digester.
  • the ozone digester is selected from at least one of an ultraviolet ozone digester and a catalytic ozone digester.
  • the engine air intake and dust removal system of the present invention also includes an ozone removal device for removing or reducing the ozone generated by the air intake electric field device.
  • Ozone in the air participates in ionization to form ozone, which affects the performance of subsequent devices. For example, if ozone enters the engine, The internal chemical composition of oxygen element increases, the molecular weight increases, from hydrocarbon compounds to non-hydrocarbon compounds, the appearance becomes darker, the precipitation increases, the corrosion increases, and the performance of the lubricating oil is reduced.
  • the gas dedusting system also includes an ozone removal device to avoid or reduce the decline in performance of subsequent devices, such as avoiding or reducing the decline in the performance of the lubricating oil in the engine.
  • the present invention provides an air intake dust removal method, including the following steps:
  • the dust removal process is performed.
  • the dust is cleaned in any of the following ways:
  • the dust is carbon black.
  • the cathode of the air intake dust removal electric field 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 dust accumulation requirements. In an embodiment of the 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 anode of the intake dust removal electric field.
  • the cross section of the cathode wire is circular;
  • the cathode wire needs to be designed into a polyhedron shape. The length of the cathode wire is adjusted according to the anode of the intake dust removal electric field.
  • the cathode of the air intake dust removal electric field includes a plurality of cathode rods.
  • the diameter of the cathode rod is not greater than 3 mm.
  • a metal rod or an alloy rod that is easy to discharge is used as the cathode rod.
  • the shape of the cathode rod may be needle-shaped, polygonal, burr-shaped, threaded rod-shaped, columnar or the like. The shape of the cathode rod can be adjusted according to the shape of the anode of the intake air dedusting electric field.
  • the cross section of the cathode rod needs to be designed to be circular;
  • the dust surface is a circular arc surface, and the cathode rod needs to be designed into a polyhedron shape.
  • the cathode of the intake air dedusting electric field passes through the anode of the intake air dedusting electric field.
  • the anode of the air intake dust removal electric field includes one or more hollow anode tubes arranged in parallel. When there are a plurality of hollow anode tubes, all the hollow anode tubes constitute a honeycomb-shaped anode for the electric field of air intake dust removal.
  • the hollow anode tube may have a circular or polygonal cross section. If the cross section of the hollow anode tube is circular, a uniform electric field can be formed between the anode of the air intake dust removal electric field and the cathode of the air intake dust removal electric field, and the inner wall of the hollow anode tube is not easy to accumulate dust.
  • the cross section of the hollow anode tube is a triangular shape, three dust accumulation surfaces and three distant dust holding angles can be formed on the inner wall of the hollow anode tube.
  • This structure of the hollow anode tube has the highest dust holding rate. If the cross section of the hollow anode tube is quadrangular, 4 dust-collecting surfaces and 4 dust-holding angles can be obtained, but the grouping structure is unstable. If the cross section of the hollow anode tube is hexagonal, 6 dust accumulation surfaces and 6 dust accumulation angles can be formed, and the dust accumulation surface and the dust accumulation 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 diameter of the inscribed circle diameter of the hollow anode tube ranges from 5 mm to 400 mm.
  • the present invention provides a method for accelerating intake air, including the following steps:
  • An electric field is generated in the flow channel, the electric field is not perpendicular to the flow channel, and the electric field includes an inlet and an outlet.
  • the electric field includes a first anode and a first cathode, the first anode and the first cathode form the flow channel, and the flow channel connects the inlet and the outlet.
  • the first anode and the first cathode ionize the gas in the flow channel.
  • the electric field includes a second electrode, and the second electrode is disposed at or near the inlet.
  • the second electrode is a cathode and serves as an extension of the first cathode.
  • the second electrode is provided independently of the first anode and the first cathode.
  • the electric field includes a third electrode, and the third electrode is disposed at or near the outlet.
  • the third electrode is an anode, and the third electrode is an extension of the first anode.
  • the third electrode is provided independently of the first anode and the first cathode.
  • the first 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 dust accumulation requirements. In an embodiment of the 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 first anode.
  • the cross section of the cathode wire is circular; if the dust collecting surface of the first anode is an arc surface, the cathode wire Need to be designed as a polyhedron. The length of the cathode wire is adjusted according to the first anode.
  • the first cathode includes a number of cathode rods.
  • the diameter of the cathode rod is not greater than 3 mm.
  • a metal rod or an alloy rod that is easy to discharge is used as the cathode rod.
  • the shape of the cathode rod may be needle-shaped, polygonal, burr-shaped, threaded rod-shaped, columnar or the like. The shape of the cathode rod can be adjusted according to the shape of the first anode.
  • the cross section of the cathode rod needs to be designed to be circular; if the dust collecting surface of the first anode is an arc surface , The cathode rod needs to be designed into a polyhedron shape.
  • the first cathode is disposed in the first anode.
  • the first anode includes one or more hollow anode tubes arranged in parallel. When there are multiple hollow anode tubes, all of the hollow anode tubes constitute a honeycomb first anode.
  • the hollow anode tube may have a circular or polygonal cross section. If the cross section of the hollow anode tube is circular, a uniform electric field can be formed between the first anode and the first cathode, and the inner wall of the hollow anode tube is not prone to dust accumulation. If the cross section of the hollow anode tube is a triangular shape, three dust accumulation surfaces and three distant dust holding angles can be formed on the inner wall of the hollow anode tube.
  • This structure of the hollow anode tube has the highest dust holding rate. If the cross section of the hollow anode tube is quadrangular, 4 dust-collecting surfaces and 4 dust-holding angles can be obtained, but the grouping structure is unstable. If the cross section of the hollow anode tube is hexagonal, 6 dust accumulation surfaces and 6 dust accumulation angles can be formed, and the dust accumulation surface and the dust accumulation 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. In an embodiment of the present invention, the diameter of the inscribed circle diameter of the hollow anode tube ranges from 5 mm to 400 mm.
  • the present invention provides a method for reducing electric field coupling of intake dust removal, including the following steps:
  • the anode of the intake dust removal electric field or / and the cathode of the intake dust removal electric field is selected.
  • the size of the anode of the intake dust removal electric field or / and the cathode of the intake dust removal electric field is selected such that the number of electric field couplings is ⁇ 3.
  • the ratio of the dust collecting area of the anode of the intake air dust removal electric field to the discharge area of the cathode of the intake air dust removal electric field is selected.
  • the ratio of the dust accumulation area of the anode of the intake air dust removal electric field to the discharge area of the cathode of the intake air dust removal electric field is 1.667: 1-1680: 1.
  • the ratio of the dust accumulation area of the intake dust removal electric field anode to the discharge area of the intake dust removal electric field cathode is selected to be 6.67: 1-56.67: 1.
  • the diameter of the cathode of the dust-removing electric field is 1-3 mm, and the pole spacing between the anode of the dust-removing electric field and the cathode of the dust-removing electric field is 2.5-139.9 mm;
  • the discharge area ratio of the cathode of the dedusting electric field is 1.667: 1-1680: 1.
  • the pole separation between the anode of the dust removal electric field and the cathode of the dust removal electric field is selected to be less than 150 mm.
  • the pole distance between the anode of the dust-removing electric field and the cathode of the dust-removing electric field is selected to be 2.5-139.9 mm. More preferably, the pole spacing between the anode of the dust-removing electric field and the cathode of the dust-removing electric field is selected to be 5.0-100 mm.
  • the length of the anode of the air intake dust removal electric field is selected to be 10-180 mm. More preferably, the length of the anode of the intake dust removal electric field is selected to be 60-180 mm.
  • the cathode length of the air intake dust removal electric field is selected to be 30-180 mm. More preferably, the cathode length of the intake dust removal electric field is selected to be 54-176 mm.
  • the cathode of the air intake dust removal electric field 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 dust accumulation requirements. In an embodiment of the 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 anode of the intake dust removal electric field.
  • the cross section of the cathode wire is circular;
  • the cathode wire needs to be designed into a polyhedron shape. The length of the cathode wire is adjusted according to the anode of the intake dust removal electric field.
  • the cathode of the air intake dust removal electric field includes a plurality of cathode rods.
  • the diameter of the cathode rod is not greater than 3 mm.
  • a metal rod or an alloy rod that is easy to discharge is used as the cathode rod.
  • the shape of the cathode rod may be needle-shaped, polygonal, burr-shaped, threaded rod-shaped, columnar or the like. The shape of the cathode rod can be adjusted according to the shape of the anode of the intake air dedusting electric field.
  • the cross section of the cathode rod needs to be designed to be circular;
  • the dust surface is a circular arc surface, and the cathode rod needs to be designed into a polyhedron shape.
  • the cathode of the intake air dedusting electric field passes through the anode of the intake air dedusting electric field.
  • the anode of the air intake dust removal electric field includes one or more hollow anode tubes arranged in parallel. When there are a plurality of hollow anode tubes, all the hollow anode tubes constitute a honeycomb-shaped anode for the electric field of air intake dust removal.
  • the hollow anode tube may have a circular or polygonal cross section. If the cross section of the hollow anode tube is circular, a uniform electric field can be formed between the anode of the air intake dust removal electric field and the cathode of the air intake dust removal electric field, and the inner wall of the hollow anode tube is not easy to accumulate dust.
  • the cross section of the hollow anode tube is a triangular shape, three dust accumulation surfaces and three distant dust holding angles can be formed on the inner wall of the hollow anode tube.
  • This structure of the hollow anode tube has the highest dust holding rate. If the cross section of the hollow anode tube is quadrangular, 4 dust-collecting surfaces and 4 dust-holding angles can be obtained, but the grouping structure is unstable. If the cross section of the hollow anode tube is hexagonal, 6 dust accumulation surfaces and 6 dust accumulation angles can be formed, and the dust accumulation surface and the dust accumulation 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 diameter of the inscribed circle diameter of the hollow anode tube ranges from 5 mm to 400 mm.
  • the present invention provides a method for removing dust from intake air, including the following steps:
  • the intake electret element is close to the outlet of the intake electric field device, or the intake electret element is provided at the outlet of the intake electric field device.
  • the anode of the intake air dust removal electric field and the cathode of the intake air dust removal electric field form an intake air flow channel, and the intake air electret element is provided in the intake air flow channel.
  • the intake runner includes an intake runner outlet, the intake electret element is close to the intake runner outlet, or the intake electret element is provided at the inlet Air outlet.
  • the charged intake electret element when the intake ionization and dust removal electric field has no electrified driving voltage, the charged intake electret element is used to adsorb particulate matter in the intake air.
  • the charged intake electret element adsorbs certain particulate matter in the intake, it is replaced with a new intake electret element.
  • the intake ionization and dedusting electric field is restarted to adsorb particulate matter in the intake and charge the new intake electret element.
  • the material of the intake electret element includes an inorganic compound having electret properties.
  • the electret performance refers to that the intake electret element is charged after being charged by an external power source, and still retains a certain charge when completely disconnected from the power source, thereby acting as an electrode as an electric field electrode.
  • the inorganic compound is selected from one or more combinations of oxygen-containing compounds, nitrogen-containing compounds, or glass fibers.
  • the oxygen-containing compound is selected from one or more combinations of metal-based oxides, oxygen-containing composites, and oxygen-containing inorganic heteropoly acid salts.
  • the metal-based oxide is selected from one or more combinations of aluminum oxide, zinc oxide, zirconium oxide, titanium oxide, barium oxide, tantalum oxide, silicon oxide, lead oxide, and tin oxide .
  • the metal-based oxide is alumina.
  • the oxygen-containing composite is selected from one or more combinations of titanium-zirconium composite oxide or titanium-barium composite oxide.
  • the oxygen-containing inorganic heteropoly acid salt is selected from one or more combinations of zirconium titanate, lead zirconate titanate, or barium titanate.
  • the nitrogen-containing compound is silicon nitride.
  • the material of the intake electret element includes an organic compound having electret properties.
  • the electret performance refers to that the intake electret element is charged after being charged by an external power source, and still retains a certain charge when completely disconnected from the power source, thereby acting as an electrode as an electric field electrode.
  • the organic compound is selected from one or more combinations of fluoropolymer, polycarbonate, PP, PE, PVC, natural wax, resin, and rosin.
  • the fluoropolymer is selected from polytetrafluoroethylene (PTFE), polyperfluoroethylene propylene (Teflon-FEP), soluble polytetrafluoroethylene (PFA), and polyvinylidene fluoride (PVDF) One or more combinations.
  • PTFE polytetrafluoroethylene
  • Teflon-FEP polyperfluoroethylene propylene
  • PFA soluble polytetrafluoroethylene
  • PVDF polyvinylidene fluoride
  • the fluoropolymer is polytetrafluoroethylene.
  • the present invention provides an intake air dust removal method including the following steps: the intake air is subjected to intake air ionization and dust removal to remove or reduce ozone generated by the intake air ionization and dust removal.
  • ozone generated by the ionization and dust removal of the intake air is subjected to ozone digestion.
  • the ozone digestion is selected from at least one of ultraviolet digestion and catalytic digestion.
  • FIG. 1 is a schematic structural diagram of an intake dust removal system in an embodiment.
  • the air intake dust removal system 101 includes an air intake dust removal system inlet 1011, a centrifugal separation mechanism 1012, a first water filtering mechanism 1013, an air intake electric field device 1014, an air intake insulating mechanism 1015, an air intake air distribution device, and a second water filtering mechanism 1017 and / or intake ozone unit 1018.
  • the first water filtering mechanism 1013 and / or the second water filtering mechanism 1017 are optional, that is, the intake air dust removal system provided by the present invention may include the first water filtering mechanism 1013 and / or the second water filtering mechanism 1017 , The first water filtering mechanism 1013 and / or the second water filtering mechanism 1017 may not be included.
  • the inlet 1011 of the intake dust removal system is provided on the intake wall of the centrifugal separation mechanism 1012 to receive the gas with particulate matter.
  • the centrifugal separation mechanism 1012 provided at the lower end of the intake dust removal system 101 uses a conical cylinder.
  • the connection between the conical cylinder and the intake electric field device 1014 is an exhaust port, and a first filter layer for filtering particulate matter is provided on the exhaust port.
  • the bottom of the conical cylinder is provided with a powder outlet for receiving particulate matter.
  • the gas containing particulate matter enters the centrifugal separation mechanism 1012 from the inlet 1011 of the intake dust removal system at a speed of 12-30 m / s, the gas will change from linear motion to circular motion.
  • the vast majority of the rotating airflow flows downward from the cylindrical body toward the cone along the wall of the vessel.
  • the particulate matter is thrown toward the inner wall of the separation mechanism under the action of centrifugal force.
  • the momentum of the downward axial velocity near the inner wall falls along the wall surface and is discharged from the powder outlet.
  • the externally swirling airflow continuously flows into the central part of the separation mechanism to form a centripetal radial airflow.
  • This part of the airflow constitutes an internal swirling flow that rotates upward.
  • the direction of rotation of the internal and external swirling flow is the same.
  • the first water filtering mechanism 1013 disposed in the centrifugal separation mechanism 1012 includes a first electrode disposed at the inlet 1011 of the intake dust removal system is a conductive mesh plate.
  • the conductive mesh plate is used to Electrons conduct water.
  • the second electrode for adsorbing charged water is the anode dust accumulation part of the intake electric field device 1014, that is, the dust removal electric field anode 10141.
  • FIG. 2 is a structural diagram of another embodiment of a first water filtering mechanism provided in the air intake device.
  • the first electrode 10131 of the first water filtering mechanism 1013 is disposed at the air inlet, and the first electrode 10131 is a conductive mesh plate with a negative potential.
  • the second electrode 10132 of the present embodiment is disposed in the air intake device in a net shape, and the second electrode 10132 has a positive potential.
  • the second electrode 10132 is also called a collector.
  • the second electrode 10132 is specifically planar and the first electrode 10131 is parallel to the second electrode 10132.
  • a mesh electric field is formed between the first electrode 10131 and the second electrode 10132.
  • the first electrode 10131 is a mesh structure made of metal wire, and the first electrode 10131 is composed of a wire mesh.
  • the area of the second electrode 10132 is larger than the area of the first electrode 10131.
  • the air intake electric field device 1014 includes an air intake dust electric field anode 10141 and an air intake dust electric field cathode 10142 disposed in the air intake dust electric field anode 10141.
  • the air intake dust electric field anode 10141 and the air intake dust electric field cathode 10142 form an asymmetric Electrostatic field, in which, after the gas containing particulate matter enters the intake electric field device 1014 through the exhaust port, the cathode 10142 of the intake dust removal electric field discharges, ionizing the gas, so that the particulate matter obtains a negative charge , Moving toward the anode 10141 of the intake dust removal electric field and deposited on the anode 10141 of the intake dust removal electric field.
  • the inside of the anode dust collecting electric field anode 10141 is composed of a hollow anode tube bundle in a honeycomb shape (as shown in FIG. 19), and the shape of the port of the anode tube bundle is hexagonal.
  • the cathode 10142 of the air intake dust removal electric field includes a plurality of electrode rods, each of which is inserted into each anode tube bundle in the anode tube bundle group in one-to-one correspondence, wherein the electrode rods are shaped like needles, polygons, and burrs , Threaded rod or column.
  • the outlet end of the cathode 10142 of the intake dust removal electric field is lower than the outlet end of the anode 10141 of the inlet dust removal electric field, and the outlet end of the cathode 10142 of the inlet dust removal electric field and the inlet dust removal electric field
  • the intake end of the anode 10141 is flush, so that an acceleration electric field is formed inside the intake electric field device 1014.
  • the intake insulation mechanism 1015 includes an insulation portion and a heat insulation portion.
  • the material of the insulating part is a ceramic material or a glass material.
  • the insulating part is an umbrella-shaped string ceramic column or glass column, or a column-shaped string ceramic column or glass column, and the inside and outside of the umbrella or the inside and outside of the column are glazed.
  • the cathode 10142 of the intake dust removal electric field is mounted on a cathode support plate 10143, and the cathode support plate 10143 and the anode 10141 of the intake dust removal electric field are connected by an intake insulation mechanism 1015.
  • the air intake insulation mechanism 1015 is used to achieve insulation between the cathode support plate 10143 and the anode 10141 of the air intake dust removal electric field.
  • the intake dust removal electric field anode 10141 includes a first anode portion 101412 and a second anode portion 101411, that is, the first anode portion 101412 is near the inlet of the intake electric field device, and the second anode portion 101411 is near the intake Electric field device outlet.
  • the cathode support plate and the intake insulation mechanism are between the first anode portion 101412 and the second anode portion 101411, that is, the intake insulation mechanism 1015 is installed in the middle of the intake ionization electric field or the intake dust removal electric field cathode 10142, which can
  • the dust removal electric field cathode 10142 plays a good supporting role and fixes the intake dust removal electric field cathode 10142 relative to the intake dust removal electric field anode 10141 to maintain the intake dust removal electric field cathode 10142 and the intake dust removal electric field anode 10141 The set distance.
  • FIG. 3A, FIG. 3B and FIG. 3C are structural diagrams of three implementations of the air intake equalizing device.
  • the air intake equalizing device can make the intake air amount of the engine changing at various rotation speeds evenly pass through the electric field generated by the anode of the intake dust removal electric field. At the same time, the internal temperature of the anode of the intake dust removal electric field can be kept constant, and the oxygen is sufficient.
  • the air intake equalizing device 1020 includes:
  • An air inlet pipe 10201 located on one side of the anode of the air inlet dust removal electric field
  • An air outlet pipe 10202 provided on the other side of the anode of the dust removal electric field; wherein the side where the air inlet pipe 10201 is installed is opposite to the other side where the air outlet pipe 10202 is installed.
  • the intake air equalization device 1026 may further include a first venturi plate air equalization mechanism 1028 provided at the intake end of the anode of the intake dust removal electric field and an anode provided at the anode of the intake dust removal electric field
  • the second venturi plate wind equalizing mechanism 1030 at the outlet end (as shown in the top view of the second venturi plate wind equalizing mechanism shown in FIG. 7D can be seen as a folded type), the first venturi plate wind equalizing mechanism is opened and Air holes, the second venturi plate air distribution mechanism is provided with air outlet holes, the air inlet holes and the air outlet holes are arranged in a staggered arrangement, and the front air intake side air is discharged to form a cyclone structure.
  • a second filter screen is provided at the junction of the intake electric field device 1014 and the second water filtering mechanism 1017 for filtering particles with a smaller particle size that have not been treated by the intake electric field device 1014 Fine particles.
  • the second water filtering mechanism 1017 disposed at the air outlet includes a third filter screen, a rotating shaft, and a water blocking ball.
  • the third filter screen is inclinedly installed at the air outlet through a rotating shaft, wherein a water blocking ball is installed at a position corresponding to the third air filter and the air outlet.
  • the to-be-entered gas pushes the third filter screen to rotate around a rotating shaft, a water film is formed on the third filter screen, and the water blocking ball blocks the air outlet end to prevent water from rushing out.
  • the air intake ozone mechanism 1018 provided at the air outlet of the air intake device uses an ozone removing lamp.
  • the air intake electric field device shown in FIG. 4 includes an air intake dedusting electric field anode 10141, an air intake dedusting electric field cathode 10142 and an air intake electret element 205, the air intake dedusting electric field anode 10141 and the air intake dedusting electric field cathode 10142 forms an electric field for intake ionization and dust removal when the power is turned on.
  • the intake electret element 205 is provided in the intake ionization and dust removal electric field.
  • the direction of the arrow in FIG. 4 is the flow direction of the object to be treated.
  • the air intake electret element is provided at the outlet of the air intake electric field device.
  • the intake ionization and dust removal electric field charges the intake electret element.
  • the air intake electret element has a porous structure, and the material of the air intake electret element is alumina.
  • the anode of the air intake dust removal electric field is tubular, the exterior of the air intake electret element is tubular, and the exterior of the air intake electret element is sleeved inside the anode of the air intake dust removal electric field.
  • the air intake electret element and the anode of the air intake dust removal electric field are detachably connected.
  • An air intake dust removal method includes the following steps:
  • the intake electret element is provided at the outlet of the intake electric field device; the material of the intake electret element is alumina; when the intake ionization and dedusting electric field has no electrified driving voltage, the charged intake air is used
  • the electret element absorbs particulate matter in the intake air; after the charged intake electret element absorbs certain particulate matter in the intake air, replace it with a new intake electret element; replace with a new intake air
  • the polar body component restarts the intake ionization and dust removal electric field to adsorb particulate matter in the intake air and charge the new intake electret component.
  • the air intake electric field device shown in FIGS. 5 and 6 includes an air intake dust removal electric field anode 10141, an air intake dust removal electric field cathode 10142 and an air intake electret element 205, the air intake dust removal electric field anode 10141 and the air intake
  • the dust-removing electric field cathode 10142 forms an intake flow channel 292, and the intake electret element 205 is provided in the intake flow channel 292.
  • the direction of the arrow in FIG. 5 is the flow direction of the object to be treated.
  • the intake runner 292 includes an intake runner outlet, and the intake electret element 205 is adjacent to the intake runner outlet.
  • the cross section of the intake electret element in the intake flow channel accounts for 10% of the cross section of the intake flow channel, as shown in FIG.
  • the cross-sectional area is the cross-sectional area of the intake electret element in the intake runner, and the sum of the first cross-sectional area of S1 and the second cross-sectional area of S2 is the cross-sectional area of the intake runner, and the first cross-sectional area of S1
  • the area does not include the cross-sectional area of the cathode 10142 of the intake dust removal electric field.
  • the anode of the intake air dust removal electric field and the cathode of the intake air dust removal electric field form an intake air ionization dust removal electric field when the power is turned on.
  • the intake ionization and dust removal electric field charges the intake electret element.
  • the air intake electret element has a porous structure, and the material of the air intake electret element is polytetrafluoroethylene.
  • the anode of the air intake dust removal electric field is tubular, the exterior of the air intake electret element is tubular, and the exterior of the air intake electret element is sleeved inside the anode of the air intake dust removal electric field.
  • the air intake electret element and the anode of the air intake dust removal electric field are detachably connected.
  • a method for removing dust from intake air includes the following steps:
  • the intake electret element is close to the outlet of the intake runner; the material of the intake electret element is polytetrafluoroethylene; when the intake ionization and dust removal electric field has no electrified driving voltage, the charged The intake electret element absorbs particulate matter in the intake air; after the charged intake electret element absorbs certain particulate matter in the intake air, replace it with a new intake electret element; replace with a new intake After the air electret element restarts the air intake ionization and dust removal electric field to adsorb particulate matter in the air intake and charge the new air intake electret element.
  • the engine intake air dust removal system includes an intake electric field device and an ozone removal device 206.
  • the intake electric field device includes an intake air removal electric field anode 10141 and an intake air removal electric field cathode 10142, the ozone removal The device is used to remove or reduce the ozone generated by the intake electric field device, and the ozone removing device is between the outlet of the intake electric field device and the outlet of the intake dust removal system.
  • the intake dust removal electric field anode 10141 and the intake dust removal electric field cathode 10142 are used to generate intake air ionization and dust removal electric field.
  • the ozone removing device 206 includes an ozone digester for digesting ozone generated by the intake electric field device.
  • the ozone digester is an ultraviolet ozone digester, and the arrow direction in the figure is the flow direction of the intake air.
  • An air inlet dust removal method includes the following steps: the air inlet is ionized and dedusted by the air inlet, and then the ozone generated by the air inlet ionized dust removal is ozone digested, and the ozone digestion is ultraviolet digestion.
  • the ozone removal device is used to remove or reduce the ozone generated by the air intake electric field device. Since the oxygen in the air participates in ionization to form ozone, which affects the performance of subsequent devices, such as if the ozone enters the engine, the internal chemical component oxygen element increases and the molecular weight Increased, from hydrocarbon compounds to non-hydrocarbon compounds, the appearance of darker color, increased precipitation, increased corrosion, reducing the performance of lubricating oil, therefore, the engine intake dust removal system of the present invention also includes an ozone removal device , To avoid or reduce the decline in performance of subsequent devices, such as avoiding or reducing the decline in the use of lubricating oil in the engine.
  • the electric field generating unit in this embodiment can be applied to an intake electric field device. As shown in FIG. 9, 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 The two electrodes of the power supply are electrically connected.
  • the power supply is a DC power supply.
  • the anode 4051 of the dust removal electric field and the cathode 4052 of the dust removal electric field are electrically connected to the anode and the cathode of the DC power supply, respectively.
  • the anode 4051 of the dust removal electric field has a positive potential
  • the cathode 4052 of the dust removal electric field has a negative potential.
  • the DC power supply may specifically be a DC high-voltage power supply.
  • a discharge electric field is formed between the above-mentioned dedusting electric field anode 4051 and the dedusting electric field cathode 4052, and the discharge electric field is an electrostatic field.
  • the anode 4051 of the dust removal electric field in this embodiment is a hollow regular hexagonal tube
  • the cathode 4052 of the dust removal electric field is rod-shaped
  • the cathode 4052 of the dust removal electric field is inserted into the anode 4051 of the dust removal electric field.
  • the method of reducing electric field coupling includes the following steps: the ratio of the dust collecting area of the dust collecting anode 4051 to the discharge area of the dust removing electric field cathode 4052 is 6.67: 1, and the pole spacing between the dust removing electric field anode 4051 and the dust removing electric field cathode 4052 is 9.9mm, The length of the dust-removing electric field anode 4051 is 60 mm, and the length of the dust-removing electric field cathode 4052 is 54 mm.
  • the dust-removing electric field anode 4051 includes a fluid channel.
  • the fluid channel includes an inlet end and an outlet end.
  • the dust-removing electric field cathode 4052 is placed in the fluid channel
  • the dedusting electric field cathode 4052 extends in the direction of the dust collector 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 close to the dedusting electric field cathode 4052
  • There is an angle ⁇ between the outlet ends, and ⁇ 118 °, and under the action of the dust-removing electric field anode 4051 and the dust-removing electric field cathode 4052, more substances to be treated can be collected, and the number of electric field couplings ⁇ 3 can be reduced Electric field coupling consumption of aerosol, water mist, oil mist, loose smooth particles can save electric energy of electric field by 30-50%.
  • the intake electric field device includes an electric field stage composed of a plurality of the above-mentioned electric field generating units, and there are a plurality of the electric field stages, so as to effectively improve the dust collection efficiency of the electric field device by using a plurality of dust collection units.
  • the anode of each dust removal electric field is the same polarity
  • the cathode of each dust removal electric field is the same polarity.
  • the electric field stages of the multiple electric field stages are connected in series, and the series electric field stages are connected by a connecting shell.
  • the distance between the adjacent two electric field stages is greater than 1.4 times the pole spacing.
  • the electric field levels are two levels, that is, a first-level electric field and a second-level electric field, and the first-level electric field and the second-level electric field are connected in series through a connection housing.
  • the substance to be treated may be particulate dust or other impurities to be treated, such as aerosol, water mist, oil mist, etc.
  • the electric field generating unit in this embodiment can be applied to an intake electric field device. As shown in FIG. 9, 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 The two electrodes of the power supply are electrically connected.
  • the power supply is a DC power supply.
  • the anode 4051 of the dust removal electric field and the cathode 4052 of the dust removal electric field are electrically connected to the anode and the cathode of the DC power supply, respectively.
  • the anode 4051 of the dust removal electric field has a positive potential
  • the cathode 4052 of the dust removal electric field has a negative potential.
  • the DC power supply may specifically be a DC high-voltage power supply.
  • a discharge electric field is formed between the above-mentioned dedusting electric field anode 4051 and the dedusting electric field cathode 4052, and the discharge electric field is an electrostatic field.
  • the anode 4051 of the dust removal electric field has a hollow regular hexagonal tube shape
  • the cathode 4052 of the dust removal electric field has a rod shape
  • the cathode 4052 of the dust removal electric field passes through the anode 4051 of the dust removal electric field.
  • the method for reducing electric field coupling includes the following steps: the ratio of the dust collecting area of the dust collecting field anode 4051 to the discharge area of the dust removing electric field cathode 4052 is 1680: 1, and the pole spacing between the dust removing electric field anode 4051 and the dust removing electric field cathode 4052 is 139.9mm, The length of the dust-removing electric field anode 4051 is 180 mm, and the length of the dust-removing electric field cathode 4052 is 180 mm.
  • the dust-removing electric field anode 4051 includes a fluid channel.
  • the fluid channel includes an inlet end and an outlet end.
  • the dust-removing electric field cathode 4052 is placed in the fluid channel
  • the dedusting electric field cathode 4052 extends in the direction of the dust collector 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 close to the dedusting electric field cathode 4052
  • the outlet end is flush, and under the action of the dedusting electric field anode 4051 and the dedusting electric field cathode 4052, more materials to be treated can be collected, and the number of electric field couplings is ⁇ 3, which can reduce the electric field to aerosol, water mist, oil mist 3. Coupling consumption of loose and smooth particles saves 20-40% of electric energy in the electric field.
  • the substance to be treated may be particulate dust or other impurities to be treated, such as aerosol, water mist, oil mist, etc.
  • the electric field generating unit in this embodiment can be applied to an intake electric field device. As shown in FIG. 9, 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 The two electrodes of the power supply are electrically connected.
  • the power supply is a DC power supply.
  • the anode 4051 of the dust removal electric field and the cathode 4052 of the dust removal electric field are electrically connected to the anode and the cathode of the DC power supply, respectively.
  • the anode 4051 of the dust removal electric field has a positive potential
  • the cathode 4052 of the dust removal electric field has a negative potential.
  • the DC power supply may specifically be a DC high-voltage power supply.
  • a discharge electric field is formed between the above-mentioned dedusting electric field anode 4051 and the dedusting electric field cathode 4052, and the discharge electric field is an electrostatic field.
  • the anode 4051 of the dust removal electric field has a hollow regular hexagonal tube shape
  • the cathode 4052 of the dust removal electric field has a rod shape
  • the cathode 4052 of the dust removal electric field passes through the anode 4051 of the dust removal electric field.
  • the method of reducing electric field coupling includes the following steps: the ratio of the dust collecting area of the dust collecting field anode 4051 to the discharge area of the dust removing electric field cathode 4052 is 1.667: 1, the pole spacing between the dust removing electric field anode 4051 and the dust removing electric field cathode 4052 is 2.4 mm,
  • the dust removal field anode 4051 has a length of 30 mm and the dust removal field cathode 4052 has a length of 30 mm.
  • the dust removal field anode 4051 includes a fluid channel including an inlet end and an outlet end.
  • the dust removal field cathode 4052 is placed in the fluid channel
  • the dedusting electric field cathode 4052 extends in the direction of the dust collector 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 close to the dedusting electric field cathode 4052
  • the outlet end is flush, and under the action of the dedusting electric field anode 4051 and the dedusting electric field cathode 4052, more materials to be treated can be collected, and the number of electric field couplings is ⁇ 3, which can reduce the electric field to aerosol, water mist, oil mist 1. Coupling consumption of loose and smooth particles, saving electric field electric energy by 10-30%.
  • the substance to be treated may be particulate dust or other impurities to be treated, such as aerosol, water mist, oil mist, etc.
  • the electric field generating unit in this embodiment can be applied to an intake electric field device. As shown in FIG. 9, 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 The two electrodes of the power supply are electrically connected.
  • the power supply is a DC power supply.
  • the anode 4051 of the dust removal electric field and the cathode 4052 of the dust removal electric field are electrically connected to the anode and the cathode of the DC power supply, respectively.
  • the anode 4051 of the dust removal electric field has a positive potential
  • the cathode 4052 of the dust removal electric field has a negative potential.
  • the DC power supply may specifically be a DC high-voltage power supply.
  • a discharge electric field is formed between the above-mentioned dedusting electric field anode 4051 and the dedusting electric field cathode 4052, and the discharge electric field is an electrostatic field.
  • the anode 4051 of the dust removal electric field in this embodiment is a hollow regular hexagonal tube
  • the cathode 4052 of the dust removal electric field is rod-shaped
  • the cathode 4052 of the dust removal electric field is installed in the anode 4051 of the dust removal electric field.
  • the ratio of the dust collecting area of the anode 4051 to the discharge area of the cathode 4052 of the dedusting electric field is 6.67: 1, the pole spacing between the anode 4051 of the dedusting electric field and the cathode 4052 of the dedusting electric field is 9.9 mm, the length of the anode 4051 of the dedusting electric field is 60 mm, and the cathode of the dedusting electric field The length of 4052 is 54mm.
  • the anode 4051 of the dedusting electric field includes a fluid channel.
  • the fluid channel includes an inlet end and an outlet end.
  • the cathode 4052 of the dedusting electric field is placed in the fluid channel.
  • the cathode 4052 of the dedusting electric field is along the dust collector.
  • the direction of the fluid channel extends.
  • 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.
  • There is an angle ⁇ between the outlet end of the anode 4051 of the dust removal electric field and the near outlet end of the cathode 4052 of the dust removal electric field. 118 °, and under the action of the anode 4051 of the dust removal electric field and the cathode 4052 of the dust removal electric field, more substances to be treated can be collected to ensure the development of the electric field Means higher dust collecting efficiency, a typical exhaust particles pm0.23 dust collecting efficiency of 99.99%.
  • the intake electric field device includes an electric field stage composed of a plurality of the above-mentioned electric field generating units, and there are a plurality of the electric field stages, so as to effectively improve the dust collection efficiency of the electric field device by using a plurality of dust collection units.
  • the anode of each dust removal electric field is the same polarity
  • the cathode of each dust removal electric field is the same polarity.
  • the electric field stages of the multiple electric field stages are connected in series, and the series electric field stages are connected by a connecting shell.
  • the distance between the adjacent two electric field stages is greater than 1.4 times the pole spacing.
  • the electric field levels are two levels, that is, a first-level electric field 4053 and a second-level electric field 4054.
  • the first-level electric field 4053 and the second-level electric field 4054 are connected in series through a connection housing 4055.
  • the substance to be treated may be particulate dust or other impurities to be treated, such as aerosol, water mist, oil mist, etc.
  • the electric field generating unit in this embodiment can be applied to an intake electric field device. As shown in FIG. 9, 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 The two electrodes of the power supply are electrically connected.
  • the power supply is a DC power supply.
  • the anode 4051 of the dust removal electric field and the cathode 4052 of the dust removal electric field are electrically connected to the anode and the cathode of the DC power supply, respectively.
  • the anode 4051 of the dust removal electric field has a positive potential
  • the cathode 4052 of the dust removal electric field has a negative potential.
  • the DC power supply may specifically be a DC high-voltage power supply.
  • a discharge electric field is formed between the above-mentioned dedusting electric field anode 4051 and the dedusting electric field cathode 4052, and the discharge electric field is an electrostatic field.
  • the dust-removing electric field anode 4051 is a hollow regular hexagonal tube, and the dust-removing electric field cathode 4052 is rod-shaped.
  • the dust-removing electric field cathode 4052 is interposed in the dust-removing electric field anode 4051.
  • the dust-collecting area of the dust-removing electric field anode 4051 and the dust-removing electric field cathode 4052 The discharge area ratio is 1680: 1, the pole spacing between the dedusting electric field anode 4051 and the dedusting electric field cathode 4052 is 139.9mm, the length of the dedusting electric field anode 4051 is 180mm, the length of the dedusting electric field cathode 4052 is 180mm, and the dedusting electric field anode 4051 includes A fluid channel including an inlet end and an outlet end, the dust-removing electric field cathode 4052 is placed in the fluid channel, the dust-removing electric field cathode 4052 extends in the direction of the dust collector fluid channel, and the inlet of the dust-removing electric field anode 4051 The end is flush with the near inlet end of the dedusting electric field cathode 4052, the exit end of the dedusting electric field anode 4051 is flush with the near exit end of the dedusting electric field cathode
  • the intake electric field device includes an electric field stage composed of a plurality of the above-mentioned electric field generating units, and there are a plurality of the electric field stages, so as to effectively improve the dust collection efficiency of the electric field device by using a plurality of dust collection units.
  • the anode of each dust removal electric field is the same polarity
  • the cathode of each dust removal electric field is the same polarity.
  • the substance to be treated may be particulate dust or other impurities to be treated, such as aerosol, water mist, oil mist, etc.
  • the electric field generating unit in this embodiment can be applied to an intake electric field device. As shown in FIG. 9, 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 The two electrodes of the power supply are electrically connected.
  • the power supply is a DC power supply.
  • the anode 4051 of the dust removal electric field and the cathode 4052 of the dust removal electric field are electrically connected to the anode and the cathode of the DC power supply, respectively.
  • the anode 4051 of the dust removal electric field has a positive potential
  • the cathode 4052 of the dust removal electric field has a negative potential.
  • the DC power supply may specifically be a DC high-voltage power supply.
  • a discharge electric field is formed between the above-mentioned dedusting electric field anode 4051 and the dedusting electric field cathode 4052, and the discharge electric field is an electrostatic field.
  • the dust-removing electric field anode 4051 is a hollow regular hexagonal tube, and the dust-removing electric field cathode 4052 is rod-shaped.
  • the dust-removing electric field cathode 4052 is interposed in the dust-removing electric field anode 4051.
  • the ratio of the discharge area is 1.667: 1, and the pole spacing between the dust-removing electric field anode 4051 and the dust-removing electric field cathode 4052 is 2.4 mm.
  • the dust removal field anode 4051 has a length of 30 mm and the dust removal field cathode 4052 has a length of 30 mm.
  • the dust removal field anode 4051 includes a fluid channel including an inlet end and an outlet end.
  • the dust removal field cathode 4052 is placed in the fluid channel
  • the dedusting electric field cathode 4052 extends in the direction of the dust collector 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 close to the dedusting electric field cathode 4052
  • the outlet end is flush, and under the action of the dust removal electric field anode 4051 and the dust removal electric field cathode 4052, more materials to be treated can be collected to ensure a higher dust collection efficiency of the electric field device, and typical tail gas particles pm0.23 dust collection The efficiency is 99.99%.
  • the dust-removing electric field anode 4051 and the dust-removing electric field cathode 4052 constitute a dust collecting unit, and there are a plurality of dust collecting units, so as to effectively improve the dust collecting efficiency of the electric field device by using a plurality of dust collecting units.
  • the substance to be treated may be particulate dust or other impurities to be treated, such as aerosol, water mist, oil mist, etc.
  • the engine air intake system in this embodiment includes the electric field device in Embodiment 8, Embodiment 9, or Embodiment 10 described above.
  • the gas to enter the engine needs to flow through the electric field device first, so that the electric field device can effectively remove the dust in the gas waiting for the treatment substances to be removed; then, the processed gas enters the engine again to ensure that the gas entering the engine is cleaner , Contains less impurities such as dust; thus ensuring the working efficiency of the engine is higher, and the engine exhaust gas contains less pollutants.
  • the engine air intake system is also called an air intake device.
  • the electric field generating unit in this embodiment can be applied to an intake electric field device. As shown in FIG. 9, 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 The two electrodes of the power supply are electrically connected.
  • the power supply is a DC power supply.
  • the anode 4051 of the dust removal electric field and the cathode 4052 of the dust removal electric field are electrically connected to the anode and the cathode of the DC power supply, respectively.
  • the anode 4051 of the dust removal electric field has a positive potential
  • the cathode 4052 of the dust removal electric field has a negative potential.
  • the DC power supply may specifically be a DC high-voltage power supply.
  • a discharge electric field is formed between the above-mentioned dedusting electric field anode 4051 and the dedusting electric field cathode 4052, and the discharge electric field is an electrostatic field.
  • the anode 4051 of the dust removal electric field has a hollow regular hexagonal tube shape
  • the cathode 4052 of the dust removal electric field has a rod shape.
  • the cathode 4052 of the dust removal electric field is installed in the anode 4051 of the dust removal electric field.
  • the anode 4051 of the dust removal electric field has a length of 5 cm, and the cathode 4052 of the dust removal electric field has 5cm, the dedusting electric field anode 4051 includes a fluid channel, the fluid channel includes an inlet end and an outlet end, the dedusting electric field cathode 4052 is placed in the fluid channel, the dedusting electric field cathode 4052 is along the dust collector fluid channel The direction extends, the inlet end of the dust removal electric field anode 4051 is flush with the near inlet end of the dust removal electric field cathode 4052, the outlet end of the dust removal electric field anode 4051 is flush with the near outlet end of the dust removal electric field cathode 4052, the dust removal electric field anode 4051 and the dust removal electric field
  • the pole spacing of the cathode 4052 is 9.9mm, and under the action of the dedusting electric field anode 4051 and the dedusting electric field cathode 4052, it makes it resistant to high temperature shock
  • the intake electric field device includes an electric field stage composed of a plurality of the above-mentioned electric field generating units, and there are a plurality of the electric field stages, so as to effectively improve the dust collection efficiency of the electric field device by using a plurality of dust collection units.
  • the anode of each dust removal electric field is the same polarity
  • the cathode of each dust removal electric field is the same polarity.
  • the substance to be treated may be particulate dust.
  • the electric field generating unit in this embodiment can be applied to an intake electric field device. As shown in FIG. 9, 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 The two electrodes of the power supply are electrically connected.
  • the power supply is a DC power supply.
  • the anode 4051 of the dust removal electric field and the cathode 4052 of the dust removal electric field are electrically connected to the anode and the cathode of the DC power supply, respectively.
  • the anode 4051 of the dust removal electric field has a positive potential
  • the cathode 4052 of the dust removal electric field has a negative potential.
  • the DC power supply may specifically be a DC high-voltage power supply.
  • a discharge electric field is formed between the above-mentioned dedusting electric field anode 4051 and the dedusting electric field cathode 4052, and the discharge electric field is an electrostatic field.
  • the anode 4051 of the dust removal electric field is a hollow regular hexagonal tube, and the cathode 4052 of the dust removal electric field is rod-shaped.
  • the cathode 4052 of the dust removal electric field is installed in the anode 4051 of the dust removal electric field.
  • the anode 4051 of the dust removal electric field has a length of 9 cm and the cathode 4052 of the dust removal electric field has a length of 9cm
  • the dust-removing electric field anode 4051 includes a fluid channel
  • the fluid channel includes an inlet end and an outlet end
  • the dust-removing electric field cathode 4052 is placed in the fluid channel
  • the dust-removing electric field cathode 4052 is located along the dust collector fluid channel
  • the direction extends, the inlet end of the dust removal electric field anode 4051 is flush with the near inlet end of the dust removal electric field cathode 4052, the outlet end of the dust removal electric field anode 4051 is flush with the near outlet end of the dust removal electric field cathode 4052, the dust removal electric field anode 4051 and the dust removal electric field
  • the pole spacing of the cathode 4052 is 139.9mm, and under the action of the dedusting electric field anode 4051 and the dedusting electric field catho
  • the intake electric field device includes an electric field stage composed of a plurality of the above-mentioned electric field generating units, and there are a plurality of the electric field stages, so as to effectively improve the dust collection efficiency of the electric field device by using a plurality of dust collection units.
  • the anode of each storage electric field is the same polarity
  • the cathode of each dust removal electric field is the same polarity.
  • the substance to be treated may be particulate dust.
  • the electric field generating unit in this embodiment can be applied to an intake electric field device. As shown in FIG. 9, 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 The two electrodes of the power supply are electrically connected.
  • the power supply is a DC power supply.
  • the anode 4051 of the dust removal electric field and the cathode 4052 of the dust removal electric field are electrically connected to the anode and the cathode of the DC power supply, respectively.
  • the anode 4051 of the dust removal electric field has a positive potential
  • the cathode 4052 of the dust removal electric field has a negative potential.
  • the DC power supply may specifically be a DC high-voltage power supply.
  • a discharge electric field is formed between the above-mentioned dedusting electric field anode 4051 and the dedusting electric field cathode 4052, and the discharge electric field is an electrostatic field.
  • the anode 4051 of the dust removal electric field has a hollow regular hexagonal tube shape
  • the cathode 4052 of the dust removal electric field has a rod shape.
  • the cathode 4052 of the dust removal electric field is installed in the anode 4051 of the dust removal electric field.
  • the anode 4051 of the dust removal electric field has a length of 1 cm, and the cathode 4052 of the dust removal electric field has 1cm, the dedusting electric field anode 4051 includes a fluid channel, the fluid channel includes an inlet end and an outlet end, the dedusting electric field cathode 4052 is placed in the fluid channel, the dedusting electric field cathode 4052 is along the dust collector fluid channel The direction extends, the inlet end of the dust removal electric field anode 4051 is flush with the near inlet end of the dust removal electric field cathode 4052, the outlet end of the dust removal electric field anode 4051 is flush with the near outlet end of the dust removal electric field cathode 4052, the dust removal electric field anode 4051 and the dust removal electric field
  • the pole spacing of the cathode 4052 is 2.4mm, 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 makes it resistant to high
  • the intake electric field device includes an electric field stage composed of a plurality of the above-mentioned electric field generating units, and there are a plurality of the electric field stages, so as to effectively improve the dust collection efficiency of the electric field device by using a plurality of dust collection units.
  • the anode of each dust removal electric field is the same polarity
  • the cathode of each dust removal electric field is the same polarity.
  • the electric field stages of the multiple electric field stages are connected in series, and the series electric field stages are connected by a connecting shell.
  • the distance between the adjacent two electric field stages is greater than 1.4 times the pole spacing.
  • the electric field levels are two levels, namely, the first level electric field and the second level electric field, and the first level electric field and the second level electric field are connected in series through a connection housing.
  • the substance to be treated may be particulate dust.
  • the electric field generating unit in this embodiment can be applied to an intake electric field device. As shown in FIG. 9, 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 The two electrodes of the power supply are electrically connected.
  • the power supply is a DC power supply.
  • the anode 4051 of the dust removal electric field and the cathode 4052 of the dust removal electric field are electrically connected to the anode and the cathode of the DC power supply, respectively.
  • the anode 4051 of the dust removal electric field has a positive potential
  • the cathode 4052 of the dust removal electric field has a negative potential.
  • the DC power supply may specifically be a DC high-voltage power supply.
  • a discharge electric field is formed between the above-mentioned dedusting electric field anode 4051 and the dedusting electric field cathode 4052, and the discharge electric field is an electrostatic field.
  • the anode 4051 of the dust removal electric field in this embodiment is a hollow regular hexagonal tube
  • the cathode 4052 of the dust removal electric field is rod-shaped
  • the cathode 4052 of the dust removal electric field is interposed in the anode 4051 of the dust removal electric field. It is 3cm
  • the length of the dust removal electric field cathode 4052 is 2cm
  • 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 The cathode 4052 extends in the direction of the dust collector fluid channel.
  • the inlet end of the dust removal electric field anode 4051 is flush with the near inlet end of the dust removal electric field cathode 4052.
  • the dust collection efficiency corresponding to an electric field temperature of 200 ° C is 99.9%; the dust collection efficiency corresponding to an electric field temperature of 400 ° C is 90%; the dust collection efficiency corresponding to an electric field temperature of 500 ° C is 50%.
  • the intake electric field device includes an electric field stage composed of a plurality of the above-mentioned electric field generating units, and there are a plurality of the electric field stages, so as to effectively improve the dust collection efficiency of the electric field device by using a plurality of dust collection units.
  • each dust collector has the same polarity and each discharge has the same polarity.
  • the electric field stages of the multiple electric field stages are connected in series, and the series electric field stages are connected by a connecting shell.
  • the distance between the adjacent two electric field stages is greater than 1.4 times the pole spacing.
  • the electric field levels are two levels, that is, a first-level electric field and a second-level electric field, and the first-level electric field and the second-level electric field are connected in series through a connection housing.
  • the substance to be treated may be particulate dust.
  • the engine air intake system in this embodiment includes the electric field device in Embodiment 12, Embodiment 13, Embodiment 14, or Embodiment 15 described above.
  • the gas to enter the engine needs to flow through the electric field device first, so that the electric field device can effectively remove the dust in the gas waiting for the treatment substances to be removed; then, the processed gas enters the engine again to ensure that the gas entering the engine is cleaner , Contains less impurities such as dust; thus ensuring the working efficiency of the engine is higher, and the engine exhaust gas contains less pollutants.
  • the engine air intake system is also called an air intake device.
  • the electric field device in this embodiment can be applied to an air intake system, including a dust removal electric field cathode 5081 and a dust removal 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 cathode 5081 of the dust removal electric field has a negative potential
  • the anode 5082 and the auxiliary electrode 5083 of the dust removal electric field have positive potentials.
  • the auxiliary electrode 5083 is fixed to the anode 5082 of the dust removal electric field. After the anode 5082 of the dust removal electric field 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 anode of the dust removal electric field 5082 have the same positive potential.
  • the auxiliary electrode 5083 may extend in the front-rear direction, that is, the length direction of the auxiliary electrode 5083 may be the same as the length direction of the anode 5082 of the dust removal electric field.
  • the anode 5082 of the dust removal electric field has a tubular shape
  • the cathode 5081 of the dust removal electric field has a rod shape
  • the cathode 5081 of the dust removal electric field passes through the anode 5082 of the dust removal electric field.
  • the auxiliary electrode 5083 is also in the shape of a tube, and the auxiliary electrode 5083 and the anode 5082 of the dust removal electric field form an anode tube 5084.
  • the front end of the anode tube 5084 is flush with the cathode 5081 of the dedusting electric field, and the rear end of the anode tube 5084 exceeds the rear end of the cathode 5081 of the dedusting electric field.
  • the electrode 5083 that is, in this embodiment, the lengths of the dust-removing electric field anode 5082 and the dust-removing electric field cathode 5081 are the same, and the dust-removing electric field anode 5082 and the dust-removing electric field cathode 5081 are opposed to each other in the front-back direction; the auxiliary electrode 5083 is located behind the dust-removing electric field anode 5082 and the dust-removing electric field cathode 5081.
  • an auxiliary electric field is formed between the auxiliary electrode 5083 and the dedusting electric field cathode 5081.
  • the auxiliary electric field exerts a backward force on the negatively charged oxygen ion flow between the dedusting electric field anode 5082 and the dedusting electric field cathode 5081, so that the dedusting electric field anode 5082 and The flow of negatively charged oxygen ions between the cathode 5081 of the dust removal electric field has a backward moving speed.
  • the negatively charged oxygen ions will be combined with the material to be treated in the process of moving towards the anode 5082 of the dust removal electric field and backward, because the oxygen ions have a backward movement Speed, when oxygen ions are combined with the material to be processed, there will be no strong collision between the two, thereby avoiding greater energy consumption due to the stronger collision, making oxygen ions easily combined with the material to be processed, and
  • the charge efficiency of the material to be processed in the gas is higher, and then under the action of the anode 5082 and anode tube 5084 of the dust removal electric field, more material to be processed can be collected to ensure higher dust removal efficiency of the electric field device.
  • the dedusting electric field anode 5082, the auxiliary electrode 5083, and the dedusting electric field cathode 5081 constitute a dedusting unit, and there are a plurality of dedusting units to effectively improve the dedusting efficiency of the electric field device by using multiple dedusting units.
  • the substance to be treated may be particulate dust or other impurities to be treated.
  • the above gas may be the gas to be entered into the engine, or the gas discharged from the engine.
  • the DC power supply may specifically be a DC high-voltage power supply.
  • a discharge electric field is formed between the above-mentioned dedusting electric field cathode 5081 and the dedusting electric field anode 5082.
  • the discharge electric field is an electrostatic field.
  • the ion flow in the electric field between the dedusting electric field cathode 5081 and the dedusting electric field anode 5082 is perpendicular to the electrode direction, and flows back and forth between the two electrodes, causing ions to flow back and forth between the electrodes.
  • the auxiliary electrode 5083 is used to shift the relative positions of the electrodes to form a relative imbalance between the dedusting electric field anode 5082 and the dedusting electric field cathode 5081. This imbalance causes the ion flow in the electric field to be deflected.
  • the electric field device uses the auxiliary electrode 5083 to form an electric field that can direct ion current.
  • the above-mentioned electric field device is also referred to as an acceleration direction electric field device.
  • the collection rate of the particulate matter entering the electric field in the direction of ion current in the electric field device is nearly double that of the particulate matter entering the electric field in the direction of reverse ion current, thereby improving the dust collection efficiency of the electric field and reducing the electric power consumption of the electric field.
  • the main reason for the low dust removal efficiency of the dust collection electric field in the prior art is that the direction of the dust entering the electric field is opposite to or perpendicular to the direction of the ion flow in the electric field, which causes the dust and ion flow to collide violently with each other and produce greater energy consumption. It also affects the charging efficiency, thereby reducing the electric field dust collection efficiency and increasing energy consumption in the prior art.
  • the electric field device when the electric field device is used to collect the dust in the gas, the gas and dust enter the electric field in the ion flow direction, the dust is fully charged, and the electric field consumption is small; the unipolar electric field dust collection efficiency will reach 99.99%.
  • the gas and dust enter the electric field in the direction of ion flow the dust is not fully charged, the electric power consumption of the electric field will also 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 fluid transmission, oxygenation, heat exchange, etc. of the unpowered fan.
  • the electric field device in this embodiment can be applied to an air intake system, including a dust removal electric field cathode 5081 and a dust removal electric field anode 5082, which are electrically connected to the cathode and anode of the DC power source, respectively, and the auxiliary electrode 5083 is electrically connected to the cathode of the DC power source.
  • both the auxiliary electrode 5083 and the dust removal electric field cathode 5081 have a negative potential
  • the dust removal electric field anode 5082 has a positive potential.
  • the auxiliary electrode 5083 can be fixedly connected to the cathode 5081 of the dust removal electric field. In this way, after the cathode 5081 of the dust removal electric field is electrically connected to the cathode of the DC power supply, the auxiliary electrode 5083 is also electrically connected to the cathode of the DC power supply. Meanwhile, in this embodiment, the auxiliary electrode 5083 extends in the front-rear direction.
  • the anode 5082 of the dust removal electric field has a tubular shape
  • the cathode 5081 of the dust removal electric field has a rod shape
  • the cathode 5081 of the dust removal electric field passes through the anode 5082 of the dust removal electric field.
  • the auxiliary electrode 5083 in this embodiment is also rod-shaped, and the auxiliary electrode 5083 and the dust-removing electric field cathode 5081 constitute a cathode rod.
  • the front end of the cathode rod extends forward beyond the front end of the anode 5082 of the dust removal electric field, and the portion of the cathode rod that extends forward compared to the anode 5082 of the dust removal electric field is the auxiliary electrode 5083.
  • the lengths of the dust-removing electric field anode 5082 and the dust-removing electric field cathode 5081 are the same, and the dust-removing electric field anode 5082 and the dust-removing electric field cathode 5081 are opposed to each other in the front-back direction; the auxiliary electrode 5083 is located in front of the dust-removing electric field anode 5082 and the dust-removing electric field cathode 5081. In this way, an auxiliary electric field is formed between the auxiliary electrode 5083 and the dedusting electric field anode 5082.
  • the auxiliary electric field exerts a backward force on the negatively charged oxygen ion flow between the dedusting electric field anode 5082 and the dedusting electric field cathode 5081, so that the dedusting electric field anode 5082 and
  • the flow of negatively charged oxygen ions between the cathode 5081 of the dust removal electric field has a backward moving speed.
  • the dedusting electric field anode 5082, the auxiliary electrode 5083, and the dedusting electric field cathode 5081 constitute a dedusting unit, and there are a plurality of dedusting units to effectively improve the dedusting efficiency of the electric field device by using multiple dedusting units.
  • the substance to be treated may be particulate dust or other impurities to be treated.
  • the electric field device in this embodiment can be applied to an air intake system, and the auxiliary electrode 5083 extends in the left-right direction.
  • the longitudinal direction of the auxiliary electrode 5083 is different from the longitudinal direction of the dedusting electric field anode 5082 and the dedusting electric field cathode 5081.
  • the auxiliary electrode 5083 may be perpendicular to the anode 5082 of the dust removal electric field.
  • the dedusting electric field cathode 5081 and the dedusting 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 cathode 5081 of the dust removal electric field has a negative potential
  • the anode 5082 and the auxiliary electrode 5083 of the dust removal electric field have positive potentials.
  • the dust removal electric field cathode 5081 and the dust removal electric field anode 5082 are opposed to each other in the front-rear direction, and the auxiliary electrode 5083 is located behind the dust removal electric field anode 5082 and the dust removal electric field cathode 5081. In this way, an auxiliary electric field is formed between the auxiliary electrode 5083 and the dedusting electric field cathode 5081.
  • the auxiliary electric field exerts a backward force on the negatively charged oxygen ion flow between the dedusting electric field anode 5082 and the dedusting electric field cathode 5081, so that the dedusting electric field anode 5082 and The flow of negatively charged oxygen ions between the cathode 5081 of the dust removal electric field has a backward moving speed.
  • the negatively charged oxygen ions will be in phase with the substance to be processed in the process of moving toward the anode 5082 of the dedusting electric field and backward Combination, because the oxygen ions have a backward moving speed, when the oxygen ions are combined with the material to be processed, there will not be a strong collision between the two, thereby avoiding greater energy consumption due to the stronger collision, making the oxygen
  • the ions are easy to combine with the material to be processed, and make the charge efficiency of the material to be processed in the gas higher, and then under the action of the anode 5082 of the dust removal electric field, more material to be processed can be collected to ensure the dust removal of the electric field device higher efficiency.
  • the electric field device in this embodiment can be applied to an air intake system, and the auxiliary electrode 5083 extends in the left-right direction.
  • the longitudinal direction of the auxiliary electrode 5083 is different from the longitudinal direction of the dedusting electric field anode 5082 and the dedusting electric field cathode 5081.
  • the auxiliary electrode 5083 may be perpendicular to the cathode 5081 of the dust removal electric field.
  • the dedusting electric field cathode 5081 and the dedusting 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 cathode 5081 of the dust removal electric field and the auxiliary electrode 5083 have a negative potential
  • the anode 5082 of the dust removal electric field has a positive potential.
  • the dust-removing electric field cathode 5081 and the dust-removing electric field anode 5082 are opposed in the front-rear direction, and the auxiliary electrode 5083 is located in front of the dust-removing electric field anode 5082 and the dust-removing electric field cathode 5081. In this way, an auxiliary electric field is formed between the auxiliary electrode 5083 and the dedusting electric field anode 5082.
  • the auxiliary electric field exerts a backward force on the negatively charged oxygen ion flow between the dedusting electric field anode 5082 and the dedusting electric field cathode 5081, so that the dedusting electric field anode 5082 and The flow of negatively charged oxygen ions between the cathode 5081 of the dust removal electric field has a backward moving speed.
  • the negatively charged oxygen ions will be in phase with the substance to be processed in the process of moving toward the anode 5082 of the dedusting electric field and backward Combination, because the oxygen ions have a backward moving speed, when the oxygen ions are combined with the material to be processed, there will not be a strong collision between the two, thereby avoiding greater energy consumption due to the stronger collision, making the oxygen
  • the ions are easy to combine with the material to be processed, and make the charge efficiency of the material to be processed in the gas higher, and then under the action of the anode 5082 of the dust removal electric field, more material to be processed can be collected to ensure the dust removal of the electric field device higher efficiency.
  • the engine air intake device in this embodiment includes the electric field device in the foregoing embodiments 17, 18, 19, or 20.
  • the gas to enter the engine needs to flow through the electric field device first, so that the electric field device can effectively remove the dust in the gas waiting for the treatment substances to be removed; then, the processed gas enters the engine again to ensure that the gas entering the engine is cleaner , Contains less impurities such as dust; thus ensuring the working efficiency of the engine is higher, and the engine exhaust gas contains less pollutants.
  • the engine air intake device is also referred to as the air intake device
  • the electric field device is also referred to as the intake electric field device
  • the dust removal electric field cathode 5081 is also referred to as the intake air dust removal electric field cathode
  • the dust removal electric field anode 5082 is also referred to as the intake air dust removal electric field anode.
  • this embodiment provides an intake electric field device, including an intake electric field device inlet 3085, an intake runner 3086, an electric field runner 3087, an electric field runner 3088, and an intake runner 3086 that are sequentially connected
  • the intake pre-electrode 3083 is installed in it, and the ratio of the cross-sectional area of the intake pre-electrode 3083 to the cross-sectional area of the intake runner 3086 is 99% -10%.
  • the intake electric field device also includes an intake dedusting electric field cathode 3081 and intake The anode 3082 of the dust removal electric field and the electric field flow channel 3087 are located between the cathode 3081 of the intake dust removal electric field and the anode 3082 of the intake dust removal electric field.
  • the working principle of the intake electric field device of the present invention is that: the gas containing pollutants enters the intake runner 3086 through the inlet 3085 of the intake electric field device, and the intake front electrode 3083 installed in the intake runner 3086 conducts electrons to some pollutants Part of the pollutants are charged.
  • the intake dust removal electric field anode 3082 exerts an attractive force on the charged pollutants, and the charged pollutants move toward the intake dust removal electric field anode 3082.
  • the intake ionization dedusting electric field is formed between the intake air dedusting electric field cathode 3081 and the intake air dedusting electric field anode 3082 in the electric field flow channel 3087.
  • the device enables the pollutant to be more efficiently charged and more fully charged, thereby ensuring that the anode 3082 of the intake dust removal electric field can collect more pollution And ensure that the intake electric field device of the present invention has a higher collection efficiency for pollutants.
  • the cross-sectional area of the intake front electrode 3083 refers to the sum of the areas of the intake front electrode 3083 along the solid part of the cross section.
  • the ratio of the cross-sectional area of the intake front electrode 3083 to the cross-sectional area of the intake runner 3086 may be 99% to 10%, or 90 to 10%, or 80 to 20%, or 70 to 30%, or 60 to 40 %, Or 50%.
  • the intake front electrode 3083 and the intake dust removal electric field cathode 3081 are both electrically connected to the cathode of the DC power supply, and the intake dust removal electric field anode 3082 is electrically connected to the anode of the DC power supply.
  • the intake front electrode 3083 and the intake dust electric field cathode 3081 both have a negative potential, and the intake dust electric field anode 3082 has a positive potential.
  • the intake front electrode 3083 in this embodiment may be specifically mesh-shaped.
  • the intake pre-electrode 3083 is used in a mesh structure, which facilitates the flow of gas and pollutants through the intake pre-electrode 3083, and makes the pollutants in the gas and the intake pre-charge
  • the contact of the electrode 3083 is more sufficient, so that the intake front electrode 3083 can conduct electrons to more pollutants and make the charging efficiency of the pollutants higher.
  • the anode 3082 of the intake air dedusting electric field has a tubular shape
  • the cathode 3081 of the intake air dedusting electric field has a rod shape
  • the cathode 3081 of the intake air dedusting electric field passes through the anode 3082 of the air dedusting electric field.
  • the anode 3082 of the intake air electric field and the cathode 3081 of the intake air electric field have an asymmetric structure.
  • the ionizing electric field will charge the pollutants, and under the attraction force exerted by the intake air dedusting electric field anode 3082, the charged pollutants will be collected in On the inner wall of the anode 3082 of the air intake dust removal electric field.
  • the anode 3082 of the intake air electric field and the cathode 3081 of the intake air electric field both extend in the front-rear direction, and the front end of the anode 3082 of the air intake electric field 30 is located in the cathode 3081 of the air electric field in the front-rear direction. In front of the front end. As shown in FIG. 16, the rear end of the intake air electric field anode 3082 is located behind the rear end of the intake air electric field cathode 3081 in the front-rear direction.
  • the length of the anode 3082 of the intake air electric field in the front-rear direction is longer, so that the area of the adsorption surface on the inner wall of the anode 3082 of the intake air electric field is larger, so that it is more attractive to pollutants with negative potential And can collect more pollutants.
  • the cathode 3081 and the anode 3082 of the intake electric field constitute an ionization unit.
  • the gas field device has a stronger ability to collect pollutants and a higher collection efficiency.
  • the above-mentioned pollutants include ordinary dust with weak conductivity, metal dust with strong conductivity, mist droplets, aerosol, and the like.
  • the intake electric field device collects ordinary dust with weak conductivity and pollutants with high conductivity as follows: when the gas flows into the intake runner 3086 through the inlet 3085 of the intake electric field device, the gas Contaminants such as metal dust, mist droplets, or aerosols with high conductivity are directly negatively charged when they come into contact with the intake front electrode 3083, or when the distance to the intake front electrode 3083 reaches a certain range, and then , All the pollutants enter the electric field flow channel 3087 with the airflow, and the intake air dedusting electric field anode 3082 exerts an attractive force on the negatively charged metal dust, mist droplets, or aerosols, and collects this part of the pollutants.
  • the anode 3082 of the dust-removing electric field and the cathode 3081 of the intake dust-removing electric field form an ionizing electric field.
  • the ionizing electric field obtains oxygen ions by ionizing the oxygen in the gas, and the negatively charged oxygen ions combine with the ordinary dust to make the ordinary dust negatively charged.
  • the anode 3082 of the gas dedusting electric field exerts an attractive force on this part of the negatively charged dust and collects this part of the pollutants, thereby making the gas more conductive and conductive
  • the weaker pollutants are all collected, and the intake electric field device can collect a wider variety of substances and have a stronger collection capacity.
  • the above-mentioned intake dust electric field cathode 3081 is also referred to as a corona charging electrode.
  • the above DC power supply is specifically a DC high voltage power supply.
  • a direct current high voltage is passed between the intake front electrode 3083 and the intake dust removal electric field anode 3082 to form a conductive loop; an intake dust removal electric field cathode 3081 and an intake dust removal electric field anode 3082 are passed a direct current high voltage to form an ionization discharge corona electric field .
  • the intake front electrode 3083 is a densely distributed conductor.
  • the air intake front electrode 3083 When the easily charged dust passes through the air intake front electrode 3083, the air intake front electrode 3083 directly supplies electrons to the dust, and the dust is charged, and then is absorbed by the heteropolar anode air dedusting electric field anode 3082; at the same time, the uncharged dust passes through the air intake
  • the ionization zone formed by the cathode 3081 of the dedusting electric field and the anode 3082 of the intake dedusting electric field, the ionized oxygen formed by the ionization zone will charge the electrons to the dust, so that the dust continues to be charged, and is adsorbed by the anode 3082 of the intake air dedusting electric field of the opposite pole.
  • the intake electric field device can form two or more power-on modes.
  • the ionization discharge corona electric field formed between the cathode 3081 of the intake air dedusting electric field and the anode 3082 of the intake air dedusting electric field can be used to ionize oxygen to charge the pollutants, and then use the intake air to remove dust
  • the electric field anode 3082 collects pollutants; when the oxygen content in the gas is too low, or in an oxygen-free state, or the pollutants are conductive dust, etc., the air intake front electrode 3083 is used to directly power up the pollutants to fully charge the pollutants. It is adsorbed by the anode 3082 of the air intake and dust removal electric field.
  • the above two charged electric fields are used to collect high-resistance dust that is easy to charge and low-resistance metal dust, aerosol, liquid mist, etc. that are easy to be charged.
  • the two power-on methods are used at the same time, and the application range of the electric field is expanded.
  • the present invention effectively overcomes various shortcomings in the prior art and has high industrial utilization value.

Abstract

一种发动机进气除尘系统(101)和方法，发动机进气除尘系统(101)包括进气除尘系统入口(1011)、进气除尘系统出口、进气电场装置(1014)。发动机进气除尘系统(101)和方法能有效除去欲进入发动机的气体中的颗粒物，使得进入发动机的气体更加清洁。

Description

一种发动机进气除尘系统及方法 技术领域
本发明属于环保领域，涉及一种发动机进气除尘系统及方法。
背景技术
发动机进气系统对于发动机的功能至关重要，它将空气引导至发动机的各个气缸。现有发动机进气系统包括空气滤清器，用于清除空气中的污染物。根据地点、气候和季节的不同，空气中还可能包含许多污染物，例如烟灰，花粉，灰尘，污垢，树叶和昆虫。这些污染物中可能导致发动机零件过度磨损，也可能造成进气系统阻塞。发动机进气系统的筛网通常会清除大多数较大的颗粒，例如昆虫和树叶，而空气过滤器会捕集较细的颗粒，例如灰尘，污垢和花粉。一般来讲，空气过滤器可捕获80％至90％的5μm以下的颗粒。
现有的发动机空气滤清器有许多缺点。例如，它在去除颗粒(尤其是细颗粒)方面不是非常有效。此外，现有的发动机空气滤清器会产生空气阻力并减少进入发动机的空气。
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发动机进气除尘系统及方法，用于克服现有技术的至少一个缺点。本发明使用电离除尘方法对发动机进气进行除尘处理，该方法没有压差，对进入发动机的空气不会产生阻力。同时，本发明研究发现发动机进气中的灰尘、污垢和花粉等颗粒物的量对发动机排放的尾气中颗粒物的量有一定的影响，减少发动机进气中颗粒物含量，可显著降低发动机尾气中颗粒物含量，确保尾气达到排放标准。本发明在电离电场的阳极和阴极之间还设有与电离电场不平行的辅助电场，辅助电场能给阳离子施加朝向电离电场的出口的力，使得氧离子流向出口的流速大于空气流速，起到增氧作用，进入发动机的进气中氧气含量增多，进而大大提高发动机的功率。
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1：一种进气除尘系统，包括进气除尘系统入口、进气除尘系统出口、进气电场装置。
2.本发明提供的示例2：包括上述示例1，其中，所述进气电场装置包括进气电场装置入口、进气电场装置出口、进气除尘电场阴极和进气除尘电场阳极，所述进气除尘电场阴极和所述进气除尘电场阳极用于产生进气电离除尘电场。
3.本发明提供的示例3：包括上述示例2，其中，所述进气除尘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进气电场装置入口，第二阳极部靠近所述进气电场装置出口，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。
4.本发明提供的示例4：包括上述示例3，其中，所述进气电场装置还包括进气绝缘机构，用于实现所述阴极支撑板和所述进气除尘电场阳极之间的绝缘。
5.本发明提供的示例5：包括上述示例3，其中，所述进气除尘电场阳极和所述进气除尘电场阴极之间形成电场流道，所述进气绝缘机构设置在所述电场流道外。
6.本发明提供的示例6：包括上述示例4或5，其中，所述进气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。
7.本发明提供的示例7：包括上述示例6，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。
8.本发明提供的示例8：包括上述示例7，其中，伞状串陶瓷柱或伞状串玻璃柱的外缘与所述进气除尘电场阳极的距离大于电场距离1.4倍，伞状串陶瓷柱或伞状串玻璃柱的伞突边间距总和大于伞状串陶瓷柱或伞状串玻璃柱的绝缘间距1.4倍，伞状串陶瓷柱或伞状串玻璃柱的伞边内深总长大于伞状串陶瓷柱或伞状串玻璃柱的绝缘距离1.4倍。
9.本发明提供的示例9：包括上述示例3至8中的任一项，其中，所述第一阳极部的长度是所述进气除尘电场阳极长度的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。
10.本发明提供的示例10：包括上述示例3至9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，减少积累在所述进气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。
11.本发明提供的示例11：包括上述示例3至10中的任一项，其中，所述第二阳极部包括积尘段和预留积尘段。
12.本发明提供的示例12：包括上述示例2至11中的任一项，其中，所述进气除尘电场阴极包括至少一根电极棒。
13.本发明提供的示例13：包括上述示例12，其中，所述电极棒的直径不大于3mm。
14.本发明提供的示例14：包括上述示例12或13，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。
15.本发明提供的示例15：包括上述示例2至14中的任一项，其中，所述进气除尘电场阳极由中空的管束组成。
16.本发明提供的示例16：包括上述示例15，其中，所述进气除尘电场阳极管束的中空 的截面采用圆形或多边形。
17.本发明提供的示例17：包括上述示例16，其中，所述多边形为六边形。
18.本发明提供的示例18：包括上述示例14至17中的任一项，其中，所述进气除尘电场阳极的管束呈蜂窝状。
19.本发明提供的示例19：包括上述示例2至18中的任一项，其中，所述进气除尘电场阴极穿射于所述进气除尘电场阳极内。
20.本发明提供的示例20：包括上述示例2至19中的任一项，其中，当电场积尘到一定程度时，所述进气电场装置进行除尘处理。
21.本发明提供的示例21：包括上述示例20，其中，所述进气电场装置检测电场电流来确定是否积尘到一定程度，需要进行除尘处理。
22.本发明提供的示例22：包括上述示例20或21，其中，所述进气电场装置增高电场电压来进行除尘处理。
23.本发明提供的示例23：包括上述示例20或21，其中，所述进气电场装置利用电场反电晕放电现象来进行除尘处理。
24.本发明提供的示例24：包括上述示例20或21，其中，所述进气电场装置利用电场反电晕放电现象，增高电场电压，限制入注电流，使发生在阳极积碳位置的急剧放电产生等离子，所述等离子使灰尘有机成分深度氧化，高分子键断裂，形成小分子二氧化碳和水，来进行除尘处理。
25.本发明提供的示例25：包括上述示例2至24中的任一项，其中，所述进气电场装置还包括辅助电场单元，用于产生与所述进气电离除尘电场不平行的辅助电场。
26.本发明提供的示例26：包括上述示例2至24中的任一项，其中，所述进气电场装置还包括辅助电场单元，所述进气电离除尘电场包括流道，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。
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进气电离除尘电场的进口。
28.本发明提供的示例28：包括上述示例27，其中，所述第一电极为阴极。
29.本发明提供的示例29：包括上述示例27或28，其中，所述辅助电场单元的第一电极是所述进气除尘电场阴极的延伸。
30.本发明提供的示例30：包括上述示例29，其中，所述辅助电场单元的第一电极与所述进气除尘电场阳极具有夹角α，且0°＜α≤125°、或45°≤α≤125°、或60°≤α≤100°、或α＝90°。
31.本发明提供的示例31：包括上述示例25至30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进气电离除尘电场的出口。
32.本发明提供的示例32：包括上述示例31，其中，所述第二电极为阳极。
33.本发明提供的示例33：包括上述示例31或32，其中，所述辅助电场单元的第二电极是所述进气除尘电场阳极的延伸。
34.本发明提供的示例34：包括上述示例33，其中，所述辅助电场单元的第二电极与所述进气除尘电场阴极具有夹角α，且0°＜α≤125°、或45°≤α≤125°、或60°≤α≤100°、或α＝90°。
35.本发明提供的示例35：包括上述示例25至28、31和32中的任一项，其中，所述辅助电场的电极与所述进气电离除尘电场的电极独立设置。
36.本发明提供的示例36：包括上述示例2至35中的任一项，其中，所述进气除尘电场阳极的积尘面积与所述进气除尘电场阴极的放电面积的比为1.667：1-1680：1。
37.本发明提供的示例37：包括上述示例2至35中的任一项，其中，所述进气除尘电场阳极的积尘面积与所述进气除尘电场阴极的放电面积的比为6.67：1-56.67：1。
38.本发明提供的示例38：包括上述示例2至37中的任一项，其中，所述进气除尘电场阴极直径为1-3毫米，所述进气除尘电场阳极与所述进气除尘电场阴极的极间距为2.5-139.9毫米；所述进气除尘电场阳极的积尘面积与所述进气除尘电场阴极的放电面积的比为1.667：1-1680：1。
39.本发明提供的示例39：包括上述示例2至37中的任一项，其中，所述进气除尘电场阳极和所述进气除尘电场阴极的极间距小于150mm。
40.本发明提供的示例40：包括上述示例2至37中的任一项，其中，所述进气除尘电场阳极与所述进气除尘电场阴极的极间距为2.5-139.9mm。
41.本发明提供的示例41：包括上述示例2至37中的任一项，其中，所述进气除尘电场阳极与所述进气除尘电场阴极的极间距为5-100mm。
42.本发明提供的示例42：包括上述示例2至41中的任一项，其中，所述进气除尘电场阳极长度为10-180mm。
43.本发明提供的示例43：包括上述示例2至41中的任一项，其中，所述进气除尘电场阳极长度为60-180mm。
44.本发明提供的示例44：包括上述示例2至43中的任一项，其中，所述进气除尘电场阴极长度为30-180mm。
45.本发明提供的示例45：包括上述示例2至43中的任一项，其中，所述进气除尘电场 阴极长度为54-176mm。
46.本发明提供的示例46：包括上述示例36至45中的任一项，其中，当运行时，所述进气电离除尘电场的耦合次数≤3。
47.本发明提供的示例47：包括上述示例25至45中的任一项，其中，当运行时，所述进气电离除尘电场的耦合次数≤3。
48.本发明提供的示例48：包括上述示例2至47中的任一项，其中，所述进气电离除尘电场电压的取值范围为1kv-50kv。
49.本发明提供的示例49：包括上述示例2至48中的任一项，其中，所述进气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大于所述极间距的1.4倍。
51.本发明提供的示例51：包括上述示例2至50中的任一项，其中，所述进气电场装置还包括进气前置电极，所述进气前置电极在所述进气电场装置入口与所述进气除尘电场阳极和所述进气除尘电场阴极形成的进气电离除尘电场之间。
52.本发明提供的示例52：包括上述示例51，其中，所述进气前置电极呈点状、线状、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。
53.本发明提供的示例53：包括上述示例51或52，其中，所述进气前置电极上设有进气通孔。
54.本发明提供的示例54：包括上述示例53，其中，所述进气通孔呈多角形、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，所述进气通孔的大小为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，所述进气前置电极为固体、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，所述进气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，所述进气前置电极为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，所述进气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，在工作时，在带污染物的气体进入所述进气除尘电场阴极、进气除尘电场阳极形成的进气电离除尘电场之前，且带污染物的气体通过所述进气前置电极时，所述进气前置电极使气体中的污染物带电。
61.本发明提供的示例61：包括上述示例60，其中，当带污染物的气体进入所述进气电离除尘电场时，所述进气除尘电场阳极给带电的污染物施加吸引力，使污染物向所述进气除尘电场阳极移动，直至污染物附着在所述进气除尘电场阳极上。
62.本发明提供的示例62：包括上述示例60或61，其中，所述进气前置电极将电子导入污染物，电子在位于所述进气前置电极和所述进气除尘电场阳极之间的污染物之间进行传递，使更多污染物带电。
63.本发明提供的示例63：包括上述示例60至62中的任一项，其中，所述进气前置电极和所述进气除尘电场阳极之间通过污染物传导电子、并形成电流。
64.本发明提供的示例64：包括上述示例60至63中的任一项，其中，所述进气前置电极通过与污染物接触的方式使污染物带电。
65.本发明提供的示例65：包括上述示例60至64中的任一项，其中，所述进气前置电极通过能量波动的方式使污染物带电。
66.本发明提供的示例66：包括上述示例60至65中的任一项，其中，所述进气前置电极上设有进气通孔。
67.本发明提供的示例67：包括上述示例51至66中的任一项，其中，所述进气前置电极呈线状，所述进气除尘电场阳极呈面状。
68.本发明提供的示例68：包括上述示例51至67中的任一项，其中，所述进气前置电极垂直于所述进气除尘电场阳极。
69.本发明提供的示例69：包括上述示例51至68中的任一项，其中，所述进气前置电极与所述进气除尘电场阳极相平行。
70.本发明提供的示例70：包括上述示例50至68中的任一项，其中，所述进气前置电极呈曲线状或圆弧状。
71.本发明提供的示例71：包括上述示例51至70中的任一项，其中，所述进气前置电极采用金属丝网。
72.本发明提供的示例72：包括上述示例51至71中的任一项，其中，所述进气前置电极与所述进气除尘电场阳极之间的电压不同于所述进气除尘电场阴极与所述进气除尘电场阳极之间的电压。
73.本发明提供的示例73：包括上述示例51至72中的任一项，其中，所述进气前置电极与所述进气除尘电场阳极之间的电压小于起始起晕电压。
74.本发明提供的示例74：包括上述示例51至73中的任一项，其中，所述进气前置电极与所述进气除尘电场阳极之间的电压为0.1kv/mm-2kv/mm。
75.本发明提供的示例75：包括上述示例51至74中的任一项，其中，所述进气电场装置包括进气流道，所述进气前置电极位于所述进气流道中；所述进气前置电极的截面面积与进气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％。
76.本发明提供的示例76：包括上述示例2至75中的任一项，其中，所述进气电场装置包括进气驻极体元件。
77.本发明提供的示例77：包括上述示例76，其中，所述进气除尘电场阳极和所述进气除尘电场阴极接通电源时，所述进气驻极体元件在所述进气电离除尘电场中。
78.本发明提供的示例78：包括上述示例76或77，其中，所述进气驻极体元件靠近所述进气电场装置出口，或者，所述进气驻极体元件设于所述进气电场装置出口。
79.本发明提供的示例79：包括上述示例77至78中的任一项，其中，所述进气除尘电场阳极和所述进气除尘电场阴极形成进气流道，所述进气驻极体元件设于所述进气流道中。
80.本发明提供的示例80：包括上述示例79，其中，所述进气流道包括进气流道出口，所述进气驻极体元件靠近所述进气流道出口，或者，所述进气驻极体元件设于所述进气流道出口。
81.本发明提供的示例81：包括上述示例79或80，其中，所述进气驻极体元件于所述进气流道中的横截面占进气流道横截面5％-100％。
82.本发明提供的示例82：包括上述示例81，其中，所述进气驻极体元件于所述进气流道中的横截面占进气流道横截面10％-90％、20％-80％、或40％-60％。
83.本发明提供的示例83：包括上述示例76至82中的任一项，其中，所述进气电离除尘电场给所述进气驻极体元件充电。
84.本发明提供的示例84：包括上述示例76至83中的任一项，其中，所述进气驻极体元件具有多孔结构。
85.本发明提供的示例85：包括上述示例76至84中的任一项，其中，所述进气驻极体元件为织品。
86.本发明提供的示例86：包括上述示例76至85中的任一项，其中，所述进气除尘电场阳极内部为管状，所述进气驻极体元件外部为管状，所述进气驻极体元件外部套设于所述进 气除尘电场阳极内部。
87.本发明提供的示例87：包括上述示例76至86中的任一项，其中，所述进气驻极体元件与所述进气除尘电场阳极为可拆卸式连接。
88.本发明提供的示例88：包括上述示例76至87中的任一项，其中，所述进气驻极体元件的材料包括具有驻极性能的无机化合物。
89.本发明提供的示例89：包括上述示例88，其中，所述无机化合物选自含氧化合物、含氮化合物或玻璃纤维中的一种或多种组合。
90.本发明提供的示例90：包括上述示例89，其中，所述含氧化合物选自金属基氧化物、含氧复合物、含氧的无机杂多酸盐中的一种或多种组合。
91.本发明提供的示例91：包括上述示例90，其中，所述金属基氧化物选自氧化铝、氧化锌、氧化锆、氧化钛、氧化钡、氧化钽、氧化硅、氧化铅、氧化锡中的一种或多种组合。
92.本发明提供的示例92：包括上述示例90，其中，所述金属基氧化物为氧化铝。
93.本发明提供的示例93：包括上述示例90，其中，所述含氧复合物选自钛锆复合氧化物或钛钡复合氧化物中的一种或多种组合。
94.本发明提供的示例94：包括上述示例90，其中，所述含氧的无机杂多酸盐选自钛酸锆、锆钛酸铅或钛酸钡中的一种或多种组合。
95.本发明提供的示例95：包括上述示例89，其中，所述含氮化合物为氮化硅。
96.本发明提供的示例96：包括上述示例76至95中的任一项，其中，所述进气驻极体元件的材料包括具有驻极性能的有机化合物。
97.本发明提供的示例97：包括上述示例96，其中，所述有机化合物选自氟聚合物、聚碳酸酯、PP、PE、PVC、天然蜡、树脂、松香中的一种或多种组合。
98.本发明提供的示例98：包括上述示例97，其中，所述氟聚合物选自聚四氟乙烯、聚全氟乙丙烯、可溶性聚四氟乙烯、聚偏氟乙烯中的一种或多种组合。
99.本发明提供的示例99：包括上述示例97，其中，所述氟聚合物为聚四氟乙烯。
100.本发明提供的示例100：包括上述示例1至99中的任一项，其中，还包括进气均风装置。
101.本发明提供的示例101：包括上述示例100，其中，所述进气均风装置在所述进气除尘系统入口与所述进气除尘电场阳极和所述进气除尘电场阴极形成的进气电离除尘电场之间，当所述进气除尘电场阳极为四方体时，所述进气均风装置包括：设置于所述进气除尘电场阳极一侧边的进气管和设置于另一侧边的出气管；其中，所述进气管与所述出气管相对立。
102.本发明提供的示例102：包括上述示例100，其中，所述进气均风装置在所述进气除尘系统入口与所述进气除尘电场阳极和所述进气除尘电场阴极形成的进气电离除尘电场之间，当所述进气除尘电场阳极为圆柱体时，所述进气均风装置由若干可旋转的均风叶片组成。
103.本发明提供的示例103：包括上述示例100，其中，所述进气均风装置第一文氏板均风机构和设置于所述进气除尘电场阳极的出气端的第二文氏板均风机构，所述第一文氏板均风机构上开设有进气孔，所述第二文氏板均风机构上开设有出气孔，所述进气孔与所述出气孔错位排布，且正面进气侧面出气，形成旋风结构。
104.本发明提供的示例104：包括上述示例1至103中的任一项，其中，还包括除臭氧装置，用于去除去或减少所述进气电场装置产生的臭氧，所述除臭氧装置在所述进气电场装置出口与所述进气除尘系统出口之间。
105.本发明提供的示例105：包括上述示例104，其中，所述除臭氧装置还包括臭氧消解器。
106.本发明提供的示例106：包括上述示例105，其中，所述臭氧消解器选自紫外线臭氧消解器和催化臭氧消解器中的至少一种。
107.本发明提供的示例107：包括上述示例1至106中的任一项，其中，还包括离心分离机构。
108.本发明提供的示例108：包括上述示例107，其中，所述离心分离机构包括气流转向通道，且气流转向通道能改变气流的流动方向。
109.本发明提供的示例109：包括上述示例108，其中，所述气流转向通道能引导气体沿圆周方向流动。
110.本发明提供的示例110：包括上述示例107或108，其中，所述气流转向通道呈螺旋形或圆锥形。
111.本发明提供的示例111：包括上述示例107至110中的任一项，其中，所述离心分离机构包括分离筒。
112.本发明提供的示例112：包括上述示例111，其中，所述分离筒中设有所述气流转向通道，所述分离筒的底部设有出尘口。
113.本发明提供的示例113：包括上述示例111或112，其中，所述分离筒侧壁上设有与所述气流转向通道的第一端相连通的进气口。
114.本发明提供的示例114：包括上述示例111至113中的任一项，其中，所述分离筒的顶部设有与所述气流转向通道的第二端相连通的出气口。
115.本发明提供的示例115：包括上述示例1至114中的任一项，其中，还包括发动机。
116.本发明提供的示例116：一种发动机进气电场除尘方法，包括以下步骤：
使含尘气体通过进气除尘电场阳极和进气除尘电场阴极产生的电离除尘电场；
进气电场积尘时，进行清尘处理。
117.本发明提供的示例117：包括示例116的发动机进气电场除尘方法，其中，利用电场反电晕放电现象完成清尘处理。
118.本发明提供的示例118：包括示例116的发动机进气电场除尘方法，其中，利用电场反电晕放电现象，增高电压，限制入注电流，完成清尘处理。
119.本发明提供的示例119：包括示例116的发动机进气电场除尘方法，其中，利用电场反电晕放电现象，增高电压，限制入注电流，使发生在阳极积尘位置的急剧放电产生等离子，所述等离子使灰尘有机成分深度氧化，高分子键断裂，形成小分子二氧化碳和水，完成清尘处理。
120.本发明提供的示例120：包括示例116至119任一项的发动机进气电场除尘方法，其中，当所述电场装置检测到电场电流增加到一个给定值，所述电场装置进行清尘处理。
121.本发明提供的示例121：包括示例116至120任一项的发动机进气电场除尘方法，其中，所述除尘电场阴极包括至少一根电极棒。
122.本发明提供的示例122：包括示例121的发动机进气电场除尘方法，其中，所述电极棒的直径不大于3mm。
123.本发明提供的示例123：包括示例121或122的发动机进气电场除尘方法，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。
124.本发明提供的示例124：包括示例116至123任一项的发动机进气电场除尘方法，其中，所述除尘电场阳极由中空的管束组成。
125.本发明提供的示例125：包括示例124的发动机进气电场除尘方法，其中，所述阳极管束的中空的截面采用圆形或多边形。
126.本发明提供的示例126：包括示例125的发动机进气电场除尘方法，其中，所述多边形为六边形。
127.本发明提供的示例127：包括示例124至126任一项的发动机进气电场除尘方法，其中，所述除尘电场阳极的管束呈蜂窝状。
128.本发明提供的示例128：包括示例116至127任一项的发动机进气电场除尘方法，其中，所述除尘电场阴极穿射于所述除尘电场阳极内。
129.本发明提供的示例129：包括示例116至128任一项的发动机进气电场除尘方法，其中，当检测到的电场电流增加到一个给定值时，进行清尘处理。
130.本发明提供的示例130：一种给发动机进气增氧的方法，包括以下步骤：
使进气通过一个流道；
在流道中产生电场，所述电场不与所述流道垂直，所述电场包括进口和出口。
131.本发明提供的示例131：包括示例130的给发动机进气增氧的方法，其中，所述电场包括第一阳极和第一阴极，所述第一阳极和第一阴极形成所述流道，所述流道接通所述进口和出口。
132.本发明提供的示例132：包括示例130至131任一项的给发动机进气增氧的方法，其中，所述第一阳极和第一阴极电离所述进气中的氧气。
133.本发明提供的示例133：包括示例130至132任一项的给发动机进气增氧的方法，其中，所述电场包括第二电极，所述第二电极设置在或靠近所述进口。
134.本发明提供的示例134：包括示例133的给发动机进气增氧的方法，其中，所述第二电极为阴极。
135.本发明提供的示例135：包括示例133或134的给发动机进气增氧的方法，其中，所述第二电极是所述第一阴极的延伸。
136.本发明提供的示例136：包括示例135的给发动机进气增氧的方法，其中，所述第二电极与所述第一阳极具有夹角α，且0°＜α≤125°、或45°≤α≤125°、或60°≤α≤100°、或α＝90°。
137.本发明提供的示例137：包括示例130至136任一项的给发动机进气增氧的方法，其中，所述电场包括第三电极，所述第三电极设置在或靠近所述出口。
138.本发明提供的示例138：包括示例137的给发动机进气增氧的方法，其中，所述第三电极为阳极。
139.本发明提供的示例139：包括示例137或138的给发动机进气增氧的方法，其中，所述第三电极是所述第一阳极的延伸。
140.本发明提供的示例140：包括示例139的给发动机进气增氧的方法，其中，所述第三电极与所述第一阴极具有夹角α，且0°＜α≤125°、或45°≤α≤125°、或60°≤α≤100°、或α＝90°。
141.本发明提供的示例141：包括示例135至140任一项的给发动机进气增氧的方法，其中，所述第三电极与所述第一阳极和第一阴极独立设置。
142.本发明提供的示例142：包括示例133至141任一项的给发动机进气增氧的方法，其中，所述第二电极与所述第一阳极和第一阴极独立设置。
143.本发明提供的示例143：包括示例131至142任一项的给发动机进气增氧的方法，其中，所述第一阴极包括至少一根电极棒。
144.本发明提供的示例144：包括示例131至143任一项的给发动机进气增氧的方法，其中，所述第一阳极由中空的管束组成。
145.本发明提供的示例145：包括示例144的给发动机进气增氧的方法，其中，所述阳极管束的中空的截面采用圆形或多边形。
146.本发明提供的示例146：包括示例145的给发动机进气增氧的方法，其中，所述多边形为六边形。
147.本发明提供的示例147：包括示例144至146任一项的给发动机进气增氧的方法，其中，所述第一阳极的管束呈蜂窝状。
148.本发明提供的示例148：包括示例131至147任一项的给发动机进气增氧的方法，其中，所述第一阴极穿射于所述第一阳极内。
149.本发明提供的示例149：包括示例131至148任一项的给发动机进气增氧的方法，其中，所述电场作用于所述流道中的氧气离子，增加氧气离子流量，增加所述出口进气含氧量。
150.本发明提供的示例150：一种减少发动机进气除尘电场耦合的方法，包括以下步骤：
选择进气除尘电场阳极参数或/和进气除尘电场阴极参数以减少电场耦合次数。
151.本发明提供的示例151：包括示例150的减少发动机进气除尘电场耦合的方法，其中，包括选择所述进气除尘电场阳极的集尘面积与进气除尘电场阴极的放电面积的比。
152.本发明提供的示例152：包括示例151的减少发动机进气除尘电场耦合的方法，其中，包括选择所述进气除尘电场阳极的积尘面积与所述进气除尘电场阴极的放电面积的比为1.667：1-1680：1。
153.本发明提供的示例153：包括示例151的减少发动机进气除尘电场耦合的方法，其中，包括选择所述进气除尘电场阳极的积尘面积与所述进气除尘电场阴极的放电面积的比为6.67：1-56.67：1。
154.本发明提供的示例154：包括示例150至153任一项的减少发动机进气除尘电场耦合的方法，其中，包括选择所述进气除尘电场阴极直径为1-3毫米，所述进气除尘电场阳极与所述进气除尘电场阴极的极间距为2.5-139.9毫米；所述进气除尘电场阳极的积尘面积与所述进气除尘电场阴极的放电面积的比为1.667：1-1680：1。
155.本发明提供的示例155：包括示例150至154任一项的减少发动机进气除尘电场耦合的方法，其中，包括选择所述进气除尘电场阳极和所述进气除尘电场阴极的极间距小于 150mm。
156.本发明提供的示例156：包括示例150至154任一项的减少发动机进气除尘电场耦合的方法，其中，包括选择所述进气除尘电场阳极与所述进气除尘电场阴极的极间距为2.5-139.9mm。
157.本发明提供的示例157：包括示例150至154任一项的减少发动机进气除尘电场耦合的方法，其中，包括选择所述进气除尘电场阳极与所述进气除尘电场阴极的极间距为5-100mm。
158.本发明提供的示例158：包括示例150至157任一项的减少发动机进气除尘电场耦合的方法，其中，包括选择所述进气除尘电场阳极长度为10-180mm。
159.本发明提供的示例159：包括示例150至157任一项的减少发动机进气除尘电场耦合的方法，其中，包括选择所述进气除尘电场阳极长度为60-180mm。
160.本发明提供的示例160：包括示例150至159任一项的减少发动机进气除尘电场耦合的方法，其中，包括选择所述进气除尘电场阴极长度为30-180mm。
161.本发明提供的示例161：包括示例150至159任一项的减少发动机进气除尘电场耦合的方法，其中，包括选择所述进气除尘电场阴极长度为54-176mm。
162.本发明提供的示例162：包括示例150至161任一项的减少发动机进气除尘电场耦合的方法，其中，包括选择所述进气除尘电场阴极包括至少一根电极棒。
163.本发明提供的示例163：包括示例162的减少发动机进气除尘电场耦合的方法，其中，包括选择所述电极棒的直径不大于3mm。
164.本发明提供的示例164：包括示例162或163的减少发动机进气除尘电场耦合的方法，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。
165.本发明提供的示例165：包括示例150至164任一项的减少发动机进气除尘电场耦合的方法，其中，包括选择所述进气除尘电场阳极由中空的管束组成。
166.本发明提供的示例166：包括示例165的减少发动机进气除尘电场耦合的方法，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。
167.本发明提供的示例167：包括示例166的减少发动机进气除尘电场耦合的方法，其中，包括选择所述多边形为六边形。
168.本发明提供的示例168：包括示例165至167任一项的减少发动机进气除尘电场耦合的方法，其中，包括选择所述进气除尘电场阳极的管束呈蜂窝状。
169.本发明提供的示例169：包括示例150至168任一项的减少发动机进气除尘电场耦合的方法，其中，包括选择所述进气除尘电场阴极穿射于所述进气除尘电场阳极内。
170.本发明提供的示例170：包括示例150至169任一项的减少发动机进气除尘电场耦合的方法，其中，包括选择的所述进气除尘电场阳极或/和进气除尘电场阴极尺寸使电场耦合次数≤3。
171.本发明提供的示例171：一种发动机进气除尘方法，包括如下步骤：
1)利用进气电离除尘电场吸附进气中的颗粒物；
2)利用进气电离除尘电场给进气驻极体元件充电。
172.本发明提供的示例172：包括示例171的发动机进气除尘方法，其中，所述进气驻极体元件靠近进气电场装置出口，或者，所述进气驻极体元件设于进气电场装置出口。
173.本发明提供的示例173：包括示例171的发动机进气除尘方法，其中，所述进气除尘电场阳极和所述进气除尘电场阴极形成进气流道，所述进气驻极体元件设于所述进气流道中。
174.本发明提供的示例174：包括示例173的发动机进气除尘方法，其中，所述进气流道包括进气流道出口，所述进气驻极体元件靠近所述进气流道出口，或者，所述进气驻极体元件设于所述进气流道出口。
175.本发明提供的示例175：包括示例171至174任一项的发动机进气除尘方法，其中，当进气电离除尘电场无上电驱动电压时，利用充电的进气驻极体元件吸附进气中的颗粒物。
176.本发明提供的示例176：包括示例174的发动机进气除尘方法，其中，在充电的进气驻极体元件吸附一定的进气中的颗粒物后，将其替换为新的进气驻极体元件。
177.本发明提供的示例177：包括示例176的发动机进气除尘方法，其中，替换为新的进气驻极体元件后重新启动进气电离除尘电场吸附进气中的颗粒物，并给新的进气驻极体元件充电。
178.本发明提供的示例178：包括示例171至177任一项的发动机进气除尘方法，其中，所述进气驻极体元件的材料包括具有驻极性能的无机化合物。
179.本发明提供的示例179：包括示例178的发动机进气除尘方法，其中，所述无机化合物选自含氧化合物、含氮化合物或玻璃纤维中的一种或多种组合。
180.本发明提供的示例180：包括示例179的发动机进气除尘方法，其中，所述含氧化合物选自金属基氧化物、含氧复合物、含氧的无机杂多酸盐中的一种或多种组合。
181.本发明提供的示例181：包括示例180的发动机进气除尘方法，其中，所述金属基氧化物选自氧化铝、氧化锌、氧化锆、氧化钛、氧化钡、氧化钽、氧化硅、氧化铅、氧化锡中的一种或多种组合。
182.本发明提供的示例182：包括示例180的发动机进气除尘方法，其中，所述金属基氧 化物为氧化铝。
183.本发明提供的示例183：包括示例180的发动机进气除尘方法，其中，所述含氧复合物选自钛锆复合氧化物或钛钡复合氧化物中的一种或多种组合。
184.本发明提供的示例184：包括示例180的发动机进气除尘方法，其中，所述含氧的无机杂多酸盐选自钛酸锆、锆钛酸铅或钛酸钡中的一种或多种组合。
185.本发明提供的示例185：包括示例179的发动机进气除尘方法，其中，所述含氮化合物为氮化硅。
186.本发明提供的示例186：包括示例171至177任一项的发动机进气除尘方法，其中，所述进气驻极体元件的材料包括具有驻极性能的有机化合物。
187.本发明提供的示例187：包括示例186的发动机进气除尘方法，其中，所述有机化合物选自氟聚合物、聚碳酸酯、PP、PE、PVC、天然蜡、树脂、松香中的一种或多种组合。
188.本发明提供的示例188：包括示例187的发动机进气除尘方法，其中，所述氟聚合物选自聚四氟乙烯、聚全氟乙丙烯、可溶性聚四氟乙烯、聚偏氟乙烯中的一种或多种组合。
189.本发明提供的示例189：包括示例187的发动机进气除尘方法，其中，所述氟聚合物为聚四氟乙烯。
190.本发明提供的示例190：一种发动机进气除尘方法，其特征在于，包括以下步骤：所述进气经进气电离除尘后去除或减少进气电离除尘产生的臭氧。
191.本发明提供的示例191：包括示例190的发动机进气除尘方法，其中，对进气电离除尘产生的臭氧进行臭氧消解。
192.本发明提供的示例192：包括示例190的发动机进气除尘方法，其中，所述臭氧消解选自紫外线消解和催化消解中的至少一种。
附图说明
图1为本发明的发动机进气除尘系统中进气除尘系统于一实施例中的结构示意图。
图2为本发明的发动机进气除尘系统中设置于进气电场装置内的第一滤水机构的另一实施例结构图。
图3A为本发明的发动机进气除尘系统中进气电场装置的进气均风装置的一种实施结构图。
图3B为本发明的发动机进气除尘系统中进气电场装置的进气均风装置的另一种实施结构图。
图3C为本发明的发动机进气除尘系统中进气电场装置的进气均风装置的又一种实施结 构图。
图3D为本发明的发动机进气除尘系统中进气电场装置的中第二文氏板均风机构的俯视结构图。
图4为本发明是实施例2进气电场装置的示意图。
图5为本发明实施例3进气电场装置的示意图。
图6为本发明图1的进气电场装置的俯视图。
图7为实施例3进气驻极体元件于进气流道中的横截面占进气流道横截面的示意图。
图8为本发明实施例4进气除尘系统的示意图。
图9为电场发生单元结构示意图。
图10为图9电场发生单元的A-A视图。
图11为标注长度和角度的图9电场发生单元的A-A视图。
图12为两个电场级的电场装置结构示意图。
图13为本发明实施例17中电场装置的结构示意图。
图14为本发明实施例19中电场装置的结构示意图。
图15为本发明实施例20中电场装置的结构示意图。
图16为本发明实施例22中进气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。
于本发明的一实施例中的发动机进气除尘系统包括离心分离机构。于本发明一实施例中离心分离机构包括气流转向通道，该气流转向通道能改变气流的流动方向。当含有颗粒物的气体流经气流转向通道时，气体的流动方向将发生改变；而气体中的颗粒物等将在惯性作用下继续沿原方向移动，直至与气流转向通道的侧壁、即离心分离机构的内壁发生碰撞，颗粒 物无法沿原方向继续移动，且在重力作用下向下掉落，这样，颗粒物就从气体中分离出来。
于本发明一实施例中气流转向通道能引导气体沿圆周方向流动。于本发明一实施例中气流转向通道可以呈螺旋形或圆锥形。于本发明一实施例中离心分离机构包括分离筒。分离筒中设有所述气流转向通道，分离筒的底部可设有出尘口。分离筒侧壁上可设有与气流转向通道的第一端相连通的进气口。分离筒的顶部可设有与气流转向通道的第二端相连通的出气口。出气口也称作排气口，且排气口的大小可根据所需的进气量大小进行设置。气体由进气口流入分离筒的气流转向通道后，气体将由直线运动变为圆周运动，而气体中的颗粒物将在惯性作用下继续沿直线方向运动，直至颗粒物与分离筒的内壁碰撞，颗粒物不能随气体一起继续流动，颗粒物受重力作用下沉，这样，颗粒物就从气体中分离出来，且颗粒物最终由位于底部的出尘口排出，气体最终由位于顶部的排气口排出。于本发明一实施例中进气电场装置入口与离心分离机构的排气口相连通。分离筒的出气口位于分离筒与进气电场装置的连接处。
于本发明一实施例中离心分离机构可呈弯折型结构。离心分离机构的形状可以是环型、回字型、十字型、T字型、L字型、凹字型、或折型中的一种形状或多种形状的组合。离心分离机构的气流转向通道具有至少一个转弯。当气体流经该转弯处时，其流动方向将发生改变，而气体中的颗粒物将在惯性作用下继续沿原方向移动，直至颗粒物与离心分离机构的内壁相碰撞，碰撞后颗粒物将受重力作用下沉，颗粒物从气体中脱离出来，并最终由位于下端的出粉口排出，而气体最终由排气口流出。
于本发明一实施例中离心分离机构的排气口处可设置第一过滤层，第一过滤层可包括金属网片，该金属网片可垂直于气流方向设置。金属网片将对由排气口排出的气体进行过滤，以将气体中仍未分离的颗粒物过滤掉。
于本发明一实施例中发动机进气除尘系统可包括进气均风装置。该进气均风装置设置在进气电场装置之前，能使进入进气电场装置中的气流均匀通过。
于本发明一实施例中进气电场装置的进气除尘电场阳极可为立方体，进气均风装置可包括位于阴极支撑板一侧边的进气管、及位于阴极支撑板另一侧边的出气管，阴极支撑板位于进气除尘电场阳极的进气端；其中，安装进气管的侧边与安装出气管的侧边相对立。进气均风装置能使进入进气电场装置的气流均匀通过静电场。
于本发明一实施例中进气除尘电场阳极可为圆柱体，进气均风装置位于所述进气除尘系统入口与所述进气除尘电场阳极和所述进气除尘电场阴极形成的进气电离除尘电场之间，且进气均风装置包括若干围绕进气电场装置入口中心旋转的均风叶片。进气均风装置能够使各种变化的进气量均匀通过进气除尘电场阳极产生的电场，同时，能够保持进气除尘电场阳极 内部温度恒定，氧气充足。进气均风装置能使进入进气电场装置的气流均匀通过静电场。
于本发明一实施例中进气均风装置包括设置于进气除尘电场阳极的进气端的进风板和设置于进气除尘电场阳极出气端的出风板，进风板上开设有进气孔，出风板上开设有出气孔，进气孔与出气孔错位排布，且正面进气、侧面出气，形成旋风结构。进气均风装置能使进入进气电场装置的气流均匀通过静电场。
于本发明一实施例中发动机进气除尘系统可包括进气除尘系统入口、进气除尘系统出口和进气电场装置。且于本发明一实施例中进气电场装置可包括进气电场装置入口、进气电场装置出口、及位于进气电场装置入口和进气电场装置出口之间的进气前置电极，当气体由进气电场装置入口流经进气前置电极时，气体中的颗粒物等将带电。
于本发明一实施例中进气电场装置包括进气前置电极，该进气前置电极在进气电场装置入口与进气除尘电场阳极和进气除尘电场阴极形成的进气电离除尘电场之间。当气体由进气电场装置入口流经进气前置电极时，气体中的颗粒物等将带电。
于本发明一实施例中进气前置电极的形状可以为点状、线状、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。当进气前置电极为有孔结构时，进气前置电极上设有一个或多个进气通孔。于本发明一实施例中进气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进气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进气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。当进气前置电极为固体时，可采用固态金属，比如304钢，或其它固态的导体、比如石墨等。当进气前置电极为液体时，可以是含离子导电液体。
在工作时，在带污染物的气体进入进气除尘电场阳极和进气除尘电场阴极形成的进气电离除尘电场之前，且带污染物的气体通过进气前置电极时，进气前置电极使气体中的污染物带电。当带污染物的气体进入进气电离除尘电场时，进气除尘电场阳极给带电的污染物施加吸引力，使污染物向进气除尘电场阳极移动，直至污染物附着在进气除尘电场阳极上。
于本发明一实施例中进气前置电极将电子导入污染物，电子在位于进气前置电极和进气除尘电场阳极之间的污染物之间进行传递，使更多污染物带电。进气前置电极和进气除尘电场阳极之间通过污染物传导电子、并形成电流。
于本发明一实施例中进气前置电极通过与污染物接触的方式使污染物带电。于本发明一 实施例中进气前置电极通过能量波动的方式使污染物带电。于本发明一实施例中进气前置电极通过与污染物接触的方式将电子转移到污染物上，并使污染物带电。于本发明一实施例中进气前置电极通过能量波动的方式将电子转移到污染物上，并使污染物带电。
于本发明一实施例中进气前置电极呈线状，进气除尘电场阳极呈面状。于本发明一实施例中进气前置电极垂直于进气除尘电场阳极。于本发明一实施例中进气前置电极与进气除尘电场阳极相平行。于本发明一实施例中进气前置电极呈曲线状或圆弧状。于本发明一实施例中进气前置电极采用金属丝网。于本发明一实施例中进气前置电极与进气除尘电场阳极之间的电压不同于进气除尘电场阴极和进气除尘电场阳极之间的电压。于本发明一实施例中进气前置电极与进气除尘电场阳极之间的电压小于起始起晕电压。起始起晕电压为进气除尘电场阴极和进气除尘电场阳极之间的电压的最小值。于本发明一实施例中进气前置电极与进气除尘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进气电场装置包括进气流道，进气前置电极位于进气流道中。于本发明一实施例中进气前置电极的截面面积与进气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％。进气前置电极的截面面积是指进气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进气前置电极带负电势。
于本发明一实施例中当气体通过进气电场装置入口流入进气流道中，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进气前置电极相接触时，或与进气前置电极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进气电离除尘电场，进气除尘电场阳极给已带负电的金属粉尘、雾滴、或气溶胶等施加吸引力，使已带负电的污染物向进气除尘电场阳极移动，直至该部分污染物附着在进气除尘电场阳极上，实现将该部分污染物收集起来，同时，进气除尘电场阳极与进气除尘电场阴极之间形成的进气电离除尘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，进气除尘电场阳极给该部分带负电荷的粉尘等污染物施加吸引力，使粉尘等污染物向进气除尘电场阳极移动，直至该部分污染物附着在进气除尘电场阳极上，实现将该部分普通粉尘等污染物也收集起来，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，并使得进气除尘电场阳极能收集气体中污染物的种类更广泛，且收集能力更强，收集效率更高。
于本发明一实施例中进气电场装置入口与分离机构的排气口相连通。
于本发明一实施例中进气电场装置可包括进气除尘电场阴极和进气除尘电场阳极，进气除尘电场阴极与进气除尘电场阳极之间形成电离除尘电场。气体进入电离除尘电场，气体中的氧离子将被电离，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，进气除尘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进气除尘电场阳极上，以清除掉气体中的颗粒物。
于本发明一实施例中，所述进气除尘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积尘要求做调整。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进气除尘电场阳极的形状调整，例如，若进气除尘电场阳极的积尘面是平面，则阴极丝的截面呈圆形；若进气除尘电场阳极的积尘面是圆弧面，阴极丝需要设计成多面形。阴极丝的长度根据进气除尘电场阳极进行调整。
于本发明一实施例中，所述进气除尘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进气除尘电场阳极的形状进行调整，例如，若进气除尘电场阳极的积尘面是平面，则阴极棒的截面需要设计成圆形；若进气除尘电场阳极的积尘面是圆弧面，则阴极棒需要设计成多面形。
于本发明一实施例中，进气除尘电场阴极穿设于进气除尘电场阳极内。
于本发明一实施例中，进气除尘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进气除尘电场阳极。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，进气除尘电场阳极和进气除尘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，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，进气除尘电场阴极安装在阴极支撑板上，阴极支撑板与进气除尘电场阳极通过进气绝缘机构相连接。所述进气绝缘机构用于实现所述阴极支撑板和所述进气除尘电场阳极之间的绝缘。于本发明一实施例中，进气除尘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进气电场装置入口，第二阳极部靠近进气电场装置出口。阴极支撑板和进气绝缘机构在第一阳极部和第二阳极部之间，即进气绝缘机构安装在电离电场中间、或进气除尘电场阴极中间，可以对进气除尘电场阴极起到良好的支撑作用，并对进气 除尘电场阴极起到相对于进气除尘电场阳极的固定作用，使进气除尘电场阴极和进气除尘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进气绝缘机构设置在电场流道外、即第二级流道外，以防止或减少气体中的灰尘等聚集在进气绝缘机构上，导致进气绝缘机构击穿或导电。
于本发明一实施例中，进气绝缘机构采用耐高压陶瓷绝缘子，对进气除尘电场阴极和进气除尘电场阳极之间进行绝缘。进气除尘电场阳极也称作一种外壳。
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进气绝缘机构之前，第一阳极部能够除去气体中的水，防止水进入进气绝缘机构，造成进气绝缘机构短路、打火。另外，第一阳级部能够除去气体中相当一部分的灰尘，当气体通过进气绝缘机构时，相当一部分的灰尘已被消除，减少灰尘造成进气绝缘机构短路的可能性。于本发明一实施例中进气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进气除尘电场阳极和进气除尘电场阴极导通，从而使进气除尘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。在气体流经第二级流道过程中，第一阳极部和进气除尘电场阴极先接触具有污染性的气体，进气绝缘机构后接触气体，达到先除尘后经过进气绝缘机构的目的，减少对进气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。于本发明一实施例中第一阳极部长度占进气除尘电场阳极总长度的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进气绝缘机构之后。第二阳极部包括积尘段和预留积尘段。其中积尘段利用静电吸附气体中的颗粒物，该积尘段是为了增加积尘面积，延长进气电场装置的使用时间。预留积尘段能为积尘段提供失效保护。预留积尘段是为了在满足设计除尘要求的前提下，进一步提高积尘面积，提高除尘效果。预留积尘段作为补充前段积尘使用。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，由于进气除尘电场阴极和进气除尘电场阳极之间存在极高电位差，为了防止进气除尘电场阴极和进气除尘电场阳极导通，进气绝缘机构设置在进气除尘电场阴极和进气除尘电场阳极之间的第二级流道之外。因此，进气绝缘机构外悬于进气除尘电场阳极的外侧。于本发明一实施例中进气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。可根据进气除尘电场阴极和进气除尘电场阳极之间的极间距的1.4倍设置绝缘距离。于本发明一实施例中进气绝缘机构使用陶瓷，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，进气绝缘机构包括绝缘部和隔热部。为了使进气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进气除尘电场阳极的距离大于电场距离的1.4倍、即大于极间距的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、脱硝净化反应腔。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进气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进气除尘电场阴极和进气除尘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。
本发明的进气电场装置的进气除尘电场阴极和进气除尘电场阳极之间形成电离除尘电场。为了减少电离除尘电场发生电场耦合，于本发明一实施例中，减少电场耦合的方法包括如下步骤：选择进气除尘电场阳极的集尘面积与进气除尘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进气除尘电场阳极的集尘面积与进气除尘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进气除尘电场阳极的集尘面积和相对极小的进气除尘电场阴极的 放电面积，具体选择上述面积比，可以减少进气除尘电场阴极的放电面积，减小吸力，扩大进气除尘电场阳极的集尘面积，扩大吸力，即进气除尘电场阴极和进气除尘电场阳极间产生不对称的电极吸力，使荷电后粉尘落入进气除尘电场阳极的集尘表面，虽极性改变但无法再被进气除尘电场阴极吸走，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％。集尘面积是指进气除尘电场阳极工作面的面积，比如，若进气除尘电场阳极呈中空的正六边形管状，集尘面积即为中空的正六边形管状的内表面积，集尘面积也称作积尘面积。放电面积指进气除尘电场阴极工作面的面积，比如，若进气除尘电场阴极呈棒状，放电面积即为棒状的外表面积。
于本发明一实施例中进气除尘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。进气除尘电场阳极的长度是指进气除尘电场阳极工作面的一端至另一端的最小长度。进气除尘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进气除尘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进气除尘电场阳极及进气电场装置具有耐高温特性，并使得进气电场装置在高温冲击下具有高效率的集尘能力。
于本发明一实施例中进气除尘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。进气除尘电场阴极的长度是指除尘电场阴极工作面的一端至另一端的最小长度。进气除尘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进气除尘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进气除尘电场阴极及进气电场装置具有耐高温特性，并使得进气电场装置在高温冲击下具有高效率的集尘能力。
于本发明一实施例中进气除尘电场阳极和进气除尘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。进气除尘电场阳极和进气除尘电场阴极之间的距离也称作极间距。极间距具体是指进气除尘电场阳极、进气除尘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，并使进气电场装置具有耐高温特性。
于本发明一实施例中，所述除尘电场阴极直径为1-3毫米，所述除尘电场阳极与所述除尘电场阴极的极间距为2.5-139.9毫米；所述除尘电场阳极的积尘面积与所述除尘电场阴极的放电面积的比为1.667：1-1680：1。
鉴于电离除尘的特有性能，电离除尘可适用去除气体中的颗粒物。但是，经过许多大学、研究机构、企业的多年的研究，现有电场除尘装置只能去除约70％的颗粒物，不能满足许多行业的需要。另外，现有技术中的电场除尘装置体积过于庞大。
本发明的发明人研究发现，现有技术中电场除尘装置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，本发明提供的电离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，现有电离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。
进气除尘电场阳极和进气除尘电场阴极之间的电离除尘电场也称作第一电场。于本发明一实施例中进气除尘电场阳极和进气除尘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除尘电场的流道不垂直。第二电场也称作辅助电场，可以通过一个或两个第一辅助电极形成当第二电场由一个第一辅助电极形成时，该第一辅助电极可以放在电离除尘电场的进口或出口，该第一辅助电极可以带负电势、或正电势。其中，当所述第一辅助电极为阴极时，设置在或靠近所述电离除尘电场的进口；所述第一辅助电极与所述进气除尘电场阳极具有夹角α，且0°＜α≤125°、或45°≤α≤125°、或 60°≤α≤100°、或α＝90°。当所述第一辅助电极为阳极时，设置在或靠近所述电离除尘电场的出口；所述第一辅助电极与所述进气除尘电场阴极具有夹角α，且0°＜α≤125°、或45°≤α≤125°、或60°≤α≤100°、或α＝90°。当第二电场由两个第一辅助电极形成时，其中一个第一辅助电极可以带负电势，另一个第一辅助电极可以带正电势；一个第一辅助电极可以放在电离电场的进口，另一个第一辅助电极放在电离电场的出口。另外，第一辅助电极可以是进气除尘电场阴极或进气除尘电场阳极的一部分，即第一辅助电极可以是由进气除尘电场阴极或进气除尘电场阳极的延伸段构成，此时进气除尘电场阴极和进气除尘电场阳极的长度不一样。第一辅助电极也可以是一个单独的电极，也就是说第一辅助电极可以不是进气除尘电场阴极或进气除尘电场阳极的一部分，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。
第二电场能给进气除尘电场阳极和进气除尘电场阴极之间带负电荷的氧离子流施加朝向电离电场的出口的力，使得进气除尘电场阳极和进气除尘电场阴极之间带负电荷的氧离子流具有向出口的移动速度。在气体流入电离电场，并向电离电场的出口方向流动过程中，带负电荷的氧离子也在向进气除尘电场阳极且向电离电场的出口方向移动，且带负电荷的氧离子在向进气除尘电场阳极且向电离电场的出口移动过程中将与气体中的颗粒物等相结合，由于氧离子具有向出口的移动速度，氧离子在与颗粒物相结合时，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，保证氧离子易于与颗粒物相结合，并使得气体中的颗粒物的荷电效率更高，进而在进气除尘电场阳极的作用下，能将更多的颗粒物收集起来，保证进气电场装置的除尘效率更高。进气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，从而提高电场的积尘效率，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。进气电场装置在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％。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％。于本发明一实施例中进气电场装置形成的离子流有利于无动力风扇流体输送、进气增氧、或热量交换等。
灰尘清洁
随着，除尘电场阳极持续收集进气中的颗粒物等，颗粒物等在除尘电场阳极上堆积并形成灰尘，且灰尘厚度不断增加，使极间距减小。于本发明一实施例中，当电场积尘时，所述 进气电场装置检测电场电流，并通过以下任一方式进行灰尘清洁：
(1)当所述进气电场装置检测到电场电流增加到一个给定值，增高电场电压。
(2)当所述进气电场装置检测到电场电流增加到一个给定值，利用电场反电晕放电现象完成灰尘清洁。
(3)当所述进气电场装置检测到电场电流增加到一个给定值，利用电场反电晕放电现象，增高电场电压，限制入注电流，完成灰尘清洁。
(4)当所述进气电场装置检测到电场电流增加到一个给定值，利用电场反电晕放电现象，增高电场电压，限制入注电流，使发生在阳极积碳位置的急剧放电产生等离子，所述等离子使灰尘有机成分深度氧化，高分子键断裂，形成小分子二氧化碳和水，完成灰尘清洁。
电离电压
于本发明一实施例中进气除尘电场阳极和进气除尘电场阴极分别与电源的两个电极电性连接。加载在进气除尘电场阳极和进气除尘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进气电场装置的体积、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，积尘面积大于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进气除尘电场阳极由第一中空阳极管构成、并呈蜂窝状。第一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第一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，第一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进气电场装置包括第一电场级，该第一电场级包括若干个第一电场发生单元，第一电场发生单元可以有一个或多个。第一电场发生单元也称作第一集尘单元，第一集尘单元包括上述进气除尘电场阳极和进气除尘电场阴极，第一集尘单元有一个或多个。第一电场级有多个时，能有效提高进气电场装置的集尘效率。同一第一电场级中，各进气除尘电场阳极为相同极性，各进气除尘电场阴极为相同极性。且第一电场级有多个时，各第一电场级之间串联。于本发明一实施例中进气电场装置还包括若干个连接壳体，串联第一电场级通过连接壳体连接；相邻两级的第一电场级的距离大于极间距的1.4倍。
于本发明一实施例中用电场充电驻极体材料。进气电场装置有故障时，充电驻极体材料会用来除尘。
于本发明一实施例中，所述进气电场装置包括进气驻极体元件。
于本发明一实施例中，所述进气驻极体元件设于所述进气除尘电场阳极内。
于本发明一实施例中，所述进气除尘电场阳极和所述进气除尘电场阴极接通电源时形成进气电离除尘电场，所述进气驻极体元件在所述进气电离除尘电场中。
于本发明一实施例中，所述进气驻极体元件靠近进气电场装置出口，或者，所述进气驻极体元件设于进气电场装置出口。
于本发明一实施例中，所述进气除尘电场阳极和所述进气除尘电场阴极形成进气流道，所述进气驻极体元件设于所述进气流道中。
于本发明一实施例中，所述进气流道包括进气流道出口，所述进气驻极体元件靠近所述进气流道出口，或者，所述进气驻极体元件设于所述进气流道出口。
于本发明一实施例中，所述进气驻极体元件于所述进气流道中的横截面占进气流道横截面5％～100％。
于本发明一实施例中，所述进气驻极体元件于所述进气流道中的横截面占进气流道横截面10％-90％、20％-80％、或40％-60％。
于本发明一实施例中，所述进气电离除尘电场给所述进气驻极体元件充电。
于本发明一实施例中，所述进气驻极体元件具有多孔结构。
于本发明一实施例中，所述进气驻极体元件为织品。
于本发明一实施例中，所述进气除尘电场阳极内部为管状，所述进气驻极体元件外部为管状，所述进气驻极体元件外部套设于所述进气除尘电场阳极内部。
于本发明一实施例中，所述进气驻极体元件与所述进气除尘电场阳极为可拆卸式连接。
于本发明一实施例中，所述进气驻极体元件的材料包括具有驻极性能的无机化合物。所述驻极性能是指进气驻极体元件在外接电源充电后带有电荷，并在完全脱离电源的条件下，依然保持有一定的电荷，从而作为电极起到电场电极作用的能力。
于本发明一实施例中，所述无机化合物选自含氧化合物、含氮化合物或玻璃纤维中的一种或多种组合。
于本发明一实施例中，所述含氧化合物选自金属基氧化物、含氧复合物、含氧的无机杂多酸盐中的一种或多种组合。
于本发明一实施例中，所述金属基氧化物选自氧化铝、氧化锌、氧化锆、氧化钛、氧化钡、氧化钽、氧化硅、氧化铅、氧化锡中的一种或多种组合。
于本发明一实施例中，所述金属基氧化物为氧化铝。
于本发明一实施例中，所述含氧复合物选自钛锆复合氧化物或钛钡复合氧化物中的一种或多种组合。
于本发明一实施例中，所述含氧的无机杂多酸盐选自钛酸锆、锆钛酸铅或钛酸钡中的一种或多种组合。
于本发明一实施例中，所述含氮化合物为氮化硅。
于本发明一实施例中，所述进气驻极体元件的材料包括具有驻极性能的有机化合物。所述驻极性能是指进气驻极体元件在外接电源充电后带有电荷，并在完全脱离电源的条件下，依然保持有一定的电荷，从而作为电极起到电场电极作用的能力。
于本发明一实施例中，所述有机化合物选自氟聚合物、聚碳酸酯、PP、PE、PVC、天然蜡、树脂、松香中的一种或多种组合。
于本发明一实施例中，所述氟聚合物选自聚四氟乙烯(PTFE)、聚全氟乙丙烯(Teflon-FEP)、可溶性聚四氟乙烯(PFA)、聚偏氟乙烯(PVDF)中的一种或多种组合。
于本发明一实施例中，所述氟聚合物为聚四氟乙烯。
在上电驱动电压条件下产生进气电离除尘电场，利用进气电离除尘电场电离部分待处理物，吸附进气中的颗粒物，同时向进气驻极体元件进行充电，当进气电场装置出现故障时即无上电驱动电压时，充电的进气驻极体元件产生电场，利用充电的进气驻极体元件产生的电场吸附进气中的颗粒物，即在进气电离除尘电场出现故障情况下仍然可以进行颗粒物的吸附。
于本发明一实施例中，所述发动机进气除尘系统还包括除臭氧装置，用于去除或减少所述进气电场装置产生的臭氧，所述除臭氧装置在进气电场装置出口与进气除尘系统出口之间。
于本发明一实施例中，所述除臭氧装置包括臭氧消解器。
于本发明一实施例中，所述臭氧消解器选自紫外线臭氧消解器和催化臭氧消解器中的至少一种。
本发明发动机进气除尘系统还包括除臭氧装置，用于去除或减少所述进气电场装置产生的臭氧，由于空气中的氧气参与电离，形成臭氧，影响后续装置性能，如若臭氧进入发动机后，内部化学成分氧元素增多，分子量增大，由烃类化合物转变成非烃化合物，外现上颜色变深，沉淀增多，腐蚀性增大，使润滑油的使用性能下降，因此，所述发动机进气除尘系统还包括除臭氧装置，避免或减少后续装置性能的下降，如避免或减少发动机中润滑油使用性能的下降。
于本发明一实施例中，本发明提供一种进气除尘方法，包括以下步骤：
使含尘气体通过进气除尘电场阳极和进气除尘电场阴极产生的电离除尘电场；
电场积尘时，进行清尘处理。
于本发明一实施例中，当检测到的电场电流增加到一个给定值时，进行清尘处理。
于本发明一实施例中，当电场积尘时，通过以下任一方式进行灰尘清洁：
(1)利用电场反电晕放电现象完成清尘处理。
(2)利用电场反电晕放电现象，增高电压，限制入注电流，完成清尘处理。
(3)利用电场反电晕放电现象，增高电压，限制入注电流，使发生在阳极积尘位置的急剧放电产生等离子，所述等离子使灰尘有机成分深度氧化，高分子键断裂，形成小分子二氧化碳和水，完成清尘处理。
优选地，所述灰尘为炭黑。
于本发明一实施例中，所述进气除尘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积尘要求做调整。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进气除尘电场阳极的形状调整，例如，若进气除尘电场阳极的积尘面是平面，则阴极丝的截面呈圆形；若进气除尘电场阳极的积尘面是圆弧面，阴极丝需要设计成多面形。阴极丝的长度根据进气除尘电场阳极进行调整。
于本发明一实施例中，所述进气除尘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进气除尘电场阳极的形状进行调整，例如，若进气除尘电场阳极的积尘面是平面，则阴极棒的截面需要设计成圆形；若进气除尘电场阳极的积尘面是圆弧面，则阴极棒需要设计成多面形。
于本发明一实施例中，进气除尘电场阴极穿设于进气除尘电场阳极内。
于本发明一实施例中，进气除尘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进气除尘电场阳极。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，进气除尘电场阳极和进气除尘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，中空阳极管的管内切圆直径取值范围为5mm-400mm。
对于进气系统，于本发明一实施例中，本发明提供一种给进气加速的方法，包括以下步 骤：
使进气通过一个流道；
在流道中产生电场，所述电场不与所述流道垂直，所述电场包括进口和出口。
其中，所述电场电离所述气体。
于本发明一实施例中，所述电场包括第一阳极和第一阴极，所述第一阳极和第一阴极形成所述流道，所述流道接通所述进口和出口。所述第一阳极和第一阴极电离所述流道中的气体。
于本发明一实施例中，所述电场包括第二电极，所述第二电极设置在或靠近所述进口。
其中，所述第二电极为阴极，且作为所述第一阴极的延伸。优选地，所述第二电极与所述第一阳极具有夹角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，所述第二电极与所述第一阳极和第一阴极独立设置。
于本发明一实施例中，所述电场包括第三电极，所述第三电极设置在或靠近所述出口。
其中，所述第三电极为阳极，所述第三电极是所述第一阳极的延伸。优选地，所述第三电极与所述第一阴极具有夹角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，所述第三电极与所述第一阳极和第一阴极独立设置。
于本发明一实施例中，所述第一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积尘要求做调整。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第一阳极的形状调整，例如，若第一阳极的积尘面是平面，则阴极丝的截面呈圆形；若第一阳极的积尘面是圆弧面，阴极丝需要设计成多面形。阴极丝的长度根据第一阳极进行调整。
于本发明一实施例中，所述第一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第一阳极的形状进行调整，例如，若第一阳极的积尘面是平面，则阴极棒的截面需要设计成圆形；若第一阳极的积尘面是圆弧面，则阴极棒需要设计成多面形。
于本发明一实施例中，第一阴极穿设于第一阳极内。
于本发明一实施例中，第一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第一阳极。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，第一阳极和第一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，中空阳极管的管内切圆直径取值范围为5mm-400mm。
进气减少电场耦合方法
对于进气系统，于一实施例中，本发明提供一种减少进气除尘电场耦合的方法，包括以下步骤：
使进气通过进气除尘电场阳极和进气除尘电场阴极产生的电离除尘电场；
选择所述进气除尘电场阳极或/和进气除尘电场阴极。
于本发明一实施例中，选择的所述进气除尘电场阳极或/和进气除尘电场阴极尺寸使电场耦合次数≤3。
具体地，选择所述进气除尘电场阳极的集尘面积与进气除尘电场阴极的放电面积的比。优选地，选择所述进气除尘电场阳极的积尘面积与所述进气除尘电场阴极的放电面积的比为1.667：1-1680：1。
更为优选地，选择所述进气除尘电场阳极的积尘面积与所述进气除尘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，所述除尘电场阴极直径为1-3毫米，所述除尘电场阳极与所述除尘电场阴极的极间距为2.5-139.9毫米；所述除尘电场阳极的积尘面积与所述除尘电场阴极的放电面积的比为1.667：1-1680：1。
优选地，选择所述除尘电场阳极和所述除尘电场阴极的极间距小于150mm。
优选地，选择所述除尘电场阳极与所述除尘电场阴极的极间距为2.5～139.9mm。更为优选地，选择所述除尘电场阳极与所述除尘电场阴极的极间距为5.0～100mm。
优选地，选择所述进气除尘电场阳极长度为10～180mm。更为优选地，选择所述进气除尘电场阳极长度为60～180mm。
优选地，选择所述进气除尘电场阴极长度为30～180mm。更为优选地，选择所述进气除尘电场阴极长度为54～176mm。
于本发明一实施例中，所述进气除尘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积尘要求做调整。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进气除尘电场阳极的形状调整，例如，若进气除尘电场阳极的积尘面是平面，则阴极丝的截面呈圆形；若进气除尘电场阳极的积尘面是圆弧面，阴极丝需要设计成多面形。阴极丝的长度根据进气除尘电场阳极进行调整。
于本发明一实施例中，所述进气除尘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进气除尘电场阳极的形状进行调整，例如，若进气除尘电场阳极的积尘面是平面，则阴极棒的截面需要设计成圆形；若进气除尘电场阳极的积尘面是圆弧面，则阴极棒需要设计成多面形。
于本发明一实施例中，进气除尘电场阴极穿设于进气除尘电场阳极内。
于本发明一实施例中，进气除尘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进气除尘电场阳极。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，进气除尘电场阳极和进气除尘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，中空阳极管的管内切圆直径取值范围为5mm-400mm。
于一实施例中，本发明提供一种进气除尘的方法，包括如下步骤：
1)利用进气电离除尘电场吸附进气中的颗粒物；
2)利用进气电离除尘电场给进气驻极体元件充电。
于本发明一实施例中，所述进气驻极体元件靠近进气电场装置出口，或者，所述进气驻极体元件设于进气电场装置出口。
于本发明一实施例中，所述进气除尘电场阳极和所述进气除尘电场阴极形成进气流道，所述进气驻极体元件设于所述进气流道中。
于本发明一实施例中，所述进气流道包括进气流道出口，所述进气驻极体元件靠近所述 进气流道出口，或者，所述进气驻极体元件设于所述进气流道出口。
于本发明一实施例中，当进气电离除尘电场无上电驱动电压时，利用充电的进气驻极体元件吸附进气中的颗粒物。
于本发明一实施例中，在充电的进气驻极体元件吸附一定的进气中的颗粒物后，将其替换为新的进气驻极体元件。
于本发明一实施例中，替换为新的进气驻极体元件后重新启动进气电离除尘电场吸附进气中的颗粒物，并给新的进气驻极体元件充电。
于本发明一实施例中，所述进气驻极体元件的材料包括具有驻极性能的无机化合物。所述驻极性能是指进气驻极体元件在外接电源充电后带有电荷，并在完全脱离电源的条件下，依然保持有一定的电荷，从而作为电极起到电场电极作用的能力。
于本发明一实施例中，所述无机化合物选自含氧化合物、含氮化合物或玻璃纤维中的一种或多种组合。
于本发明一实施例中，所述含氧化合物选自金属基氧化物、含氧复合物、含氧的无机杂多酸盐中的一种或多种组合。
于本发明一实施例中，所述金属基氧化物选自氧化铝、氧化锌、氧化锆、氧化钛、氧化钡、氧化钽、氧化硅、氧化铅、氧化锡中的一种或多种组合。
于本发明一实施例中，所述金属基氧化物为氧化铝。
于本发明一实施例中，所述含氧复合物选自钛锆复合氧化物或钛钡复合氧化物中的一种或多种组合。
于本发明一实施例中，所述含氧的无机杂多酸盐选自钛酸锆、锆钛酸铅或钛酸钡中的一种或多种组合。
于本发明一实施例中，所述含氮化合物为氮化硅。
于本发明一实施例中，所述进气驻极体元件的材料包括具有驻极性能的有机化合物。所述驻极性能是指进气驻极体元件在外接电源充电后带有电荷，并在完全脱离电源的条件下，依然保持有一定的电荷，从而作为电极起到电场电极作用的能力。
于本发明一实施例中，所述有机化合物选自氟聚合物、聚碳酸酯、PP、PE、PVC、天然蜡、树脂、松香中的一种或多种组合。
于本发明一实施例中，所述氟聚合物选自聚四氟乙烯(PTFE)、聚全氟乙丙烯(Teflon-FEP)、可溶性聚四氟乙烯(PFA)、聚偏氟乙烯(PVDF)中的一种或多种组合。
于本发明一实施例中，所述氟聚合物为聚四氟乙烯。
于本发明一实施例中，本发明提供一种进气除尘方法，包括以下步骤：所述进气经进气电离除尘后去除或减少进气电离除尘产生的臭氧。
于本发明一实施例中，对进气电离除尘产生的臭氧进行臭氧消解。
于本发明一实施例中，所述臭氧消解选自紫外线消解和催化消解中的至少一种。
下面通过具体实施例来进一步阐述本发明的发动机进气除尘系统及方法。
实施例1
请参阅图1，显示为进气除尘系统于一实施例中的结构示意图。所述进气除尘系统101包括进气除尘系统入口1011、离心分离机构1012、第一滤水机构1013、进气电场装置1014、进气绝缘机构1015、进气均风装置、第二滤水机构1017和/或进气臭氧机构1018。
本发明中第一滤水机构1013和/或第二滤水机构1017是可选的，即本发明提供的进气除尘系统中可包括第一滤水机构1013和/或第二滤水机构1017，也可不包括第一滤水机构1013和/或第二滤水机构1017。
如图1所示，所述进气除尘系统入口1011设置于所述离心分离机构1012的进气壁上，以接收带有颗粒物的气体。
设置于所述进气除尘系统101下端的离心分离机构1012采用圆锥形筒。圆锥形筒与进气电场装置1014的衔接处为一排气口，所述排气口上设置有用于过滤颗粒物的第一过滤层。所述圆锥形筒的筒底设置有接收颗粒物的出粉口。
具体地，含颗粒物的气体一般以12-30m/s速度由进气除尘系统入口1011进入离心分离机构1012时，气体将由直线运动变为圆周运动。旋转气流的绝大部分，沿器壁自圆筒体呈螺旋形向下朝锥体流动。此外，颗粒物在离心力的作用下，被甩向分离机构的内壁，颗粒物一旦与内壁接触，靠内壁附近的向下轴向速度的动量沿壁面下落，由出粉口排出。旋转下降的外旋气流，在下降过程中不断向分离机构的中心部分流入，形成向心的径向气流，这部分气流就构成了旋转向上的内旋流。内、外旋流的旋转方向是相同的。最后净化气经排气口及第一过滤网(未予图示)排入所述进气电场装置1014，一部分未被分离下来的较细尘粒也未能逃逸。
设置于所述离心分离机构1012内的第一滤水机构1013包括设置于所述进气除尘系统入口1011的第一电极为一导电网板，所述导电网板用于在上电后，将电子传导给水。用于吸附带电的水的第二电极于本实施例中为所述进气电场装置1014的阳极积尘部，即除尘电场阳极10141。
请参阅图2，显示为设置于所述进气装置内的第一滤水机构的另一实施例结构图。所述 第一滤水机构1013的第一电极10131设置于所述进气口，所述第一电极10131为一带有负电势导电网板。同时，本实施例的第二电极10132设置于所述进气装置内呈面网状，且第二电极10132带有正电势，该第二电极10132也称作收集极。本实施例中第二电极10132具体呈平面网状，且第一电极10131平行于第二电极10132。本实施例中第一电极10131和第二电极10132之间形成网面电场。另外，第一电极10131由金属丝制成的网状结构，该第一电极10131由金属丝网构成。本实施例中第二电极10132的面积大于第一电极10131的面积。所述进气电场装置1014包括进气除尘电场阳极10141和设置于进气除尘电场阳极10141内的进气除尘电场阴极10142，进气除尘电场阳极10141与进气除尘电场阴极10142之间形成非对称静电场，其中，待含有颗粒物的气体通过所述排气口进入所述进气电场装置1014后，由于所述进气除尘电场阴极10142放电，电离所述气体，以使所述颗粒物获得负电荷，向所述进气除尘电场阳极10141移动，并沉积在所述进气除尘电场阳极10141上。
具体地，所述进气除尘电场阳极10141的内部由呈蜂窝状(如图19中所示的蜂窝状)、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。
所述进气除尘电场阴极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。
在本实施例中，所述进气除尘电场阴极10142的出气端低于所述进气除尘电场阳极10141的出气端，且所述进气除尘电场阴极10142的出气端与所述进气除尘电场阳极10141的进气端齐平，以使所述进气电场装置1014内部形成加速电场。
所述进气绝缘机构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。
如图1所示，于本发明一实施例中，进气除尘电场阴极10142安装在阴极支撑板10143上，阴极支撑板10143与进气除尘电场阳极10141通过进气绝缘机构1015相连接。所述进气绝缘机构1015用于实现所述阴极支撑板10143和所述进气除尘电场阳极10141之间的绝缘。于本发明一实施例中，进气除尘电场阳极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靠近进气电场装置入口，第二阳极部101411靠近进气电场装置出口。阴极支撑板和进气绝缘机构在第一阳极部101412和第二阳极部101411之间，即进气绝缘机构1015安装在进气电离电场中间、或进气除尘电场阴极10142中间，可以对进气除尘电场阴极10142起到良好的支撑作用，并对进气除尘电场阴极10142起到相对于进气除尘电场阳极10141的固定作用，使进气除尘电场阴极10142和进气除尘电场阳极10141之间保持设定的距离。
请参阅图3A、图3B及图3C，显示为进气均风装置的三种实施结构图。
如图3A所示，进气均风装置1016当所述进气除尘电场阳极的外型呈圆柱体时，所述进气均风装置1016位于所述进气除尘系统入口1011与所述进气除尘电场阳极10141和所述进气除尘电场阴极10142形成的进气电离除尘电场之间，且由若干围绕所述进气除尘系统入口1011中心旋转的均风叶片10161组成。所述进气均风装置能够使发动机在各种转速下变化的进气量均匀通过所述进气除尘电场阳极产生的电场。同时能够保持所述进气除尘电场阳极内部温度恒定，氧气充足。
如图3B所示，当所述进气除尘电场阳极的外型呈立方体时，所述进气均风装置1020包括：
设置于位于所述进气除尘电场阳极一侧边的进气管10201；及
设置于所述除尘电场阳极另一侧边的出气管10202；其中，安装进气管10201的侧边与安装出气管10202的另一侧边相对立。
如图3C所示，所述进气均风装置1026还可以包括设置于所述进气除尘电场阳极的进气端的第一文氏板均风机构1028和设置于所述进气除尘电场阳极的出气端的第二文氏板均风机构1030(如图7D所示的第二文氏板均风机构俯视图可以看出其呈折型)，所述第一文氏板均风机构上开设与进气孔，所述第二文氏板均风机构上开设有出气孔，所述进气孔与所述出气孔错位排布，且正面进气侧面出气，形成旋风结构。
在本实施例中，所述进气电场装置1014与所述第二滤水机构1017的衔接处设置第二过滤网用于过滤未经所述进气电场装置1014处理过的粒径较小的细颗粒。
设置于所述出气端处的第二滤水机构1017包括：第三过滤网、转轴及阻水球。
所述第三过滤网通过转轴倾斜式安装于所述出气端处，其中，所述第三过滤网与所述出气口对应的位置处安装有阻水球。待进入的气体推动所述第三过滤网绕转轴旋转，所述第三过滤网上形成水膜，所述阻水球堵住所述出气端，以防止水份冲出。
设置于所述进气装置出气端的所述进气臭氧机构1018采用除臭氧灯管。
实施例2
如图4所示的进气电场装置，包括进气除尘电场阳极10141、进气除尘电场阴极10142和进气驻极体元件205，所述进气除尘电场阳极10141和所述进气除尘电场阴极10142接通电源时形成进气电离除尘电场，所述进气驻极体元件205设于所述进气电离除尘电场中，图4中箭头方向为待处理物流动方向。所述进气驻极体元件设于进气电场装置出口。所述进气电离除尘电场给所述进气驻极体元件充电。所述进气驻极体元件具有多孔结构，所述进气驻 极体元件的材料为氧化铝。所述进气除尘电场阳极内部为管状，所述进气驻极体元件外部为管状，所述进气驻极体元件外部套设于所述进气除尘电场阳极内部。所述进气驻极体元件与所述进气除尘电场阳极为可拆卸式连接。
一种进气除尘的方法，包括如下步骤：
a)利用进气电离除尘电场吸附进气中的颗粒物；
b)利用进气电离除尘电场给进气驻极体元件充电。
其中，所述进气驻极体元件设于进气电场装置出口；所述进气驻极体元件的材料为氧化铝；当进气电离除尘电场无上电驱动电压时，利用充电的进气驻极体元件吸附进气中的颗粒物；在充电的进气驻极体元件吸附一定的进气中的颗粒物后，将其替换为新的进气驻极体元件；替换为新的进气驻极体元件后重新启动进气电离除尘电场吸附进气中的颗粒物，并给新的进气驻极体元件充电。
实施例3
如图5和图6所示的进气电场装置，包括进气除尘电场阳极10141、进气除尘电场阴极10142和进气驻极体元件205，所述进气除尘电场阳极10141和所述进气除尘电场阴极10142形成进气流道292，所述进气驻极体元件205设于所述进气流道292中，图5中箭头方向为待处理物流动方向。所述进气流道292包括进气流道出口，所述进气驻极体元件205靠近所述进气流道出口。所述进气驻极体元件于所述进气流道中的横截面占进气流道横截面10％，如图7所示，即为S2/(S1+S2)*100％，其中S2第一横截面面积为所述进气驻极体元件于所述进气流道中的横截面面积，S1第一横截面面积和S2第二横截面面积的和为进气流道横截面面积，S1第一横截面面积不包括进气除尘电场阴极10142的横截面面积。所述进气除尘电场阳极和所述进气除尘电场阴极接通电源时形成进气电离除尘电场。所述进气电离除尘电场给所述进气驻极体元件充电。所述进气驻极体元件具有多孔结构，所述进气驻极体元件的材料为聚四氟乙烯。所述进气除尘电场阳极内部为管状，所述进气驻极体元件外部为管状，所述进气驻极体元件外部套设于所述进气除尘电场阳极内部。所述进气驻极体元件与所述进气除尘电场阳极为可拆卸式连接。
于本发明一实施例中，一种进气除尘的方法包括如下步骤：
1)利用进气电离除尘电场吸附进气中的颗粒物；
2)利用进气电离除尘电场给进气驻极体元件充电。
其中，所述进气驻极体元件靠近所述进气流道出口；所述进气驻极体元件的材料为聚四氟乙烯；当进气电离除尘电场无上电驱动电压时，利用充电的进气驻极体元件吸附进气中的 颗粒物；在充电的进气驻极体元件吸附一定的进气中的颗粒物后，将其替换为新的进气驻极体元件；替换为新的进气驻极体元件后重新启动进气电离除尘电场吸附进气中的颗粒物，并给新的进气驻极体元件充电。
实施例4
如图8所示，所述发动机进气除尘系统包括进气电场装置和除臭氧装置206，所述进气电场装置包括括进气除尘电场阳极10141和进气除尘电场阴极10142，所述除臭氧装置用于去除或减少所述进气电场装置产生的臭氧，所述除臭氧装置在进气电场装置出口与进气除尘系统出口之间。所述进气除尘电场阳极10141和所述进气除尘电场阴极10142用于产生进气电离除尘电场。所述除臭氧装置206包括臭氧消解器，用于消解所述进气电场装置产生的臭氧，所述臭氧消解器为紫外线臭氧消解器，图中箭头方向为进气流动方向。
一种进气除尘方法，包括以下步骤：所述进气经进气电离除尘，然后对进气电离除尘产生的臭氧进行臭氧消解，所述臭氧消解为紫外线消解。
所述除臭氧装置用于去除或减少所述进气电场装置产生的臭氧，由于空气中的氧气参与电离，形成臭氧，影响后续装置性能，如若臭氧进入发动机后，内部化学成分氧元素增多，分子量增大，由烃类化合物转变成非烃化合物，外现上颜色变深，沉淀增多，腐蚀性增大，使润滑油的使用性能下降，因此，本发明发动机进气除尘系统还包括除臭氧装置，避免或减少后续装置性能的下降，如避免或减少发动机中润滑油使用性能的下降。
实施例5
本实施例中电场发生单元可应用于进气电场装置，如图9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9、图10和图11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。
减少电场耦合的方法，包括如下步骤：选择除尘电场阳极4051的集尘面积与除尘电场阴极4052的放电面积的比为6.67：1，除尘电场阳极4051和除尘电场阴极4052的极间距为9.9mm，除尘电场阳极4051长度为60mm，除尘电场阴极4052长度为54mm，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沿集尘极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＝118°，进而在除尘电场阳极4051和除尘电场阴极4052的作用下，能将更多的待处理物质收集起来，实现电场耦合次数≤3，能够减少电场对气溶胶、水雾、油雾、松散光滑颗粒物的耦合消耗，节省电场电能30～50％。
本实施例中进气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。如图12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。
本实施例中上述待处理物质可以是呈颗粒状的粉尘，也可以是其它需处理的杂质，如气溶胶、水雾、油雾等。
实施例6
本实施例中电场发生单元可应用于进气电场装置，如图9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。
减少电场耦合的方法，包括如下步骤：选择除尘电场阳极4051的集尘面积与除尘电场阴极4052的放电面积的比为1680：1，除尘电场阳极4051和除尘电场阴极4052的极间距为139.9mm，除尘电场阳极4051长度为180mm，除尘电场阴极4052长度为180mm，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沿集尘极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，进而在除尘电场阳极4051和除尘电场阴极4052的作用下，能将更多的待处理物质收集起来，实现电场耦合次数≤3，能够减少电场对气溶胶、水雾、油雾、松散光滑颗粒物的耦合消耗，节省电场电能20～40％。
本实施例中上述待处理物质可以是呈颗粒状的粉尘，也可以是其它需处理的杂质，如气溶胶、水雾、油雾等。
实施例7
本实施例中电场发生单元可应用于进气电场装置，如图9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。
减少电场耦合的方法，包括如下步骤：选择除尘电场阳极4051的集尘面积与除尘电场阴极4052的放电面积的比为1.667：1，除尘电场阳极4051和除尘电场阴极4052的极间距为2.4mm，除尘电场阳极4051长度为30mm，除尘电场阴极4052长度为30mm，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沿集尘极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，进而在除尘电场阳极4051和除尘电场阴极4052的作用下，能将更多的待处理物质收集起来，实现电场耦合次数≤3，能够减少电场对气溶胶、水雾、油雾、松散光滑颗粒物的耦合消耗，节省电场电能10～30％。
本实施例中上述待处理物质可以是呈颗粒状的粉尘，也可以是其它需处理的杂质，如气溶胶、水雾、油雾等。
实施例8
本实施例中电场发生单元可应用于进气电场装置，如图9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9、图10和图11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的集尘面积与除尘电场阴极4052的放电面积的比为6.67：1，所述除尘电场阳极4051和除尘电场阴极4052的极间距为9.9mm，除尘电场阳极4051长度为60mm，除尘电场阴极4052长度为54mm，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沿集尘极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＝118°，进而在除尘电场阳极4051和除尘电场阴极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，典型尾气颗粒pm0.23集尘效率为99.99％。
本实施例中进气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。如图12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。
本实施例中上述待处理物质可以是呈颗粒状的粉尘，也可以是其它需处理的杂质，如气溶胶、水雾、油雾等。
实施例9
本实施例中电场发生单元可应用于进气电场装置，如图9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的集尘面积与除尘电场阴极4052的放电面积的比为1680：1，所述除尘电场阳极4051和除尘电场阴极4052的极间距为139.9mm，除尘电场阳极4051长度为180mm，除尘电场阴极4052长度为180mm，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沿集尘极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，进而在除尘电场阳极4051和除尘电场阴极4052的作用下，能将更多的待处理物质收集起来，保证本电场装置的集尘效率更高，典型尾气颗粒pm0.23集尘效率为99.99％。
本实施例中进气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。
本实施例中上述待处理物质可以是呈颗粒状的粉尘，也可以是其它需处理的杂质，如气溶胶、水雾、油雾等。
实施例10
本实施例中电场发生单元可应用于进气电场装置，如图9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的集尘面积与除尘电场阴极4052的放电面积的比为1.667：1，所述除尘电场阳极4051和除尘电场阴极4052的极间距为2.4mm。除尘电场阳极4051长度为30mm，除尘电场阴极4052长度为30mm，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沿集尘极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，进而在除尘电场阳极4051和除尘电场阴极4052的作用下，能将更多的待处理物质收集起来，保证本电场装置的集尘效率更高，典型尾气颗粒pm0.23集尘效率为99.99％。
本实施例中除尘电场阳极4051及除尘电场阴极4052构成集尘单元，且该集尘单元有多个，以利用多个集尘单元有效提高本电场装置的集尘效率。
本实施例中上述待处理物质可以是呈颗粒状的粉尘，也可以是其它需处理的杂质，如气溶胶、水雾、油雾等。
实施例11
本实施例中发动机进气系统，包括上述实施例8、实施例9或实施例10中的电场装置。欲进入发动机的气体需先流经该电场装置，以利用该电场装置有效地将气体中的粉尘等待处理物质清除掉；随后，经处理后的气体再进入发动机，以保证进入发动机的气体更加干净，所含粉尘等杂质较少；进而保证发动机的工作效率更高，且发动机排放气体中所含污染物更少。该发动机进气系统也称作进气装置。
实施例12
本实施例中电场发生单元可应用于进气电场装置，如图9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沿集尘极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，而且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。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％。
本实施例中进气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。
本实施例中上述待处理物质可以是呈颗粒状的粉尘。
实施例13
本实施例中电场发生单元可应用于进气电场装置，如图9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沿集尘极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，而且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。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％。
本实施例中进气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。
本实施例中上述待处理物质可以是呈颗粒状的粉尘。
实施例14
本实施例中电场发生单元可应用于进气电场装置，如图9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沿集尘极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，而且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。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％。
本实施例中进气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。
本实施例中上述待处理物质可以是呈颗粒状的粉尘。
实施例15
本实施例中电场发生单元可应用于进气电场装置，如图9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9和图10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沿集尘极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，而且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。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％。
本实施例中进气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，各集尘极为相同极性，各放电极为相同极性。
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12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。
本实施例中上述待处理物质可以是呈颗粒状的粉尘。
实施例16
本实施例中发动机进气系统，包括上述实施例12、实施例13、实施例14或实施例15中的电场装置。欲进入发动机的气体需先流经该电场装置，以利用该电场装置有效地将气体中的粉尘等待处理物质清除掉；随后，经处理后的气体再进入发动机，以保证进入发动机的气体更加干净，所含粉尘等杂质较少；进而保证发动机的工作效率更高，且发动机排放气体中所含污染物更少。该发动机进气系统也称作进气装置。
实施例17
本实施例中电场装置可应用于进气系统，包括除尘电场阴极5081和除尘电场阳极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。本实施例中除尘电场阴极5081具有负电势，除尘电场阳极5082和辅助电极5083均具有正电势。
同时，如图13所示，本实施例中辅助电极5083与除尘电场阳极5082固接。在除尘电场阳极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与除尘电场阳极5082具有相同的正电势。
如图13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的长度方向可与除尘电场阳极5082的长度方向相同。
如图13所示，本实施例中除尘电场阳极5082呈管状，除尘电场阴极5081呈棒状，除尘电场阴极5081穿设在除尘电场阳极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与除尘电场阳极5082构成阳极管5084。阳极管5084的前端与除尘电场阴极5081齐平，阳极管5084的后端向后超出了除尘电场阴极5081的后端，该阳极管5084相比于除尘电场阴极5081向后超出的部分为上述辅助电极5083。即本实施例中除尘电场阳极5082和除尘电场阴极5081的长度相同，除尘电场阳极5082和除尘电场阴极5081在前后方向上位置相对；辅助电极5083位于除尘电场阳极5082和除尘电场阴极5081的后方。这样，辅助电极5083与除尘电场阴极5081之间形成辅助电场，该辅助电场给除尘电场阳极5082和除尘电场阴极5081之间带负电荷的氧离子流施加向后的力，使得除尘电场阳极5082和除尘电场阴极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阳极管5084，带负电荷的氧离子在向除尘电场阳极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，进而在除尘电场阳极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13所示，本实施例中阳极管5084的后端与除尘电场阴极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°。
本实施例中除尘电场阳极5082、辅助电极5083、及除尘电场阴极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。
本实施例中上述待处理物质可以是呈颗粒状的粉尘，也可以是其它需处理的杂质。
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。
本实施例中直流电源具体可为直流高压电源。上述除尘电场阴极5081和除尘电场阳极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，除尘电场阴极5081和除尘电场阳极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，形成除尘电场阳极5082和除尘电场阴极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。本实施例中上述电场装置也称作一种有加速方向电场装置。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％。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18
本实施例中电场装置可应用于进气系统，包括除尘电场阴极5081和除尘电场阳极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。本实施例中辅助电极5083和除尘电场阴极5081均具有负电势，除尘电场阳极5082具有正电势。
本实施例中辅助电极5083可与除尘电场阴极5081固接。这样，在实现除尘电场阴极5081与直流电源的阴极电性连接后，也实现了辅助电极5083与直流电源的阴极电性连接。同时，本实施例中辅助电极5083沿前后方向延伸。
本实施例中除尘电场阳极5082呈管状，除尘电场阴极5081呈棒状，除尘电场阴极5081穿设在除尘电场阳极5082中。同时本实施例中上述辅助电极5083也棒状，且辅助电极5083和除尘电场阴极5081构成阴极棒。该阴极棒的前端向前超出除尘电场阳极5082的前端，该阴极棒与除尘电场阳极5082相比向前超出的部分为上述辅助电极5083。即本实施例中除尘电场阳极5082和除尘电场阴极5081的长度相同，除尘电场阳极5082和除尘电场阴极5081在前后方向上位置相对；辅助电极5083位于除尘电场阳极5082和除尘电场阴极5081的前方。这样，辅助电极5083与除尘电场阳极5082之间形成辅助电场，该辅助电场给除尘电场阳极5082和除尘电场阴极5081之间带负电荷的氧离子流施加向后的力，使得除尘电场阳极5082和除尘电场阴极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管状的除尘电场阳极5082，带负电荷的氧离子在向除尘电场阳极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，进而在除尘电场阳极5082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。
本实施例中除尘电场阳极5082、辅助电极5083、及除尘电场阴极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。
本实施例中上述待处理物质可以是呈颗粒状的粉尘，也可以是其它需处理的杂质。
实施例19
如图14所示，本实施例中电场装置可应用于进气系统，辅助电极5083沿左右方向延伸。本实施例中辅助电极5083的长度方向与除尘电场阳极5082和除尘电场阴极5081的长度方向不同。且辅助电极5083具体可与除尘电场阳极5082相垂直。
本实施例中除尘电场阴极5081和除尘电场阳极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。本实施例中除尘电场阴极5081具有负电势，除尘电场阳极5082和辅助电极5083均具有正电势。
如图14所示，本实施例中除尘电场阴极5081和除尘电场阳极5082在前后方向上位置相对，辅助电极5083位于除尘电场阳极5082和除尘电场阴极5081的后方。这样，辅助电极5083与除尘电场阴极5081之间形成辅助电场，该辅助电场给除尘电场阳极5082和除尘电场阴极5081之间带负电荷的氧离子流施加向后的力，使得除尘电场阳极5082和除尘电场阴极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除尘电场阳极5082和除尘电场阴极5081之间的电场，带负电荷的氧离子在向除尘电场阳极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，进而在除尘电场阳极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20
如图15所示，本实施例中电场装置可应用于进气系统，辅助电极5083沿左右方向延伸。本实施例中辅助电极5083的长度方向与除尘电场阳极5082和除尘电场阴极5081的长度方向不同。且辅助电极5083具体可与除尘电场阴极5081相垂直。
本实施例中除尘电场阴极5081和除尘电场阳极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。本实施例中除尘电场阴极5081和辅助电极5083均具有负电势，除尘电场阳极5082具有正电势。
如图15所示，本实施例中除尘电场阴极5081和除尘电场阳极5082在前后方向上位置相对，辅助电极5083位于除尘电场阳极5082和除尘电场阴极5081的前方。这样，辅助电极 5083与除尘电场阳极5082之间形成辅助电场，该辅助电场给除尘电场阳极5082和除尘电场阴极5081之间带负电荷的氧离子流施加向后的力，使得除尘电场阳极5082和除尘电场阴极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除尘电场阳极5082和除尘电场阴极5081之间的电场，带负电荷的氧离子在向除尘电场阳极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，进而在除尘电场阳极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21
本实施例中发动机进气装置，包括上述实施例17、18、19、或20中的电场装置。欲进入发动机的气体需先流经该电场装置，以利用该电场装置有效地将气体中的粉尘等待处理物质清除掉；随后，经处理后的气体再进入发动机，以保证进入发动机的气体更加干净，所含粉尘等杂质较少；进而保证发动机的工作效率更高，且发动机排放气体中所含污染物更少。本实施例中发动机进气装置也简称进气装置，电场装置也称作进气电场装置，除尘电场阴极5081也称作进气除尘电场阴极，除尘电场阳极5082也称作进气除尘电场阳极。
实施例22(进气前置电极)
如图16所示，本实施例提供一种进气电场装置，包括依次相通的进气电场装置入口3085、进气流道3086、电场流道3087、及进气电场装置出口3088，进气流道3086中安装有进气前置电极3083，进气前置电极3083的截面面积与进气流道3086的截面面积比为99％～10％，进气电场装置还包括进气除尘电场阴极3081和进气除尘电场阳极3082，电场流道3087位于进气除尘电场阴极3081和进气除尘电场阳极3082之间。本发明进气电场装置的工作原理为：含污染物的气体通过进气电场装置入口3085进入进气流道3086，安装在进气流道3086中的进气前置电极3083将电子传导给部分污染物，部分污染物带电，当污染物由进气流道3086进入电场流道3087后，进气除尘电场阳极3082给已带电的污染物施加吸引力，带电的污染物向进气除尘电场阳极3082移动，直至该部分污染物附着在进气除尘电场阳极3082上，同时，电场流道3087中进气除尘电场阴极3081和进气除尘电场阳极3082之间形成进气电离除尘电场，该进气电离除尘电场将使另一部分未带电的污染物带电，这样另一部分污染物在带电后同样会受到进气除尘电场阳极3082施加的吸引力，并最终附着在进气除尘电场阳极3082，从而利用上述进气电场装置使污染物带电效率更高，带电更充分，进而保证进气除尘电场阳 极3082能收集更多的污染物，并保证本发明进气电场装置对污染物的收集效率更高。
进气前置电极3083的截面面积是指进气前置电极3083沿截面上实体部分的面积之和。另外，进气前置电极3083的截面面积与进气流道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16所示，本实施例中进气前置电极3083和进气除尘电场阴极3081均与直流电源的阴极电性连接，进气除尘电场阳极3082与直流电源的阳极电性连接。本实施例中进气前置电极3083和进气除尘电场阴极3081均具有负电势，进气除尘电场阳极3082具有正电势。
如图16所示，本实施例中进气前置电极3083具体可呈网状。这样，当气体流经进气流道3086时，利用进气前置电极3083呈网状的结构特点，便于气体及污染物流过进气前置电极3083，并使气体中污染物与进气前置电极3083接触更加充分，从而使进气前置电极3083能将电子传导给更多的污染物，并使污染物的带电效率更高。
如图16所示，本实施例中进气除尘电场阳极3082呈管状，进气除尘电场阴极3081呈棒状，进气除尘电场阴极3081穿设在进气除尘电场阳极3082中。本实施例中进气除尘电场阳极3082和进气除尘电场阴极3081呈非对称结构。当气体流入进气除尘电场阴极3081和进气除尘电场阳极3082之间形的电离电场将使污染物带电，且在进气除尘电场阳极3082施加的吸引力作用下，将带电的污染物收集在进气除尘电场阳极3082的内壁上。
另外，如图16所示，本实施例中进气除尘电场阳极3082和进气除尘电场阴极3081均沿前后方向延伸，进气除尘电场阳极3082的前端沿前后方向上位于进气除尘电场阴极3081的前端的前方。且如图16所示，进气除尘电场阳极3082的后端沿前后方向上位于进气除尘电场阴极3081的后端的后方。本实施例中进气除尘电场阳极3082沿前后方向上的长度更长，使得位于进气除尘电场阳极3082内壁上的吸附面面积更大，从而对带有负电势的污染物的吸引力更大，并能收集更多的污染物。
如图16所示，本实施例中进气除尘电场阴极3081和进气除尘电场阳极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污染物，并使得本进气电场装置对污染物的收集能力更强，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。本实施例中进气电场装置，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：当气体通过进气电场装置入口3085流入进气流道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进气前置电极3083相接触时，或与进气前置电极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，进气除尘电场阳极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，进气除尘电场阳极3082与进气除尘电场阴极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，进气除尘电场阳极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，并使得本进气电场装置所能收集物质的种类更广泛，且收集能力更强。
本实施例中上述进气除尘电场阴极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。进气前置电极3083和进气除尘电场阳极3082之间通入直流高压，形成导电回路；进气除尘电场阴极3081和进气除尘电场阳极3082之间通入直流高压，形成电离放电电晕电场。本实施例中进气前置电极3083为密集分布的导体。当容易带电的粉尘经过进气前置电极3083时，进气前置电极3083直接将电子给粉尘，粉尘带电，随后被异极的进气除尘电场阳极3082吸附；同时未带电的粉尘经过进气除尘电场阴极3081和进气除尘电场阳极3082形成的电离区，电离区形成的电离氧会把电子荷电给粉尘，这样粉尘继续带电，并被异极的进气除尘电场阳极3082吸附。
本实施例中进气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，可利用进气除尘电场阴极3081和进气除尘电场阳极3082之间形成的电离放电电晕电场，电离氧，来使污染物荷电，再利用进气除尘电场阳极3082收集污染物；而在气体中氧气含量过低、或无氧状态、或污染物为导电尘雾等时，利用进气前置电极3083直接使污染物上电，让污染物充分带电后被进气除尘电场阳极3082吸附。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。
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 (11)

  1. 一种发动机进气除尘系统，其特征在于：包括进气除尘系统入口、进气除尘系统出口、进气电场装置；所述进气电场装置包括进气电场装置入口、进气电场装置出口、进气除尘电场阴极和进气除尘电场阳极，所述进气除尘电场阴极和所述进气除尘电场阳极用于产生进气电离除尘电场；所述进气电场装置还包括辅助电场单元，所述进气电离除尘电场包括流道，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。
  2. 根据权利要求1所述的发动机进气除尘系统，其特征在于，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进气电离除尘电场的进口。
  3. 根据权利要求2所述的发动机进气除尘系统，其特征在于，所述第一电极为阴极。
  4. 根据权利要求2或3所述的发动机进气除尘系统，其特征在于，所述辅助电场单元的第一电极是所述进气除尘电场阴极的延伸。
  5. 根据权利要求4所述的发动机进气除尘系统，其特征在于，所述辅助电场单元的第一电极与所述进气除尘电场阳极具有夹角α，且0°＜α≤125°、或45°≤α≤125°、或60°≤α≤100°、或α＝90°。
  6. 根据权利要求1至5任一项所述的发动机进气除尘系统，其特征在于，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进气电离除尘电场的出口。
  7. 根据权利要求6所述的发动机进气除尘系统，其特征在于，所述第二电极为阳极。
  8. 根据权利要求6或7所述的发动机进气除尘系统，其特征在于，所述辅助电场单元的第二电极是所述进气除尘电场阳极的延伸。
  9. 根据权利要求8所述的发动机进气除尘系统，其特征在于，所述辅助电场单元的第二电极与所述进气除尘电场阴极具有夹角α，且0°＜α≤125°、或45°≤α≤125°、或60°≤α≤100°、或α＝90°。
  10. 根据权利要求1至3、6和7任一项所述的发动机进气除尘系统，其特征在于，所述辅助电场的电极与所述进气电离除尘电场的电极独立设置。
  11. 根据权利要求1至10任一项所述的发动机进气除尘系统，其特征在于，还包括发动机。
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Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20220250087A1 (en) * 2018-10-22 2022-08-11 Shanghai Bixiufu Enterprise Management Co., Ltd. Engine exhaust dust removing system and method
WO2020083131A1 (zh) * 2018-10-22 2020-04-30 上海必修福企业管理有限公司 一种发动机进气除尘系统及方法
WO2020238978A1 (zh) * 2019-05-27 2020-12-03 上海必修福企业管理有限公司 一种电场装置及减少电场耦合方法
CN112774387B (zh) * 2021-01-21 2022-07-12 福建龙净环保股份有限公司 一种电袋复合除尘器
CN113500077B (zh) * 2021-05-28 2022-09-02 义乌市诚胜市政工程有限公司 一种封闭除尘节约水资源的除尘墙
CN113230808B (zh) * 2021-06-03 2022-02-01 濮阳职业技术学院 一种土木工程用道路粉尘吸收装置
CN114226012B (zh) * 2021-11-01 2022-11-25 陈宁 一种建筑工程检测用无尘碎石装置
CN114535240A (zh) * 2022-01-05 2022-05-27 月漪 一种用于新型高性能纤维制品生产中使用的除尘设备
CN116764436A (zh) * 2023-06-26 2023-09-19 浙江大维高新技术股份有限公司 一种水泥窑烟气处理设备和处理工艺

Citations (7)

* 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
CN2770787Y (zh) * 2004-11-29 2006-04-12 张辛石 双荷电横向集尘极板滤尘器
CN102072055A (zh) * 2010-05-28 2011-05-25 宁波市镇海华泰电器厂 机动车进气除尘装置
US20110229376A1 (en) * 2010-03-17 2011-09-22 Isaac Ray Electrostatic filter and non-thermal plasma system for air pollution control of hydrocarbon combustion engines
CN102619653A (zh) * 2012-02-08 2012-08-01 宁波市镇海华泰电器厂 兼有节油功能的道路pm2.5清除装置
CN204018023U (zh) * 2014-06-17 2014-12-17 北京光耀环境工程有限公司 一种电除尘器高效集尘与清灰装置
CN105149093A (zh) * 2015-10-29 2015-12-16 许玉蕊 三电极箱式电极电除尘装置

Family Cites Families (205)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1393712A (en) * 1918-11-04 1921-10-11 Frank W Steere Process and means for removing suspended matter from gas
US2555216A (en) * 1946-09-24 1951-05-29 Research Corp Electrical precipitator
US2608266A (en) * 1946-09-24 1952-08-26 Research Corp Gas flow control for electrical precipitators and the like
US2563297A (en) * 1947-11-24 1951-08-07 Research Corp Electrical precipitator, including an electrode washing device
US3205160A (en) * 1961-10-19 1965-09-07 Petrolite Corp Electric treater for dispersions
DE1288077B (zh) * 1965-07-09
DE2134576C3 (de) * 1971-07-10 1975-10-30 Metallgesellschaft Ag, 6000 Frankfurt Röhre n-NaBelektroabscheider
US3747299A (en) * 1972-02-04 1973-07-24 Kuan Chiang Ta Electrostatic precipitator
CS178566B1 (en) * 1974-11-14 1979-05-15 Jan Skalny Method and device for continuous concentration lowering of polycyclic aromatic hydrocarbons in gas-flow
JPS52157651U (zh) * 1976-05-25 1977-11-30
JPS58501162A (ja) * 1981-07-24 1983-07-21 トル−ス　ロドニイ　ジヨン 静電集塵器の逆コロナを検出し適用する方法
DE3141156A1 (de) * 1981-10-16 1983-04-28 Robert Bosch Gmbh, 7000 Stuttgart Verfahren und vorrichtung zum entfernen von festen bestandteilen und aerosolen, insbesondere von russbestandteilen aus dem abgas von brennkraftmaschinen
US4853005A (en) * 1985-10-09 1989-08-01 American Filtrona Corporation Electrically stimulated filter method and apparatus
US4969328A (en) * 1986-10-21 1990-11-13 Kammel Refaat A Diesel engine exhaust oxidizer
US5003774A (en) * 1987-10-09 1991-04-02 Kerr-Mcgee Chemical Corporation Apparatus for soot removal from exhaust gas
EP0379760A1 (en) * 1989-01-26 1990-08-01 Univerzita Komenskeho Device for continuously reducing concentration of carbon monoxide and other harmful types of emission
JPH04122367A (ja) * 1990-09-14 1992-04-22 Matsushita Electric Ind Co Ltd 空気清浄器
US5403383A (en) * 1992-08-26 1995-04-04 Jaisinghani; Rajan Safe ionizing field electrically enhanced filter and process for safely ionizing a field of an electrically enhanced filter
US5395430A (en) * 1993-02-11 1995-03-07 Wet Electrostatic Technology, Inc. Electrostatic precipitator assembly
CN2158507Y (zh) * 1993-04-10 1994-03-09 杭州环境净化设备厂 室内空气清净器
JPH06343898A (ja) * 1993-06-03 1994-12-20 Sumitomo Heavy Ind Ltd 電気集塵機用回路
US5549735C1 (en) * 1994-06-09 2001-08-14 Coppom Technologies Electrostatic fibrous filter
US5591253A (en) * 1995-03-07 1997-01-07 Electric Power Research Institute, Inc. Electrostatically enhanced separator (EES)
CN1138501A (zh) * 1995-06-20 1996-12-25 张明义 高效电子空气净化装置
JP3020872U (ja) * 1995-07-24 1996-02-06 一也 早川 静電式空気清浄装置
JP3526494B2 (ja) * 1995-09-30 2004-05-17 日本バイリーン株式会社 荷電式エアーフィルター装置
JP2698804B2 (ja) * 1995-10-24 1998-01-19 株式会社オーデン 電気的制御によるディーゼルエンジンの排気微粒子捕集装置
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
SE512593C2 (sv) * 1997-05-06 2000-04-10 Blue Air Ab Förfarande och anordning för rening av ett gasformigt medium
TW337731U (en) * 1997-12-29 1998-08-01 yong-xiang Lin Improved structure of an air cleaner
JP2000070627A (ja) * 1998-06-19 2000-03-07 Ebara Corp 異種膜材組み合わせエアフィルタ
DE19833226C1 (de) * 1998-07-23 2000-04-20 Steuler Industriewerke Gmbh Niederschlagsrohrbündel für Naßelektrofilter
US6156098A (en) * 1999-02-10 2000-12-05 Richards; Clyde N. Charged droplet gas scrubber apparatus and method
DE19946283C1 (de) * 1999-07-31 2000-09-28 Metallgesellschaft Ag Erdleiter für Erdungsanlagen
JP2001179127A (ja) * 1999-12-27 2001-07-03 Daikin Ind Ltd 電気集塵装置
JP3729403B2 (ja) * 2001-05-02 2005-12-21 ミドリ安全株式会社 樹脂電極及びそれを用いた静電式集塵装置
CN1332341A (zh) * 2001-07-06 2002-01-23 俞其进 空气净化机
WO2003095095A1 (en) * 2002-05-09 2003-11-20 Ohio University Membrane laminar wet electrostatic precipitator
FR2841484B1 (fr) * 2002-06-26 2004-09-10 Boucq De Beaudignies Ghisla Le Dispositif et procede de filtration de l'air et des gaz avec regeneration des particules captees
US6773489B2 (en) * 2002-08-21 2004-08-10 John P. Dunn Grid type electrostatic separator/collector and method of using same
US20090071328A1 (en) * 2002-08-21 2009-03-19 Dunn John P Grid type electrostatic separator/collector and method of using same
US7585352B2 (en) * 2002-08-21 2009-09-08 Dunn John P Grid electrostatic precipitator/filter for diesel engine exhaust removal
US6878192B2 (en) * 2002-12-09 2005-04-12 Ohio University Electrostatic sieving precipitator
US7514047B2 (en) * 2003-01-15 2009-04-07 Toyota Jidosha Kabushiki Kaisha Exhaust gas purifying apparatus
US6790259B2 (en) * 2003-01-16 2004-09-14 Blueair Ab Method and device for cleaning a gaseous fluid using a conductive grid between charging head and filter
JP4304238B2 (ja) * 2003-03-27 2009-07-29 いすゞ自動車株式会社 内燃機関の排気ガス浄化方法及びその装置
JP2004351310A (ja) * 2003-05-29 2004-12-16 Matsushita Electric Ind Co Ltd 空気浄化装置
JP2004360512A (ja) * 2003-06-03 2004-12-24 Hino Motors Ltd 排気浄化装置
US7025806B2 (en) * 2003-11-25 2006-04-11 Stri{dot over (o)}nAir, Inc. Electrically enhanced air filtration with improved efficacy
CN2770786Y (zh) * 2004-03-04 2006-04-12 何保海 电除尘器辅助电极
CN100418637C (zh) * 2004-06-10 2008-09-17 中钢集团天澄环保科技股份有限公司 泛比电阻电除尘器及除尘方法
JP4292511B2 (ja) * 2004-06-21 2009-07-08 トヨタ自動車株式会社 排ガス浄化装置
US7258729B1 (en) * 2004-08-04 2007-08-21 Air Ion Devices Inc. Electronic bi-polar electrostatic air cleaner
ATE548546T1 (de) * 2004-12-17 2012-03-15 Usui Kokusai Sangyo Kk Elektrisches behandlungsverfahren für abgas eines dieselmotors und vorrichtung dafür
JP2006281135A (ja) * 2005-04-01 2006-10-19 Denso Corp 集塵装置
FR2903726B1 (fr) * 2006-07-12 2008-10-10 Renault Sas Dispositif et procede pour la capture et l'elimination des particules contenues dans les gaz d'echappement d'un moteur a combustion interne de vehicule automobile.
JP4287873B2 (ja) * 2006-08-31 2009-07-01 日立アプライアンス株式会社 空気調和機
US7815720B2 (en) * 2006-12-27 2010-10-19 Strionair, Inc. Dual-filter electrically enhanced air-filtration apparatus and method
CN201006047Y (zh) * 2007-03-30 2008-01-16 黄樟焱 多功能旋风式等离子空气处理机
TWM345972U (en) * 2008-02-22 2008-12-01 shi-zhen Lai Dust-collecting device for exhaust pipe and chimney
CN101269813B (zh) * 2008-04-15 2012-01-04 北京民海艳科技有限公司 微硅粉提纯回收工艺
CN101274304B (zh) * 2008-05-07 2010-11-03 浙江大学 烟气多种污染物协同脱除复合静电除尘器
US7883558B2 (en) * 2008-05-07 2011-02-08 United Technologies Corporation Electrostatic particulate separation for emission treatment systems
CN101347760B (zh) * 2008-08-29 2011-04-27 江苏中科节能环保技术有限公司 一种卧式电除尘器
WO2010134448A1 (ja) * 2009-05-19 2010-11-25 国立大学法人宇都宮大学 粒子状物質燃焼装置及び方法
JP2011003457A (ja) * 2009-06-19 2011-01-06 Tokyo Electron Ltd 荷電粒子選別装置及び荷電粒子照射装置
TWM372446U (en) * 2009-07-28 2010-01-11 Taiwan Chuan Jing Technology Co Ltd Air cleaner device with cation and anion
DE102009041092A1 (de) * 2009-09-14 2011-03-24 Emitec Gesellschaft Für Emissionstechnologie Mbh Abgasbehandlungsvorrichtung mit zwei Wabenkörpern zur Erzeugung eines elektrischen Potentials
DE102009041091A1 (de) * 2009-09-14 2011-03-24 Emitec Gesellschaft Für Emissionstechnologie Mbh Vorrichtung zur Behandlung von Rußpartikel enthaltendem Abgas
CN201751006U (zh) * 2010-05-10 2011-02-23 杨莺 静电除尘专用高频电源控制器
CN101936202A (zh) * 2010-08-20 2011-01-05 陶显芳 一种汽车尾气电子净化装置
US20120103184A1 (en) * 2010-11-02 2012-05-03 Clarkson University Electrostatic filtration system
JP5693287B2 (ja) * 2011-02-21 2015-04-01 富士電機株式会社 電気集塵装置
US8894745B2 (en) * 2011-08-10 2014-11-25 John P. Dunn Vane electrostatic precipitator
US9238230B2 (en) * 2011-08-10 2016-01-19 John P. Dunn Vane electrostatic precipitator
US9039815B2 (en) * 2011-08-10 2015-05-26 John P. Dunn Vane electrostatic precipitator
US9073062B2 (en) * 2011-08-10 2015-07-07 John P. Dunn Vane electrostatic precipitator
CN202290305U (zh) * 2011-11-07 2012-07-04 福建省华澳环保科技有限公司 高效静电除尘器
EP2599556B1 (en) * 2011-11-29 2021-06-30 General Electric Technology GmbH A method for cleaning an electrostatic precipitator
CN202621286U (zh) * 2012-04-05 2012-12-26 营口中润环境科技有限公司 立板式湿法静电除尘器
CN202606276U (zh) * 2012-04-12 2012-12-19 孙茂华 利用材料驻极体特性集尘的空气净化装置
CN102974461B (zh) * 2012-04-12 2015-09-02 孙茂华 利用材料驻极体特性集尘的空气净化装置和空气净化方法
CN202683348U (zh) * 2012-04-18 2013-01-23 北京博鹏北科科技有限公司 电除尘器
CN102896044B (zh) * 2012-10-26 2015-02-18 易敏红 静电除尘器
CN104226477A (zh) * 2013-06-18 2014-12-24 珠海格力电器股份有限公司 空气净化器及其净化方法
CN103316766A (zh) * 2013-06-27 2013-09-25 江苏中兴化工设备有限公司 静电捕集器
CN204275723U (zh) * 2013-11-15 2015-04-22 北京科之建环保工程有限公司 一种用于烟气综合处理装置的静电除尘器
CN203525527U (zh) * 2013-11-15 2014-04-09 北京智成科技有限公司 一种除尘除雾脱硫脱硝脱汞烟气综合处理装置
CN203525551U (zh) * 2013-11-15 2014-04-09 北京智成科技有限公司 一种用于烟气综合处理装置的静电除尘器
TWM476903U (en) * 2013-11-26 2014-04-21 Asia Ipam Co Ltd Improvements in air blower and filter assemblies
CN103752408A (zh) * 2014-01-24 2014-04-30 清华大学 空中净化装置
CN103817007B (zh) * 2014-03-05 2016-05-18 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
CN103817005A (zh) * 2014-03-06 2014-05-28 宜兴市化工成套设备有限公司 一种板管竖流湿式高效静电除尘器
CN203737400U (zh) * 2014-03-06 2014-07-30 双盾环境科技有限公司 一种板管竖流湿式高效静电除尘器
CN103925065B (zh) * 2014-04-04 2016-04-20 武汉杜曼智能科技有限公司 自动除尘发动机热管理控制驱动器、控制方法及系统
CN103990544A (zh) * 2014-05-07 2014-08-20 杭州玺清环保科技有限公司 一种电场收尘装置
CN203886670U (zh) * 2014-05-21 2014-10-22 国电环境保护研究院 电除尘器阴极线自张紧固定装置
CN203899750U (zh) * 2014-05-27 2014-10-29 华北电力大学（保定） 一种复合式除尘器
CN104056720B (zh) * 2014-05-27 2017-10-10 华北电力大学（保定） 一种复合式除尘器
CN105221218A (zh) * 2014-06-26 2016-01-06 王绍坤 水层、静电分离式汽车尾气净化器
DE112015004322T5 (de) * 2014-10-16 2017-08-17 Ohio University Nass-Elektrofilter und Verfahren zur Abgasbehandlung
CN204227628U (zh) * 2014-10-24 2015-03-25 刘慧根 一体式静电除尘新风机
CN104437868A (zh) * 2014-11-11 2015-03-25 中国科学院过程工程研究所 一种横向极板绕流式湿式电除尘装置及湿式电除尘方法
JP6126068B2 (ja) * 2014-12-02 2017-05-10 トヨタ自動車株式会社 排ガス浄化装置
CN204593621U (zh) * 2015-01-27 2015-08-26 温州市骐邦环保科技有限公司 带除臭氧功能的空气净化装置
CN105983486B (zh) * 2015-01-28 2018-11-20 上海思奈环保科技有限公司 一种空气净化高压离子驻极体净化装置及空气净化装置
CN204816887U (zh) * 2015-01-28 2015-12-02 上海思奈环保科技有限公司 一种空气净化高压离子驻极体净化装置及空气净化装置
KR101651034B1 (ko) * 2015-02-02 2016-08-24 원효식 전기집진기 및 그 전기집진기를 포함하는 공기청정 시스템
TWM507273U (zh) * 2015-02-11 2015-08-21 Shanghai Cangqiong Environment Technology Co Ltd 高壓高頻圓管針極除菌除塵裝置
CN104689918A (zh) * 2015-03-23 2015-06-10 中冶赛迪工程技术股份有限公司 一种湿式电除尘器
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
CN104785369B (zh) * 2015-04-07 2017-12-26 东莞市三叠环保科技有限公司 负离子沉降及高压静电吸附双效空气除尘净化器
CN105268268B (zh) * 2015-04-21 2017-03-15 四川展祥特种合金科技有限公司 一种立式组合高效脱硫脱氨除尘装置
CN204678558U (zh) * 2015-05-20 2015-09-30 董坤 一种静电喷雾新风净化装置
JP6290824B2 (ja) * 2015-05-22 2018-03-07 トヨタ自動車株式会社 排気浄化装置
CN204769149U (zh) * 2015-05-30 2015-11-18 山东国舜建设集团有限公司 湿式电除尘器电场阴极模块式固定装置
CN104841560B (zh) * 2015-05-30 2016-08-17 山东国舜建设集团有限公司 湿式电除尘器电场阴极模块式固定装置
CN104971823B (zh) * 2015-06-16 2018-04-13 东莞市长资实业有限公司 一种便于清洗的空气集尘设备及具有该设备的空气净化器
CN204866199U (zh) * 2015-06-16 2015-12-16 东莞市长资实业有限公司 一种便于清洗的空气集尘设备及具有该设备的空气净化器
CN104959236A (zh) * 2015-06-30 2015-10-07 国电环境保护研究院 湿式静电除尘器阴极与阳极配置结构
CN105080715B (zh) * 2015-08-07 2017-04-19 浙江大学 采用颗粒冲刷清灰的线管式高温静电除尘装置及清灰方法
CN204996568U (zh) * 2015-08-07 2016-01-27 浙江大学 一种采用颗粒冲刷清灰的线管式高温静电除尘装置
CN204911793U (zh) * 2015-08-27 2015-12-30 东方电气集团东方锅炉股份有限公司 一种湿式静电除尘器设备
CN205079356U (zh) * 2015-09-21 2016-03-09 新疆霭励志环保科技有限公司 对称轴向电离净尘装置
CN205199731U (zh) * 2015-10-19 2016-05-04 常州大学 一种覆铜介质阻挡电极和光触媒耦合静电除尘装置
CN105312155A (zh) * 2015-10-19 2016-02-10 常州大学 覆铜介质阻挡电极和光触媒耦合静电除尘装置
CN205191760U (zh) * 2015-11-02 2016-04-27 北京福兆朗风科技有限公司 利用静电驻极体绝缘材料为载体的强电场技术除尘新风机
CN105233611A (zh) * 2015-11-05 2016-01-13 周翠华 电场与电晕联用的光催化空气净化器
CN205164956U (zh) * 2015-11-19 2016-04-20 北京聚易蓝天环保科技有限公司 均流式静电除尘器
CN105233987A (zh) * 2015-11-19 2016-01-13 北京聚易蓝天环保科技有限公司 均流式静电除尘器
CN105505478B (zh) * 2015-11-30 2018-04-10 中国科学院广州能源研究所 一种电旋风流光电晕生物质气化粗燃气净化装置与方法
CN105312154B (zh) * 2015-12-07 2017-10-24 福建龙净环保股份有限公司 一种湿式电除尘器
CN105413869A (zh) * 2015-12-07 2016-03-23 北京国能中电节能环保技术有限责任公司 一种立齿湿式电除尘器中的阴极线
CN205550987U (zh) * 2015-12-08 2016-09-07 重庆本创机械有限公司 一种发动机曲轴表面除尘装置
US20170165680A1 (en) * 2015-12-09 2017-06-15 Michael Johnson Electrostatic media filter
CN205341044U (zh) * 2015-12-18 2016-06-29 河北宁泊环保有限公司 湿雾静电除尘器
JP6447486B2 (ja) * 2015-12-22 2019-01-09 株式会社デンソー 放電制御装置、ガス供給装置及び放電制御方法
WO2017114049A1 (zh) * 2015-12-31 2017-07-06 靳瑞廷 气体介质悬浮颗粒物净化系统
CN105536421B (zh) * 2016-03-09 2017-06-30 山东蓝博环保设备有限公司 湿式静电除尘器
CN105750081A (zh) * 2016-03-09 2016-07-13 徐�明 一种喷淋式高效静电除尘器
CN205412573U (zh) * 2016-03-09 2016-08-03 山东蓝博环保设备有限公司 湿式静电除尘器
CN205591991U (zh) * 2016-03-28 2016-09-21 北京汽车股份有限公司 车辆排气管以及具有其的车辆
CN205627552U (zh) * 2016-04-09 2016-10-12 嘉兴天盾环保科技有限公司 一种高通量紧凑型电晕离子发生器
CN205587151U (zh) * 2016-04-15 2016-09-21 湖北强达环保科技股份有限公司 一种高效静电除尘器
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
CN205667904U (zh) * 2016-05-09 2016-11-02 李爱云 一种管式静电除尘器
CN105920919B (zh) * 2016-05-17 2018-07-10 华南理工大学 一种用于净化pm2.5的超疏水驻极体滤材的制备及活化方法
CN105944838B (zh) * 2016-06-30 2018-07-06 广东佳德环保科技有限公司 湿式电除尘器用钛电极电离管
CN205995620U (zh) * 2016-06-30 2017-03-08 河北安维环境工程有限公司 湿式电除雾装置
CN105921275A (zh) * 2016-06-30 2016-09-07 河北安维环境工程有限公司 湿式电除雾装置
CN206310664U (zh) * 2016-07-07 2017-07-07 格林韦尔（北京）科技发展有限公司 新风空气净化系统
US10828646B2 (en) * 2016-07-18 2020-11-10 Agentis Air Llc Electrostatic air filter
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
CN205966185U (zh) * 2016-08-10 2017-02-22 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
CN206008346U (zh) * 2016-08-31 2017-03-15 四川好时吉化工有限公司 一种用于制备复合水溶肥料的除尘器
CN206082846U (zh) * 2016-09-08 2017-04-12 佛山市科蓝环保科技股份有限公司 一种蜂巢电场结构
CN106492987B (zh) * 2016-11-15 2018-01-09 江门市科蓝环保设备有限公司 一种静电除尘器
CN106733198B (zh) * 2016-11-21 2018-08-21 深圳深亚能环保科技有限公司 一种具有自动清理功能的电场装置
CN106621661A (zh) * 2016-12-08 2017-05-10 中冶节能环保有限责任公司 一种对钢渣辊轧区含尘蒸汽进行超净排放处理的工艺方法和装置
CN206414910U (zh) * 2016-12-08 2017-08-18 中冶节能环保有限责任公司 一种对钢渣辊轧区含尘蒸汽进行超净排放处理的装置
CN106492988A (zh) * 2016-12-23 2017-03-15 福建省沃特宝环保科技有限公司 一种微通道阳极除水雾装置
CN206391818U (zh) * 2017-01-17 2017-08-11 天津市舒泰医疗器械有限公司 一种色谱仪尾气处理装置
KR101923446B1 (ko) * 2017-02-02 2018-11-30 한국철도기술연구원 미세먼지 집진시스템
CN106907215A (zh) * 2017-02-27 2017-06-30 上海必修福企业管理有限公司 一种处理发动机排放尾气的装置和方法
CN107029882A (zh) * 2017-03-23 2017-08-11 复旦大学 大面积电晕等离子体空气净化器
CN106733194B (zh) * 2017-03-31 2018-10-16 广东美的厨房电器制造有限公司 静电装置和油烟机
CN106964489A (zh) * 2017-05-13 2017-07-21 深圳天美净朗环保科技有限公司 一种静电除尘的方法及装置
CN206793910U (zh) * 2017-05-15 2017-12-26 江苏瑞洁环境工程科技有限责任公司 一种灰水自清理的湿式电除尘器
CN107051731B (zh) * 2017-05-22 2018-07-17 广东美的厨房电器制造有限公司 电极针板、静电装置和油烟机
CN107152332A (zh) * 2017-06-16 2017-09-12 苏州博菡环保科技有限公司 汽车尾气净化器
TWM549659U (zh) * 2017-08-03 2017-10-01 Xin-Xiong Fang 具自動關機功能之靜電集塵機控制裝置
CN207287767U (zh) * 2017-08-10 2018-05-01 环球国合（北京）低碳环保科技有限公司 一种电磁清灰式离子风电除尘
CN107442278A (zh) * 2017-08-10 2017-12-08 环球国合（北京）低碳环保科技有限公司 板网收尘电极式电除尘
CN207287768U (zh) * 2017-08-10 2018-05-01 环球国合（北京）低碳环保科技有限公司 网板箱收尘电极式电除尘
CN107497603A (zh) * 2017-08-10 2017-12-22 环球国合（北京）低碳环保科技有限公司 一种复合式电除尘
CN207287763U (zh) * 2017-08-10 2018-05-01 环球国合（北京）低碳环保科技有限公司 一种复合式电子风除尘
CN207287760U (zh) * 2017-08-10 2018-05-01 环球国合（北京）低碳环保科技有限公司 一种高效离子风式电除尘
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
CN108067354A (zh) * 2017-08-10 2018-05-25 莱芜万通电器有限公司 一种综合式静电除尘器
CN207013155U (zh) * 2017-09-01 2018-02-16 无锡幸运环保设备有限公司 带有拉瓦尔喷嘴的新型静电除尘器
CN107377225A (zh) * 2017-09-06 2017-11-24 维睿空气系统产品（深圳）有限公司 微静电净化装置
CN107737670A (zh) * 2017-09-11 2018-02-27 广东美的制冷设备有限公司 静电除尘模块及空气调节装置
CN107716113B (zh) * 2017-10-31 2023-10-20 珠海格力电器股份有限公司 一种集尘净化结构及除尘机
CN107569913A (zh) * 2017-11-02 2018-01-12 无锡风正科技有限公司 一种新型驻极体滤材及其制备方法
TWM556634U (zh) * 2017-11-02 2018-03-11 Lu Wen Yu 除塵系統
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
CN107965863A (zh) * 2017-11-10 2018-04-27 苏州甫腾智能科技有限公司 一种便携式空气净化装置
CN207786180U (zh) * 2017-11-10 2018-08-31 苏州甫腾智能科技有限公司 一种便携式空气净化装置
CN107930851A (zh) * 2017-11-23 2018-04-20 北京东方计量测试研究所 一种静电除尘装置
CN107842933B (zh) * 2017-12-07 2023-06-16 北京化工大学 一种基于微分毛刷摩擦起电原理的高效静电除尘装置
CN207815524U (zh) * 2017-12-26 2018-09-04 北京华钛高科科技有限公司 一种具有除臭氧功能的空气净化器
CN207929001U (zh) * 2017-12-27 2018-10-02 福建龙净环保股份有限公司 一种scr烟气脱硝装置
CN207907455U (zh) * 2018-01-26 2018-09-25 北京华清凯尔空气净化技术有限公司 一种风管、空气净化器及其集尘装置
CN207521163U (zh) * 2018-01-31 2018-06-22 北京华清凯尔空气净化技术有限公司 集尘装置及空气净化器
CN108201783A (zh) * 2018-02-01 2018-06-26 广州广大气治理工程有限公司 一种锅炉烟气多种污染物深度治理装置、系统及方法
CN108405184B (zh) * 2018-02-06 2020-05-26 常州大学 一种工业废气细颗粒物脱除装置
CN108480050B (zh) * 2018-02-09 2020-12-04 北京东方计量测试研究所 驻极体材料及静电除尘装置
CN108465297A (zh) * 2018-03-09 2018-08-31 欧阳业东 一种用于空气净化的超疏水驻极体滤材的制备方法
CN207941622U (zh) * 2018-03-19 2018-10-09 瀚沃环境技术(上海)有限公司 油烟异味净化处理设备
CN207887337U (zh) * 2018-05-05 2018-09-21 杨晓丽 一种智能化工业用焊锡烟气净化处理设备
CN208282274U (zh) * 2018-05-11 2018-12-25 澄迈中等职业技术学校 一种集净化消毒一体化的空气净化装置
CN113366198B (zh) * 2018-10-22 2023-08-15 上海必修福企业管理有限公司 一种发动机排放处理系统和方法
US20220250087A1 (en) * 2018-10-22 2022-08-11 Shanghai Bixiufu Enterprise Management Co., Ltd. Engine exhaust dust removing system and method
WO2020083097A1 (zh) * 2018-10-22 2020-04-30 上海必修福企业管理有限公司 一种发动机排放处理系统和方法
WO2020083131A1 (zh) * 2018-10-22 2020-04-30 上海必修福企业管理有限公司 一种发动机进气除尘系统及方法

Patent Citations (7)

* 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
CN2770787Y (zh) * 2004-11-29 2006-04-12 张辛石 双荷电横向集尘极板滤尘器
US20110229376A1 (en) * 2010-03-17 2011-09-22 Isaac Ray Electrostatic filter and non-thermal plasma system for air pollution control of hydrocarbon combustion engines
CN102072055A (zh) * 2010-05-28 2011-05-25 宁波市镇海华泰电器厂 机动车进气除尘装置
CN102619653A (zh) * 2012-02-08 2012-08-01 宁波市镇海华泰电器厂 兼有节油功能的道路pm2.5清除装置
CN204018023U (zh) * 2014-06-17 2014-12-17 北京光耀环境工程有限公司 一种电除尘器高效集尘与清灰装置
CN105149093A (zh) * 2015-10-29 2015-12-16 许玉蕊 三电极箱式电极电除尘装置

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