CN113423506B - Air dust removal system and method - Google Patents
Air dust removal system and method Download PDFInfo
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- CN113423506B CN113423506B CN201980069644.7A CN201980069644A CN113423506B CN 113423506 B CN113423506 B CN 113423506B CN 201980069644 A CN201980069644 A CN 201980069644A CN 113423506 B CN113423506 B CN 113423506B
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- electric field
- dust
- anode
- cathode
- dust removal
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Classifications
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- 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
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- 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
- Y02A50/2351—Atmospheric particulate matter [PM], e.g. carbon smoke microparticles, smog, aerosol particles, dust
Abstract
An air dust removal system (101) and method includes a dust removal system inlet, a dust removal system outlet, and an electric field device (1014). The electric field device (1014) comprises an electric field device inlet (1011), an electric field device outlet, a dust removal electric field cathode (10142) and a dust removal electric field anode (10141), the dust removal electric field cathode (10142) and the dust removal electric field anode (10141) being for generating an ionisation dust removal electric field. The dedusting electric field anode (10141) comprises a first anode part (101412) and a second anode part (101411), the first anode part (101412) is close to an inlet of the electric field device (1014), the second anode part (101411) is close to an outlet of the electric field device (1014), and at least one insulation mechanism (1015) is arranged between the first anode part (101412) and the second anode part (101411). Which can effectively remove particulate matters in the air.
Description
Technical Field
The invention belongs to the field of air purification, and relates to an air dust removal system and method.
Background
The air is covered on the surface of the earth in a layering way, is transparent, colorless and odorless, mainly consists of nitrogen and oxygen, and has important influence on the survival and production of human beings. Along with the continuous improvement of the living standard of people, people gradually recognize the importance of air quality. In the prior art, air is usually dedusted by a filter screen or the like. However, the dust removal effect is unstable, the energy consumption is high, and secondary pollution is easy to cause.
Disclosure of Invention
In view of the above-mentioned drawbacks of the prior art, an object of the present invention is to provide an air dust removing system and method for solving the problem that the prior art cannot effectively remove air dust. The invention creatively uses the ionization dust removal method to remove dust from the air, the method has no pressure difference, no resistance to the air, wide variety of the pollutants in the collected air, stronger dust removal capability and higher dust removal efficiency.
To achieve the above and other related objects, the present invention provides the following examples:
1. example 1 provided by the present invention: an air dust removal system comprises a dust removal system inlet, a dust removal system outlet and an electric field device.
2. Example 2 provided by the present invention: including example 1 above, wherein the electric field device includes an electric field device inlet, an electric field device outlet, a dust removal electric field cathode, and a dust removal electric field anode, the dust removal electric field cathode and the dust removal electric field anode being for generating an ionizing dust removal electric field.
3. Example 3 provided by the present invention: including the above example 2, wherein the dust removing electric field anode includes a first anode portion and a second anode portion, the first anode portion is adjacent to the electric field device inlet, the second anode portion is adjacent to the electric field device outlet, and at least one cathode support plate is disposed between the first anode portion and the second anode portion.
4. Example 4 provided by the present invention: including example 3 above, wherein the electric field device further includes an insulation mechanism for achieving insulation between the cathode support plate and the dust removing electric field anode.
5. Example 5 provided by the present invention: the above example 4 is included, wherein an electric field flow path is formed between the dust-removing electric field anode and the dust-removing electric field cathode, and the insulating mechanism is disposed outside the electric field flow path.
6. Example 6 provided by the present invention: including the above example 4 or 5, wherein the insulating mechanism includes an insulating portion and a heat insulating portion; the insulating part is made of ceramic material or glass material.
7. Example 7 provided by the present invention: the above example 6 was included, wherein the insulating portion was an umbrella-shaped string ceramic pillar, an umbrella-shaped string glass pillar, a columnar string ceramic pillar, or a columnar glass pillar, and glaze was applied inside and outside the umbrella or inside and outside the pillar.
8. Example 8 provided by the present invention: including example 7 above, wherein the distance between the outer edge of the umbrella-shaped string ceramic pillar or umbrella-shaped string glass pillar and the dust-removing electric field anode is greater than 1.4 times the electric field distance, the sum of the umbrella bead distances of the umbrella-shaped string ceramic pillar or umbrella-shaped string glass pillar is greater than 1.4 times the insulation distance of the umbrella-shaped string ceramic pillar or umbrella-shaped string glass pillar, and the inner depth of the umbrella bead of the umbrella-shaped string ceramic pillar or umbrella-shaped string glass pillar is greater than 1.4 times the insulation distance of the umbrella-shaped string ceramic pillar or umbrella-shaped string glass pillar.
9. 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, 1/4 to 1/3, 1/3 to 1/2, 1/2 to 2/3, 2/3 to 3/4, or 3/4 to 9/10 of the length of the dust removing electric field anode.
10. Example 10 provided by the present invention: including any one of examples 3 to 9 above, wherein a 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.
11. Example 11 provided by the present invention: including any of the above examples 3 to 10, wherein the second anode portion includes a dust accumulation section and a reserved dust accumulation section.
12. Example 12 provided by the present invention: including any of examples 2 to 11 above, wherein the dust removing electric field cathode includes at least one electrode rod.
13. Example 13 provided by the present invention: including example 12 above, wherein the diameter of the electrode rod is no greater than 3mm.
14. Example 14 provided by the present invention: examples 12 or 13 above are included, wherein the electrode rod has a needle shape, a polygonal shape, a burr shape, a screw rod shape, or a columnar shape.
15. Example 15 provided by the present invention: including any of examples 2 to 14 above, wherein the dust removing electric field anode is comprised of a hollow tube bundle.
16. Example 16 provided by the present invention: including example 15 above, wherein the hollow cross-section of the dust removing electric field anode tube bundle is circular or polygonal.
17. Example 17 provided by the present invention: including example 16 above, wherein the polygon is a hexagon.
18. Example 18 provided by the present invention: the tube bundle comprising any of examples 14 to 17 above, wherein the dust removing electric field anode is honeycomb shaped.
19. Example 19 provided by the present invention: including any of examples 2-18 above, wherein the de-dusting electric field cathode is perforated within the de-dusting electric field anode.
20. Example 20 provided by the present invention: including any of examples 2 to 19 above, wherein the electric field device performs dust cleaning when the electric field dust is deposited to a certain extent.
21. Example 21 provided by the present invention: including example 20 above, wherein the electric field device detects the electric field current to determine if dust is deposited to a certain extent, dust cleaning is required.
22. Example 22 provided by the present invention: including examples 20 or 21 above, wherein the electric field device utilizes an increased electric field voltage for dust cleaning.
23. Example 23 provided by the present invention: including examples 20 or 21 above, wherein the electric field device utilizes an electric field back corona discharge phenomenon for dust cleaning.
24. Example 24 provided by the present invention: including examples 20 and 21 above, wherein the electric field device uses an electric field back corona discharge phenomenon to increase an electric field voltage and limit an injection current to perform dust cleaning treatment.
25. Example 25 provided by the present invention: including the above examples 20 or 21, wherein the electric field device uses an electric field back corona discharge phenomenon to increase an electric field voltage, limit an injection current, and cause a rapid discharge occurring at a carbon deposition position of an anode to generate plasma which deeply oxidizes an organic component of dust, breaks a polymer bond, and forms small molecular carbon dioxide and water to perform dust cleaning treatment.
26. Example 26 provided by the present invention: including any one of examples 2 to 25 above, wherein the electric field device further includes an auxiliary electric field unit for generating an auxiliary electric field that is non-parallel to the ionised dust removal electric field.
27. Example 27 provided by the present invention: including any one of examples 2 to 25 above, wherein the electric field device further includes an auxiliary electric field unit, the ionised dust removal electric field including a flow channel, the auxiliary electric field unit being for generating an auxiliary electric field that is non-perpendicular to the flow channel.
28. Example 28 provided by the present invention: including examples 26 or 27 above, wherein the auxiliary electric field unit comprises a first electrode disposed at or near an inlet of the ionised dust removal electric field.
29. Example 29 provided by the present invention: including example 28 above, wherein the first electrode is a cathode.
30. Example 30 provided by the present invention: including examples 28 or 29 above, wherein the first electrode of the auxiliary electric field unit is an extension of the dedusting electric field cathode.
31. Example 31 provided by the present invention: including the above example 30, wherein the first electrode of the auxiliary electric field unit has an angle α with the dust-removing electric field anode, and 0 ° < α.ltoreq.125 °, or 45 ° - α.ltoreq.125 °, or 60 ° - α.ltoreq.100 °, or α=90°.
32. Example 32 provided by the present invention: including any of the above examples 26 to 31, wherein the auxiliary electric field unit includes a second electrode disposed at or near an outlet of the ionised dust removal electric field.
33. Example 33 provided by the present invention: including example 32 above, wherein the second electrode is an anode.
34. Example 34 provided by the present invention: including examples 32 or 33 above, wherein the second electrode of the auxiliary electric field unit is an extension of the dedusting electric field anode.
35. Example 35 provided by the present invention: including the above example 34, wherein the second electrode of the auxiliary electric field unit has an angle α with the dust-removing electric field cathode, and 0 ° < α.ltoreq.125 °, or 45 ° - α.ltoreq.125 °, or 60 ° - α.ltoreq.100 °, or α=90°.
36. Example 36 provided by the present invention: including any of the above examples 26 to 29, 32 and 33, wherein the electrode of the auxiliary electric field is disposed independently of the electrode of the ionised dust removal electric field.
37. Example 37 provided by the present invention: including any one of the above examples 2 to 36, wherein a ratio of a dust accumulation area of the dust removal electric field anode to a discharge area of the dust removal electric field cathode is 1.667:1-1680:1.
38. example 38 provided by the present invention: including any one of the above examples 2 to 36, wherein a ratio of a dust accumulation area of the dust removal electric field anode to a discharge area of the dust removal electric field cathode is 6.67:1-56.67:1.
39. example 39 provided by the present invention: including any one of the above examples 2 to 38, wherein the dust-removal electric field cathode has a diameter of 1 to 3 millimeters, and the dust-removal electric field anode has a pole spacing from the dust-removal electric field cathode of 2.5 to 139.9 millimeters; the ratio of the dust accumulation area of the dust removal electric field anode to the discharge area of the dust removal electric field cathode is 1.667:1-1680:1.
40. example 40 provided by the present invention: including any of examples 2 to 38 above, wherein the distance between the dust removing electric field anode and the dust removing electric field cathode is less than 150mm.
41. Example 41 provided by the present invention: including any of the above examples 2 to 38, wherein the dust removing electric field anode and the dust removing electric field cathode have a pole spacing of 2.5-139.9mm.
42. Example 42 provided by the present invention: including any of examples 2 to 38 above, wherein the dust removing electric field anode and the dust removing electric field cathode have a pole spacing of 5-100mm.
43. Example 43 provided by the present invention: including any one of examples 2 to 42 above, wherein the dust removing electric field anode has a length of 10 to 180mm.
44. Example 44 provided by the present invention: including any one of examples 2 to 42 above, wherein the dust removing electric field anode has a length of 60 to 180mm.
45. Example 45 provided by the present invention: including any one of examples 2 to 44 above, wherein the dust removing electric field cathode has a length of 30 to 180mm.
46. Example 46 provided by the present invention: including any of examples 2 to 44 above, wherein the dust removing electric field cathode has a length of 54 to 176mm.
47. Example 47 provided by the present invention: including any of examples 26 to 46 above, wherein the ionized dust removing electric field has a number of couplings of less than or equal to 3 when operating.
48. Example 48 provided by the present invention: including any one of the above examples 2 to 46, wherein a ratio of a dust accumulation area of the dust removal electric field anode to a discharge area of the dust removal electric field cathode, a pole spacing between the dust removal electric field anode and the dust removal electric field cathode, a length of the dust removal electric field anode, and a length of the dust removal electric field cathode are such that a number of coupling times of the ionization dust removal electric field is equal to or less than 3.
49. Example 49 provided by the present invention: including any one of examples 2 to 48 above, wherein the ionization dust removing electric field voltage has a value ranging from 1kv to 50kv.
50. Example 50 provided by the present invention: including any of examples 2 to 49 above, wherein the electric field device further comprises a number of connection housings through which the series electric field stages are connected.
51. Example 51 provided by the present invention: including example 50 described above, wherein the distance of adjacent electric field levels is greater than 1.4 times the pole pitch.
52. Example 52 provided by the present invention: including any one of examples 2 to 51 above, wherein the electric field device further includes a pre-electrode between the electric field device inlet and an ionizing dust removal electric field formed by the dust removal electric field anode and the dust removal electric field cathode.
53. Example 53 provided by the present invention: including the above example 52, wherein the pre-electrode is in a dot, line, mesh, kong Banzhuang, plate, needle, balloon, box, tube, natural form of matter, or processed form of matter.
54. Example 54 provided by the present invention: including examples 52 or 53 above, wherein the pre-electrode is provided with a through hole.
55. Example 55 provided by the present invention: including example 54 above, wherein the through holes are polygonal, circular, oval, square, rectangular, trapezoidal, or diamond-shaped.
56. Example 56 provided by the present invention: examples 54 or 55 above are included, wherein the size of the through hole is 0.1-3 mm.
57. Example 57 provided by the present invention: including any of the examples 52 to 56 above, wherein the pre-electrode is a solid, a liquid, a gaseous cluster, or a combination of one or more forms of plasma.
58. Example 58 provided by the present invention: including any of examples 52 to 57 above, wherein the pre-electrode is a conductive mixed state substance, a living body naturally mixes a conductive substance, or an object is manually processed to form a conductive substance.
59. Example 59 provided by the present invention: including any of examples 52 to 58 above, wherein the front electrode is 304 steel or graphite.
60. Example 60 provided by the present invention: including any of examples 52 to 58 above, wherein the pre-electrode is an ion-containing conductive liquid.
61. Example 61 provided by the present invention: including any of the above examples 52 to 60, wherein, in operation, the pre-electrode charges contaminants in the air before the contaminated air enters the ionised dust field formed by the dust field cathode, the dust field anode and the contaminated air passes through the pre-electrode.
62. Example 62 provided by the present invention: including example 61 above, wherein when contaminant-laden air enters the ionization dust field, the dust field anode applies an attractive force to the charged contaminant, causing the contaminant to move toward the dust field anode until the contaminant adheres to the dust field anode.
63. Example 63 provided by the present invention: examples 61 or 62 above are included wherein the pre-electrode directs electrons into the contaminant, which transfer between the contaminant between the pre-electrode and the dedusting electric field anode, charging more of the contaminant.
64. Example 64 provided by the present invention: including any of examples 61 to 63 above, wherein electrons are conducted between the front electrode and the dust removing electric field anode by contaminants and an electric current is formed.
65. Example 65 provided by the present invention: including any of examples 61 to 64 above, wherein the pre-electrode charges the contaminant by contacting the contaminant.
66. Example 66 provided by the present invention: including any of examples 61 to 65 above, wherein the pre-electrode charges the contaminant by way of energy fluctuations.
67. Example 67 provided by the present invention: including any one of examples 61 to 66 above, wherein the pre-electrode is provided with a through hole.
68. Example 68 provided by the present invention: including any one of examples 52 to 67 above, wherein the front electrode is linear and the dust removing electric field anode is planar.
69. Example 69 provided by the present invention: including any of the above examples 52 to 68, wherein the front electrode is perpendicular to the dusting electric field anode.
70. Example 70 provided by the present invention: including any of the above examples 52 to 69, wherein the pre-electrode is parallel to the de-dusting electric field anode.
71. Example 71 provided by the present invention: including any one of examples 51 to 69 above, wherein the front electrode is curved or arcuate.
72. Example 72 provided by the present invention: including any of the above examples 52 to 71, wherein the pre-electrode is a wire mesh.
73. Example 73 provided by the present invention: including any of the above examples 52 to 72, wherein a voltage between the front electrode and the de-dusting electric field anode is different from a voltage between the de-dusting electric field cathode and the de-dusting electric field anode.
74. Example 74 provided by the present invention: including any of the above examples 52 to 73, wherein a voltage between the front electrode and the dust removing electric field anode is less than an onset corona onset voltage.
75. Example 75 provided by the present invention: including any of the above examples 52 to 74, wherein the voltage between the front electrode and the dust removing electric field anode is 0.1kv-2kv/mm.
76. Example 76 provided by the present invention: including any of the above examples 52 to 75, wherein the electric field device includes a flow channel in which the pre-electrode is located; the ratio of the cross-sectional area of the front electrode to the cross-sectional area of the flow channel is 99% -10%, or 90% -10%, or 80% -20%, or 70% -30%, or 60% -40%, or 50%.
77. Example 77 provided by the present invention: including any of examples 2 to 76 above, wherein the electric field device comprises an electret element.
78. Example 78 provided by the present invention: including example 77 above, wherein the electret element is in the ionizing dust removal electric field when the dust removal electric field anode and the dust removal electric field cathode are powered on.
79. Example 79 provided by the present invention: including examples 77 or 78 above, wherein the electret element is proximate to the electric field device outlet or the electret element is disposed at the electric field device outlet.
80. Example 80 provided by the present invention: including any of the above examples 78-79, wherein the de-dusting electric field anode and the de-dusting electric field cathode form a flow channel in which the electret element is disposed.
81. Example 81 provided by the present invention: including the example 80 described above, wherein the flow channel includes a flow channel outlet, the electret element is proximate to the flow channel outlet, or the electret element is disposed at the flow channel outlet.
82. Example 82 provided by the present invention: examples 80 or 81 above are included wherein the electret element has a cross section in the flow channel that is 5% to 100% of the flow channel cross section.
83. Example 83 provided by the present invention: including the example 82 described above, wherein the electret element has a cross-section in the flow channel that is 10% -90%, 20% -80%, or 40% -60% of the flow channel cross-section.
84. Example 84 provided by the present invention: including any of examples 77 to 83 above, wherein the ionizing dust removal electric field charges the electret element.
85. Example 85 provided by the present invention: including any of examples 77 to 84 above, wherein the electret element has a porous structure.
86. Example 86 provided by the present invention: including any of examples 77 to 85 above, wherein the electret element is a web.
87. Example 87 provided by the present invention: including any of the above examples 77-86, wherein the dust field anode is tubular inside, the electret element is tubular outside, and the electret element is externally sleeved inside the dust field anode.
88. Example 88 provided by the present invention: including any of examples 77 to 87 above, wherein the electret element is detachably connected to the dusting electric field anode.
89. Example 89 provided by the present invention: the material comprising any of examples 77 to 88 above, wherein the electret element material comprises an inorganic compound having electret properties.
90. Example 90 provided by the present invention: including example 89 above, wherein the inorganic compound is selected from one or more of an oxygen-containing compound, a nitrogen-containing compound, or a combination of glass fibers.
91. Example 91 provided by the present invention: including the above example 90, wherein the oxygen-containing compound is selected from one or more combinations of metal-based oxides, oxygen-containing complexes, oxygen-containing inorganic heteropolyacid salts.
92. Example 92 provided by the present invention: including example 91 above, wherein the metal-based oxide is selected from one or more of aluminum oxide, zinc oxide, zirconium oxide, titanium oxide, barium oxide, tantalum oxide, silicon oxide, lead oxide, tin oxide, and combinations thereof.
93. Example 93 provided by the present invention: including example 91 above, wherein the metal-based oxide is aluminum oxide.
94. Example 94 provided by the present invention: including example 91 above, wherein the oxygen-containing compound is selected from one or more combinations of titanium zirconium composite oxide or titanium barium composite oxide.
95. Example 95 provided by the present invention: including example 91 above, wherein the oxygen-containing inorganic heteropolyacid salt is selected from one or more combinations of zirconium titanate, lead zirconate titanate, or barium titanate.
96. Example 96 provided by the present invention: including example 90 above, wherein the nitrogen-containing compound is silicon nitride.
97. Example 97 provided by the present invention: the material comprising any of examples 77 to 96 above, wherein the electret element material comprises an organic compound having electret properties.
98. Example 98 provided by the present invention: including example 97 above, wherein the organic compound is selected from one or more of fluoropolymers, polycarbonates, PP, PE, PVC, natural waxes, resins, rosins.
99. Example 99 provided by the present invention: including example 98 above, wherein the fluoropolymer is selected from one or more of polytetrafluoroethylene, polyperfluoroethylene propylene, soluble polytetrafluoroethylene, polyvinylidene fluoride.
100. Example 100 provided by the present invention: including example 98 above, wherein the fluoropolymer is polytetrafluoroethylene.
101. Example 101 provided by the present invention: including any of the above examples 1 to 100, wherein the wind balancing device is further included.
102. Example 102 provided by the present invention: including the above example 101, wherein the wind-homogenizing device is between the dust removal system inlet and an ionization dust removal electric field formed by the dust removal electric field anode and the dust removal electric field cathode, when the dust removal electric field anode is tetragonal, the wind-homogenizing device includes: the air inlet pipe is arranged at one side of the dust removal electric field anode, and the air outlet pipe is arranged at the other side of the dust removal electric field anode; wherein, the intake pipe is opposite with the outlet duct.
103. Example 103 provided by the present invention: the example 101 includes the above, where the wind-homogenizing device is between the dust-removing system inlet and an ionization dust-removing electric field formed by the dust-removing electric field anode and the dust-removing electric field cathode, and when the dust-removing electric field anode is a cylinder, the wind-homogenizing device is composed of a plurality of rotatable wind-homogenizing blades.
104. Example 104 provided by the present invention: including above-mentioned example 101, wherein, equal wind device first venturi board equal wind mechanism with set up in the equal wind mechanism of second venturi board of the end of giving vent to anger of dust removal electric field positive pole, the inlet port has been seted up on the equal wind mechanism of first venturi board, the outlet port has been seted up on the equal wind mechanism of second venturi board, the inlet port with the outlet port dislocation is arranged, and the front side of admitting air is given vent to anger, forms cyclone.
105. Example 105 provided by the present invention: including any of the above examples 1 to 104, further comprising an ozone removal device for removing or reducing ozone generated by the electric field device, the ozone removal device being between the electric field device outlet and the dust removal system outlet.
106. Example 106 provided by the present invention: including the example 105 described above, wherein the ozone depletion device further includes an ozone digester.
107. Example 107 provided by the present invention: including the example 106 above, wherein the ozone digester is selected from at least one of an ultraviolet ozone digester and a catalytic ozone digester.
108. Example 108 provided by the present invention: including any of examples 1 to 107 above, wherein a centrifugal separation mechanism is further included.
109. Example 109 provided by the present invention: including the example 108 described above, wherein the centrifugal separation mechanism includes a flow diversion channel, and the flow diversion channel is capable of changing a flow direction of the flow of the gas.
110. Example 110 provided by the present invention: including the example 109 described above, wherein the airflow diversion channel is capable of directing air to flow in a circumferential direction.
111. Example 111 provided by the present invention: including examples 108 or 109 described above, wherein the flow diverting passage is helical or conical.
112. Example 112 provided by the present invention: including any of the above examples 108-111, wherein the centrifugal separation mechanism comprises a separation cartridge.
113. Example 113 provided by the present invention: including the example 112 described above, wherein the airflow diversion channel is provided in the separation barrel, and a dust outlet is provided at the bottom of the separation barrel.
114. Example 114 provided by the present invention: including examples 112 or 113 above, wherein the separator bowl sidewall has an air inlet in communication with the first end of the airflow diversion channel.
115. Example 115 provided by the present invention: including any of the above examples 112-114, wherein the top of the separator bowl is provided with an air outlet in communication with the second end of the flow diverting passage.
116. Example 116 provided by the present invention: an air electric field dust removal method comprises the following steps:
an ionization dust removal electric field generated by passing dust-containing air through a dust removal electric field anode and a dust removal electric field cathode;
and when dust is deposited in the ionization dust removal electric field, dust removal treatment is carried out.
117. Example 117 provided by the present invention: the air electric field dust removal method of example 116, wherein the dust removal process is accomplished using an electric field back corona discharge phenomenon.
118. Example 118 provided by the present invention: the air electric field dust removal method of example 116, wherein the electric field back corona discharge phenomenon was utilized to boost the voltage, limit the injection current, and complete the dust removal process.
119. Example 119 provided by the present invention: the air electric field dust removal method comprising example 116, wherein the electric field back corona discharge phenomenon is utilized to increase voltage and limit injection current, so that the rapid discharge occurring at the anode dust accumulation position generates plasma, the plasma deeply oxidizes dust organic components, macromolecule bonds are broken, micromolecular carbon dioxide and water are formed, and dust removal treatment is completed.
120. Example 120 provided by the present invention: the air electric field dust removal method of any of examples 116-119, wherein the dust removal electric field cathode comprises at least one electrode rod.
121. Example 121 provided by the present invention: the air electric field dust removal method of example 120, wherein the diameter of the electrode rod is no greater than 3mm.
122. Example 122 provided by the present invention: the air electric field dust removing method including example 120 or 121, wherein the electrode rod has a shape of a needle, a polygonal shape, a burr shape, a screw rod shape, or a column shape.
123. Example 123 provided by the present invention: the air electric field dust removal method of any of examples 116-122, wherein the dust removal electric field anode consists of a hollow tube bundle.
124. Example 124 provided by the present invention: the air electric field dust removal method of example 123, wherein the hollow cross section of the anode tube bundle adopts a circular shape or a polygonal shape.
125. Example 125 provided by the present invention: the air electric field dust removal method of example 124, wherein the polygon is a hexagon.
126. Example 126 provided by the present invention: the air electric field dust removal method of any of examples 123-125, wherein the tube bundles of the dust removal electric field anodes are honeycomb-shaped.
127. Example 127 provided by the present invention: the air electric field dust removal method of any of examples 116-126, wherein the dust field cathode penetrates within the dust field anode.
128. Example 128 provided by the present invention: the air electric field dust removing method including any one of examples 116 to 127, wherein when the detected electric field current increases to a given value, dust cleaning treatment is performed.
129. Example 129 provided by the present invention: a method of oxygenating air comprising the steps of:
passing air through a flow passage;
an electric field is generated in the flow channel, the electric field being non-perpendicular to the flow channel, the electric field comprising an inlet and an outlet.
130. Example 130 provided by the present invention: the method of oxygenation of air comprising example 129, wherein the electric field comprises a first anode and a first cathode, the first anode and first cathode forming the flow path, the flow path opening the inlet and outlet.
131. Example 131 provided by the present invention: a method of oxygenation of air comprising any of examples 129 to 130, wherein the first anode and first cathode ionize oxygen in the air.
132. Example 132 provided by the present invention: a method of oxygenation of air comprising any of examples 129 to 131, wherein the electric field comprises a second electrode disposed at or near the inlet.
133. Example 133 provided by the present invention: the method of oxygenation of air comprising example 132, wherein said second electrode is a cathode.
134. Example 134 provided by the present invention: a method of oxygenation of air comprising any of examples 132 or 133, wherein the second electrode is an extension of the first cathode.
135. Example 135 provided by the present invention: the method of oxygenation of air comprising example 134, wherein the second electrode has an angle α with the first anode, and 0 ° < α+.ltoreq.125 °, or 45 ° +.ltoreq.125 °, or 60 ° +.ltoreq.100 °, or α=90°.
136. Example 136 provided by the present invention: a method of oxygenation of air comprising any of examples 129 to 135, wherein the electric field comprises a third electrode disposed at or near the outlet.
137. Example 137 provided by the present invention: the method of oxygenation of air comprising example 136, wherein the third electrode is an anode.
138. Example 138 provided by the present invention: a method of oxygenation of air comprising example 136 or 137, wherein said third electrode is an extension of said first anode.
139. Example 139 provided by the present invention: the method of oxygenation of air comprising example 138, wherein the third electrode has an angle α with the first cathode, and 0 ° < α+.ltoreq.125 °, or 45 ° +.ltoreq.125 °, or 60 ° +.ltoreq.100 °, or α=90°.
140. Example 140 provided by the present invention: a method of oxygenation of air comprising any of examples 134-139, wherein the third electrode is disposed independently of the first anode and first cathode.
141. Example 141 provided by the present invention: a method of oxygenation of air comprising any of examples 132-140, wherein the second electrode is disposed independently of the first anode and first cathode.
142. Example 142 provided by the present invention: a method of oxygenation of air comprising any of examples 130 to 141, wherein the first cathode comprises at least one electrode rod.
143. Example 143 provided by the present invention: the method of oxygenation of air comprising any of examples 130 to 142, wherein the first anode consists of a hollow tube bundle.
144. Example 144 provided by the present invention: the method of oxygenation of air comprising example 143, wherein the hollow cross-section of the anode bundle is circular or polygonal.
145. Example 145 provided by the present invention: the method of oxygenation of air comprising example 144, wherein said polygon is a hexagon.
146. Example 146 provided by the present invention: a method of oxygenation of air comprising any of examples 143 to 145, wherein the tube bundles of the first anode are honeycomb-shaped.
147. Example 147 provided by the present invention: a method of oxygenation of air comprising any of examples 130-146, wherein the first cathode penetrates within the first anode.
148. Example 148 provided by the present invention: a method of oxygenation of air comprising any of examples 130 to 147, wherein the electric field acts on oxygen ions in the flow path to increase oxygen ion flux and increase oxygen content of the outlet air.
149. Example 149 provided by the present invention: a method of reducing dust removal electric field coupling comprising the steps of:
and selecting the anode parameter of the dedusting electric field or/and the cathode parameter of the dedusting electric field to reduce the electric field coupling times.
150. Example 150 provided by the present invention: a method of reducing dust field coupling comprising example 149, wherein comprising selecting a ratio of a dust collection area of the dust field anode to a discharge area of the dust field cathode.
151. Example 151 provided by the present invention: a method of reducing dusting electric field coupling comprising example 150, wherein comprising selecting a ratio of a dust area of the dusting electric field anode to a discharge area of the dusting electric field cathode to be 1.667:1-1680:1.
152. example 152 provided by the present invention: a method of reducing dusting electric field coupling comprising example 150, wherein comprising selecting a ratio of a dust area of the dusting electric field anode to a discharge area of the dusting electric field cathode to be 6.67:1-56.67:1.
153. example 153 provided by the present invention: the method of reducing dusting electric field coupling of any of examples 149-152, comprising selecting the dusting electric field cathode to be 1-3 millimeters in diameter and the dusting electric field anode to be 2.5-139.9 millimeters in pole spacing from the dusting electric field cathode; the ratio of the dust accumulation area of the dust removal electric field anode to the discharge area of the dust removal electric field cathode is 1.667:1-1680:1.
154. example 154 provided by the present invention: a method of reducing dusting electric field coupling comprising any of examples 149 to 153, wherein comprising selecting a pole spacing of the dusting electric field anode and the dusting electric field cathode to be less than 150mm.
155. Example 155 provided by the present invention: a method of reducing dusting electric field coupling comprising any of examples 149 to 153, wherein comprising selecting a pole spacing of the dusting electric field anode to the dusting electric field cathode to be between 2.5-139.9mm.
156. Example 156 provided by the present invention: a method of reducing dusting electric field coupling comprising any of examples 149 to 153, wherein comprising selecting a pole spacing of the dusting electric field anode to the dusting electric field cathode to be between 5-100mm.
157. Example 157 provided by the present invention: a method of reducing dusting electric field coupling comprising any of examples 149 to 156, wherein comprising selecting the dusting electric field anode length to be 10-180 mm.
158. Example 158 provided by the present invention: a method of reducing dusting electric field coupling comprising any of examples 149 to 156, wherein comprising selecting the dusting electric field anode length to be 60-180 mm.
159. Example 159 provided by the present invention: a method of reducing dusting electric field coupling comprising any of examples 149 to 158, wherein comprising selecting the dusting electric field cathode length to be between 30 and 180mm.
160. Example 160 provided by the present invention: a method of reducing dusting electric field coupling comprising any of examples 149 to 158, wherein comprising selecting the dusting electric field cathode length to be 54-176 mm.
161. Example 161 provided by the present invention: the method of reducing dusting electric field coupling of any of examples 149 to 160, comprising selecting the dusting electric field cathode to comprise at least one electrode stick.
162. Example 162 provided by the present invention: a method of reducing dust removing electric field coupling comprising example 161, comprising selecting a diameter of the electrode rod to be no greater than 3mm.
163. Example 163 provided by the present invention: the method of reducing dust removing electric field coupling comprising example 161 or 162, wherein comprising selecting the shape of the electrode rod to be needle-like, multi-angular, burr-like, threaded rod-like, or cylindrical.
164. Example 164 provided by the present invention: the method of reducing dusting electric field coupling of any of examples 149-163, comprising selecting the dusting electric field anode to consist of a hollow tube bundle.
165. Example 165 provided by the present invention: a method of reducing dusting electric field coupling comprising example 164, wherein selecting a hollow cross-section of the anode tube bundle comprises employing a circle or polygon.
166. Example 166 provided by the present invention: a method of reducing electric field coupling for dust removal comprising example 165, comprising selecting the polygon to be a hexagon.
167. Example 167 provided by the present invention: the method of reducing dusting electric field coupling comprising any of examples 164 to 166, wherein the tube bundle comprising selecting the dusting electric field anode to be honeycomb-shaped.
168. Example 168 provided by the present invention: a method of reducing dusting electric field coupling comprising any of examples 149-167, wherein comprising selecting the dusting electric field cathode to penetrate within the dusting electric field anode.
169. Example 169 provided by the present invention: the method of reducing electric field coupling comprising any of examples 149 to 168, wherein the electric field anode and/or the electric field cathode dimensions are selected to result in an electric field coupling number of less than or equal to 3.
170. Example 170 provided by the present invention: an air dust removal method, comprising the steps of:
1) Adsorbing particles in the air by using an ionization dust removal electric field;
2) An electric field of ionization dust removal is used to charge the electret element.
171. Example 171 provided by the present invention: the air dust removal method of example 170, wherein the electret element is proximate to the electric field device outlet or the electret element is disposed at the electric field device outlet.
172. Example 172 provided by the present invention: the air dust removal method of example 170, wherein the dust removal field anode and the dust removal field cathode form an air flow channel, the electret element being disposed in the air flow channel.
173. Example 173 provided by the present invention: the air dust removal method of example 172, wherein the air flow channel comprises an air flow channel outlet, the electret element is proximate to the air flow channel outlet, or the electret element is disposed at the air flow channel outlet.
174. Example 174 provided by the present invention: the air dust removal method of any one of examples 170-173, wherein the particulate matter in the air is adsorbed with the charged electret element when the ionizing dust removal electric field is free of an energized drive voltage.
175. Example 175 provided by the present invention: the air dust removal method of example 174 was included in which the charged electret element was replaced with a new electret element after adsorbing some of the particulate matter in the air.
176. Example 176 provided by the present invention: the air cleaning method of example 175, wherein the ionizing dust removal electric field is restarted to adsorb particulates in the air after replacement with a new electret element and to charge the new electret element.
177. Example 177 provided by the invention: the air dust removal method of any of examples 170-176, wherein the material of the electret element comprises an inorganic compound having electret properties.
178. Example 178 provided by the present invention: the air dust removal method of example 177, wherein the inorganic compound is selected from one or more of an oxygen-containing compound, a nitrogen-containing compound, or a glass fiber.
179. Example 179 provided by the present invention: the air dust removal method of example 178, wherein the oxygen-containing compound is selected from one or more combinations of metal-based oxides, oxygen-containing complexes, oxygen-containing inorganic heteropolyacid salts.
180. Example 180 provided by the present invention: the air dust removal method of example 179, wherein the metal-based oxide is selected from one or more of aluminum oxide, zinc oxide, zirconium oxide, titanium oxide, barium oxide, tantalum oxide, silicon oxide, lead oxide, tin oxide, or a combination thereof.
181. Example 181 provided by the present invention: the air dust removal method of example 179, wherein the metal-based oxide is aluminum oxide.
182. Example 182 provided by the present invention: an air dust removal method comprising example 179, wherein the oxygen-containing compound is selected from one or more combinations of titanium zirconium composite oxides or titanium barium composite oxides.
183. Example 183 provided by the present invention: the air dust removal method of example 179, wherein the oxygen-containing inorganic heteropolyacid salt is selected from one or more of zirconium titanate, lead zirconate titanate, or barium titanate.
184. Example 184 provided by the present invention: the air dust removal method of example 178, wherein the nitrogen-containing compound is silicon nitride.
185. Example 185 provided by the present invention: the air dust removal method of any of examples 170-176, wherein the material of the electret element comprises an organic compound having electret properties.
186. Example 186 provided by the present invention: the air dust removal method of example 185, wherein the organic compound is selected from one or more of fluoropolymers, polycarbonates, PP, PE, PVC, natural waxes, resins, rosins.
187. Example 187 provided by the present invention: the air dust removal method of example 186, wherein the fluoropolymer is selected from one or more of polytetrafluoroethylene, polyperfluoroethylene propylene, soluble polytetrafluoroethylene, polyvinylidene fluoride.
188. Example 188 provided by the present invention: the air dust removal method of example 186, wherein the fluoropolymer is polytetrafluoroethylene.
189. Example 189 provided by the present invention: an air dust removal method is characterized by comprising the following steps: the air is removed or reduced by ionization dust removal.
190. Example 190 provided by the present invention: the air dust removal method of example 189, wherein ozone generated by ionization dust removal is digested with ozone.
191. Example 191 provided by the present invention: the air dust removal method of example 189, wherein the ozone digestion is selected from at least one of ultraviolet digestion and catalytic digestion.
In this application, "air" is defined broadly to include all gases.
Drawings
Fig. 1 is a schematic diagram of an electric field device in an embodiment of an air dust removal system according to the present invention.
Fig. 2 is a block diagram of another embodiment of a first water filtering mechanism disposed in an electric field device in an air dust removing system according to the present invention.
Fig. 3A is a schematic diagram of an embodiment of a wind equalizing device of an electric field device in an air dust removing system according to the present invention.
Fig. 3B is a schematic diagram of another embodiment of a wind-homogenizing device of an electric field device in the air dust removing system of the present invention.
Fig. 3C is a schematic diagram of another embodiment of a wind-homogenizing device of an electric field device in the air dust removing system of the present invention.
Fig. 3D is a top view of the second venturi plate wind-equalizing mechanism of the electric field device in the air dust removing system of the present invention.
Fig. 4 is a schematic diagram of an electric field device according to embodiment 2 of the present invention.
Fig. 5 is a schematic diagram of an electric field device according to embodiment 3 of the present invention.
Fig. 6 is a top view of the electric field device of fig. 1 according to the present invention.
Fig. 7 is a schematic view of the electret member of example 3 with a cross section of the flow channel occupying the cross section of the flow channel.
Fig. 8 is a schematic diagram of an air 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 of the present invention.
Fig. 10 is A-A view of the electric field generating unit of fig. 9.
Fig. 11 is A-A view of the electric field generating unit of fig. 9, labeled length and angle.
Fig. 12 is a schematic diagram of an electric field device structure with two electric field levels.
Fig. 13 is a schematic structural diagram of an electric field device in embodiment 17 of the present invention.
Fig. 14 is a schematic diagram of an electric field device in embodiment 19 of the present invention.
Fig. 15 is a schematic diagram of an electric field device in embodiment 20 of the present invention.
Fig. 16 is a schematic diagram of an electric field device in embodiment 22 of the present invention.
Detailed Description
Further advantages and effects of the present invention will become apparent to those skilled in the art from the disclosure of the present invention, which is described by the following specific examples.
It should be understood that the structures, proportions, sizes, etc. shown in the drawings are for illustration purposes only and should not be construed as limiting the invention to the extent that it can be practiced, since modifications, changes in the proportions, or otherwise, used in the practice of the invention, are not intended to be critical to the essential characteristics of the invention, but are intended to fall within the spirit and scope of the invention. Also, the terms such as "upper," "lower," "left," "right," "middle," and "a" and the like recited in the present specification are merely for descriptive purposes and are not intended to limit the scope of the invention, but are intended to provide relative positional changes or modifications without materially altering the technical context in which the invention may be practiced.
In an embodiment of the present invention, an air dust removal system is provided, including a dust removal system inlet, a dust removal system outlet, and an electric field device.
An air dust removal system in an embodiment of the invention includes a centrifugal separation mechanism. In one embodiment of the invention the centrifugal separation means comprises a flow diverting channel which is capable of changing the flow direction of the air flow. When the gas containing the particulate matter flows through the gas flow diversion channel, the flow direction of the gas is changed; the particles in the gas continue to move in the original direction under the action of inertia until colliding with the side wall of the airflow steering channel, namely the inner wall of the centrifugal separation mechanism, the particles cannot move continuously in the original direction and drop downwards under the action of gravity, so that the particles are separated from the gas.
In one embodiment of the invention, the gas flow diversion channel can guide the gas to flow along the circumferential direction. In one embodiment of the present invention, the airflow diversion channel may be spiral or conical. In one embodiment of the invention the centrifugal separation mechanism comprises a separation cylinder. The separating cylinder is internally provided with the airflow steering channel, and the bottom of the separating cylinder can be provided with a dust outlet. The separator cartridge side wall may be provided with an air inlet communicating with the first end of the airflow diversion channel. The top of the separating cylinder may be provided with an air outlet communicating with the second end of the airflow diversion channel. The air outlet is also referred to as an air outlet, and the size of the air outlet may be set according to the required amount of intake air. After the gas flows into the airflow steering channel of the separating cylinder from the air inlet, the gas is changed from linear motion to circular motion, and particles in the gas continue to move along the linear direction under the action of inertia until the particles collide with the inner wall of the separating cylinder, the particles cannot flow along with the gas, and the particles sink under the action of gravity, so that the particles are separated from the gas, the particles are finally discharged from a dust outlet at the bottom, and the gas is finally discharged from an air outlet at the top. In one embodiment of the invention, the inlet of the electric field device is in communication with the exhaust of the centrifugal separation mechanism. The gas outlet of the separating cylinder is positioned at the joint of the separating cylinder and the electric field device.
In one embodiment of the present invention, the centrifugal separation mechanism may have a bent structure. The centrifugal separation mechanism may be in the shape of one or a combination of a plurality of ring, return, cross, T, L, concave, or fold. The airflow diversion channel of the centrifugal separation mechanism has at least one turn. When the gas flows through the turning part, the flowing direction of the gas is changed, the particles in the gas continuously move in the original direction under the action of inertia until the particles collide with the inner wall of the centrifugal separation mechanism, the particles sink under the action of gravity after collision, the particles are separated from the gas and are finally discharged from a powder outlet at the lower end, and the gas finally flows out from the gas outlet.
In an embodiment of the present invention, a first filter layer may be disposed at the air outlet of the centrifugal separation mechanism, and the first filter layer may include a metal mesh, where the metal mesh may be disposed perpendicular to the air flow direction. The metal mesh will filter the gas exiting the vent to filter out particles in the gas that have not yet been separated.
In an embodiment of the invention, the air dust removal system may comprise an air homogenizing device. The wind homogenizing device is arranged in front of the electric field device and can enable air flow entering the electric field device to uniformly pass through.
In an embodiment of the present invention, the dust-removing electric field anode of the electric field device may be a cube, and the wind-homogenizing device may include an air inlet pipe located at one side of the cathode support plate, and an air outlet pipe located at the other side of the cathode support plate, where the cathode support plate is located at an air inlet end of the dust-removing electric field anode; wherein, the side of installation intake pipe is opposite with the side of installation outlet duct. The air equalizing device can make the air flow entering the electric field device uniformly pass through the electrostatic field.
In an embodiment of the present invention, the dust-removing electric field anode may be a cylinder, the wind-homogenizing device is located between the dust-removing system inlet and an ionization dust-removing electric field formed by the dust-removing electric field anode and the dust-removing electric field cathode, and the wind-homogenizing device includes a plurality of wind-homogenizing blades rotating around the center of the dust-removing system inlet. The air homogenizing device can enable various variable air inflow to uniformly pass through an electric field generated by the dust removal electric field anode, and meanwhile, the temperature inside the dust removal electric field anode can be kept constant, and oxygen is sufficient. The air equalizing device can make the air flow entering the electric field device uniformly pass through the electrostatic field.
In one embodiment of the invention, the air equalizing device comprises an air inlet plate arranged at the air inlet end of the dust removal electric field anode and an air outlet plate arranged at the air outlet end of the dust removal electric field anode, wherein the air inlet plate is provided with an air inlet hole, the air outlet plate is provided with air outlet holes, the air inlet holes and the air outlet holes are arranged in a staggered manner, and the air inlet at the front side and the air outlet at the side form a cyclone structure. The air equalizing device can make the air flow entering the electric field device uniformly pass through the electrostatic field.
In one embodiment of the present invention, the air dust removal system may include a dust removal system inlet, a dust removal system outlet, and an electric field device. The electric field device is also referred to as an electric field device. And in one embodiment of the present invention, the electric field device may include an electric field device inlet, an electric field device outlet, and a front electrode disposed between the electric field device inlet and the electric field device outlet, wherein particles in the gas are charged when the gas flows through the front electrode from the electric field device inlet.
In one embodiment of the present invention, the electric field device includes a pre-electrode between the inlet of the electric field device and an ionization dust removal electric field formed by the dust removal electric field anode and the dust removal electric field cathode. As the gas flows through the front electrode from the electric field device inlet, particulate matter and the like in the gas will become charged.
In one embodiment of the present invention, the shape of the pre-electrode may be point-like, linear, mesh-like, kong Banzhuang, plate-like, needle-like, ball-cage-like, box-like, tubular, natural, or processed. When the front electrode is of a porous structure, one or more air inlet through holes are formed in the front electrode. In an embodiment of the present invention, the shape of the air inlet hole may be polygonal, circular, elliptical, square, rectangular, trapezoid, or rhombic. The size of the air inlet through hole can be 0.1-3 mm, 0.1-0.2 mm, 0.2-0.5 mm, 0.5-1 mm, 1-1.2 mm, 1.2-1.5 mm, 1.5-2 mm, 2-2.5 mm, 2.5-2.8 mm or 2.8-3 mm in one embodiment of the invention.
In an embodiment of the present invention, the form of the pre-electrode may be one or more of solid, liquid, gas clusters, plasma, conductive mixed state substances, natural mixed conductive substances of living bodies, or artificial processing of the objects to form the conductive substances. Where the front electrode is solid, a solid metal such as 304 steel, or other solid conductor such as graphite, etc. may be used. When the front electrode is a liquid, it may be an ion-containing conductive liquid.
In operation, the front electrode charges the contaminant in the gas before the contaminant-laden gas enters the ionization dust removal electric field formed by the dust removal electric field anode and the dust removal electric field cathode, and when the contaminant-laden gas passes through the front electrode. When the gas with the pollutants enters the ionization dust removal electric field, the dust removal electric field anode applies attractive force to the charged pollutants, so that the pollutants move to the dust removal electric field anode until the pollutants are attached to the dust removal electric field anode.
In one embodiment of the invention, the pre-electrode directs electrons into the contaminant, which transfer between the contaminant between the pre-electrode and the dedusting field anode, charging more of the contaminant. Electrons are conducted between the front electrode and the dust removing electric field anode through pollutants, and electric current is formed.
In one embodiment of the invention the pre-electrode charges the contaminant by contacting the contaminant. In one embodiment of the invention the pre-electrode charges the contaminants by means of energy fluctuations. In one embodiment of the invention the pre-electrode transfers electrons to the contaminant by contact with the contaminant and charges the contaminant. In one embodiment of the invention the pre-electrode transfers electrons to the contaminant by way of energy fluctuations and charges the contaminant.
In one embodiment of the invention, the front electrode is linear and the dust removing electric field anode is planar. In one embodiment of the invention the front electrode is perpendicular to the dust removing electric field anode. In one embodiment of the invention the front electrode is parallel to the dust removing electric field anode. In one embodiment of the present invention, the front electrode is curved or arc-shaped. In one embodiment of the invention, the pre-electrode is a wire mesh. In one embodiment of the present invention, the voltage between the front electrode and the dust-removing electric field anode is different from the voltage between the dust-removing electric field cathode and the dust-removing electric field anode. In one embodiment of the present invention, the voltage between the front electrode and the dust removing electric field anode is less than the initial corona onset voltage. The onset corona onset voltage is the minimum value of the voltage between the dust field cathode and the dust field anode. In one embodiment of the present invention, the voltage between the front electrode and the dust removing electric field anode may be 0.1-2kv/mm.
In an embodiment of the invention, the electric field device includes a flow channel, and the front electrode is located in the flow channel. In one embodiment of the invention, the ratio of the cross-sectional area of the pre-electrode to the cross-sectional area of the flow channel is 99% -10%, or 90% -10%, or 80% -20%, or 70% -30%, or 60% -40%, or 50%. The cross-sectional area of the pre-electrode refers to the sum of the areas of the pre-electrode along the solid portion of the cross-section. In one embodiment of the invention the front electrode is negatively charged.
In an embodiment of the invention, when the gas flows into the flow channel through the inlet of the electric field device, when the metal dust, fog drops or aerosol with stronger conductivity in the gas contacts with the front electrode or the distance between the metal dust, fog drops or aerosol and other pollutants reaches a certain range, the metal dust, fog drops or aerosol and other pollutants are directly negatively charged, then all the pollutants enter the ionization dust removing electric field along with the gas flow, the anode of the dust removing electric field applies attractive force to the negatively charged metal dust, fog drops or aerosol and other pollutants, so that the negatively charged pollutants move to the anode of the dust removing electric field until the part of the pollutants are attached to the anode of the dust removing electric field, thereby realizing the collection of the part of the pollutants, and simultaneously realizing the collection of the part of the pollutants, wherein the oxygen ions are obtained through oxygen in the ionization dust removing electric field formed between the anode of the dust removing electric field and the cathode of the dust removing electric field, and after the oxygen ions with negative charges are combined with common dust, the common dust is negatively charged, the anode of the dust removing electric field applies attractive force to the part of the pollutants with negative charges, and the pollutants such as the dust and the like are enabled to move towards the anode of the dust removing electric field until the part of the pollutants is attached to the anode of the dust removing electric field, so that the part of the pollutants with weaker conductivity and the pollutants in the dust collecting the part of the metal dust is also weakly conductive, and the pollutants with stronger conductivity and the conductive and the pollutants are collected, and the pollutants in the dust and have stronger conductivity and the dust can collect the pollutants.
In one embodiment of the invention, the inlet of the electric field device is in communication with the exhaust of the separation mechanism.
In an embodiment of the present invention, the electric field device may include a dust-removing electric field cathode and a dust-removing electric field anode, and an ionization dust-removing electric field is formed between the dust-removing electric field cathode and the dust-removing electric field anode. The gas enters an ionization dust removal electric field, oxygen ions in the gas are ionized, a large amount of oxygen ions with charges are formed, the oxygen ions are combined with dust and other particles in the gas, so that the particles are charged, and an anode of the dust removal electric field applies adsorption force to the negatively charged particles, so that the particles are adsorbed on the anode of the dust removal electric field, and the particles in the gas are removed.
In an embodiment of the invention, the dust removing electric field cathode includes a plurality of cathode wires. The diameter of the cathode wire can be 0.1mm-20mm, and the size parameter is adjusted according to the application occasion and the dust accumulation requirement. In one embodiment of the invention the diameter of the cathode filament is not more than 3mm. In one embodiment of the invention, the cathode wire is made of metal wires or alloy wires which are easy to discharge, and is temperature-resistant, capable of supporting self weight and stable in electrochemistry. In one embodiment of the present invention, the cathode wire is made of titanium. The specific shape of the cathode wire is adjusted according to the shape of the dust removing electric field anode, for example, if the dust accumulation surface of the dust removing electric field anode is a plane, the section of the cathode wire is circular; if the dust accumulation surface of the dust removal electric field anode is an arc surface, the cathode wire needs to be designed into a multi-surface shape. The length of the cathode wire is adjusted according to the anode of the dust removing electric field.
In an embodiment of the invention, the dust removing electric field cathode includes a plurality of cathode bars. In one embodiment of the invention, the diameter of the cathode rod is not more than 3mm. In one embodiment of the present invention, a metal rod or an alloy rod that is easily discharged is used as the cathode rod. The shape of the cathode rod can be needle-shaped, polygonal, burr-shaped, threaded rod-shaped or columnar, etc. The shape of the cathode rod can be adjusted according to the shape of the dust removing electric field anode, for example, if the dust collecting surface of the dust removing electric field anode is a plane, the section of the cathode rod needs to be designed into a round shape; if the dust accumulation surface of the dust removal electric field anode is an arc surface, the cathode rod needs to be designed into a multi-surface shape.
In an embodiment of the present invention, the electric field dust removing cathode is disposed inside the electric field dust removing anode.
In one embodiment of the invention, the dedusting electric field anode comprises one or more hollow anode tubes arranged in parallel. When there are a plurality of hollow anode tubes, all hollow anode tubes form a honeycomb-shaped dust removal electric field anode. In one embodiment of the present invention, the hollow anode tube may have a circular or polygonal cross section. If the section of the hollow anode tube is circular, a uniform electric field can be formed between the dust removal electric field anode and the dust removal electric field cathode, and dust is not easy to accumulate on the inner wall of the hollow anode tube. If the cross section of the hollow anode tube is trilateral, 3 dust accumulation surfaces and 3 far-angle dust holding angles can be formed on the inner wall of the hollow anode tube, and the dust holding rate of the hollow anode tube with the structure is highest. If the section of the hollow anode tube is quadrilateral, 4 dust accumulation surfaces and 4 dust holding angles can be obtained, but the spliced structure is unstable. If the section of the hollow anode tube is hexagonal, 6 dust accumulation surfaces, 6 dust holding angles and the dust accumulation surfaces and the dust holding rate are balanced. If the cross section of the hollow anode tube is more polygonal, more dust accumulation sides can be obtained, but the dust holding rate is lost. In one embodiment of the present invention, the diameter of the inscribed circle of the hollow anode tube is in the range of 5mm to 400mm.
In one embodiment of the present invention, the electric field dust removing cathode is mounted on a cathode support plate, and the cathode support plate is connected with the electric field dust removing anode through an insulation mechanism. The insulation mechanism is used for realizing insulation between the cathode support plate and the dust removal electric field anode. In an embodiment of the present invention, the dust removal electric field anode includes a first anode portion and a second anode portion, wherein the first anode portion is close to the electric field device inlet, and the second anode portion is close to the electric field device outlet. The cathode support plate and the insulation mechanism are arranged between the first anode part and the second anode part, namely the insulation mechanism is arranged in the middle of an ionization electric field or in the middle of a dust removal electric field cathode, so that the dust removal electric field cathode can be well supported, and the dust removal electric field cathode can be fixed relative to the dust removal electric field anode, so that a set distance is kept between the dust removal electric field cathode and the dust removal electric field anode. In the prior art, the supporting point of the cathode is arranged at the end point of the cathode, so that the distance between the cathode and the anode is difficult to maintain. In an embodiment of the invention, the insulation mechanism is disposed outside the electric field flow channel, i.e. outside the electric field flow channel, so as to prevent or reduce dust in the gas from collecting on the insulation mechanism, which leads to breakdown or conduction of the insulation mechanism.
In one embodiment of the invention, the insulating mechanism is a high voltage resistant ceramic insulator, and the insulating mechanism insulates the dust removing electric field cathode from the dust removing electric field anode. The dust removing electric field anode is also referred to as a housing.
In an embodiment of the present invention, the first anode portion is located before the first cathode support plate and the insulating mechanism in the gas flow direction, and the first anode portion can remove water in the gas, so as to prevent water from entering the insulating mechanism, and cause the insulating mechanism to be short-circuited and fire. In addition, the first positive stage part can remove a considerable part of dust in the gas, and when the gas passes through the insulating mechanism, the considerable part of dust is eliminated, so that the possibility that the dust causes short circuit of the insulating mechanism is reduced. In one embodiment of the invention, the insulating mechanism comprises an insulating knob. The design of first positive pole portion is mainly in order to protect the insulating knob insulator from being polluted by particulate matters in the gas, in case the gas pollutes the insulating knob insulator and can lead to dust removal electric field positive pole and dust removal electric field negative pole to lead to the laying dust function inefficacy of dust removal electric field positive pole, so the design of first positive pole portion can effectively reduce the insulating knob insulator and be polluted, improves the live time of product. In the process that the gas flows through the electric field flow channel, the first anode part and the dust removing electric field cathode are contacted with the gas with pollution, and the insulating mechanism is contacted with the gas, so that the purposes of removing dust firstly and then passing through the insulating mechanism are achieved, pollution to the insulating mechanism is reduced, the cleaning maintenance period is prolonged, and the corresponding electrode is used and supported in an insulating way. The length of the first anode portion is long enough to remove a portion of the dust, reduce dust accumulation on the insulator mechanism and the cathode support plate, and reduce electrical breakdown caused by the dust. In an embodiment of the present invention, the length of the first anode portion is 1/10 to 1/4, 1/4 to 1/3, 1/3 to 1/2, 1/2 to 2/3, 2/3 to 3/4, or 3/4 to 9/10 of the total length of the anode of the dust removing electric field.
In one embodiment of the invention, the second anode part is located after the cathode support plate and the insulating means in the gas flow direction. The second anode part comprises a dust accumulation section and a reserved dust accumulation section. The dust accumulation section utilizes static electricity to adsorb particles in the gas, and the dust accumulation section is used for increasing the dust accumulation area and prolonging the service time of the electric field device. The reserved dust accumulation section can provide failure protection for the dust accumulation section. The reserved dust accumulation section is used for further improving the dust accumulation area and the dust removal effect on the premise of meeting the design dust removal requirement. The reserved dust accumulation section is used for supplementing the dust accumulation of the front section. In one embodiment of the present invention, the first anode portion and the second anode portion may use different power sources.
In an embodiment of the present invention, since there is an extremely high potential difference between the electric field cathode and the electric field anode, in order to prevent the electric field cathode and the electric field anode from being conducted, the insulation mechanism is disposed outside the electric field flow path between the electric field cathode and the electric field anode. Therefore, the insulating mechanism is externally hung outside the dust removal electric field anode. In one embodiment of the present invention, the insulating mechanism may be made of non-conductive heat-resistant material, such as ceramic, glass, etc. In one embodiment of the invention, the insulation of the completely airtight airless material requires an insulation isolation thickness of >0.3mm/kv; air insulation requirements >1.4mm/kv. The insulation distance may be set according to 1.4 times of the pole spacing between the dust removing electric field cathode and the dust removing electric field anode. In one embodiment of the invention, the insulating mechanism uses ceramic, and the surface is glazed; glue or organic material cannot be used to fill the connection, and the temperature resistance is greater than 350 ℃.
In an embodiment of the invention, the insulation mechanism includes an insulation portion and a heat insulation portion. In order to provide the insulating mechanism with an anti-fouling function, the material of the insulating part is ceramic material or glass material. In an embodiment of the present invention, the insulating portion may be an umbrella-shaped string ceramic pillar or glass pillar, and the glaze is hung inside and outside the umbrella. The distance between the outer edge of the umbrella-shaped string ceramic column or glass column and the dust removing electric field anode is more than 1.4 times of the electric field distance, namely more than 1.4 times of the polar distance. The sum of the spacing of the umbrella ribs of the umbrella-shaped string ceramic posts or the glass posts is larger than 1.4 times of the insulation spacing of the umbrella-shaped string ceramic posts. The total depth of the inner edge of the umbrella-shaped string ceramic column or the glass column is 1.4 times longer 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, and glaze is hung inside and outside the column. In an embodiment of the present invention, the insulating portion may also be tower-shaped.
In an embodiment of the present invention, a heating rod is disposed in the insulating portion, and when the ambient temperature of the insulating portion approaches the dew point, the heating rod is started and heats. Because of the temperature difference between the inside and the outside of the insulating part in use, condensation is easy to generate between the inside and the outside of the insulating part. The outer surface of the insulating part may be heated spontaneously or by gas to generate high temperature, and necessary isolation protection and scald prevention are required. The heat insulation part comprises a protective surrounding baffle plate and a denitration purification reaction cavity which are positioned outside the heat insulation part. In an embodiment of the invention, the position of the tail part of the insulating part needs to be insulated from heat, so that the environment is prevented, and the heat dissipation and high temperature heating condensation assembly is prevented.
In an embodiment of the invention, an outgoing line of a power supply of the electric field device is connected by using umbrella-shaped string ceramic columns or glass columns through a wall, an elastic latch is used for connecting a cathode support plate in the wall, a sealed insulation protective wiring cap is used for connecting the outside of the wall in a plug-in mode, and the insulation distance between a conductor of the outgoing line through the wall and the wall is larger than the ceramic insulation distance between the umbrella-shaped string ceramic columns or the glass columns. In one embodiment of the invention, the high-voltage part is directly arranged on the end head without a lead, so that the safety is ensured, the whole high-voltage module is protected by using the ip68 for external insulation, and the medium is used for heat exchange and radiation.
In one embodiment of the present invention, an asymmetric structure is used between the electric field dust collector cathode and the electric field dust collector anode. In the symmetrical electric field, the polar particles are acted by a force with the same magnitude and opposite directions, and the polar particles reciprocate in the electric field; in an asymmetric electric field, the polar particles are subjected to two different acting forces, and the polar particles move in the direction of large acting force, so that the coupling can be avoided.
An ionization dust-removing electric field is formed between a dust-removing electric field cathode and a dust-removing electric field anode of the electric field device. In order to reduce electric field coupling of the ionization dust removing electric field, in an embodiment of the present invention, a method for reducing electric field coupling includes the following steps: the ratio of the dust collection area of the dust collection electric field anode to the discharge area of the dust collection electric field cathode is selected to ensure that the electric field coupling times are less than or equal to 3. In an embodiment of the present invention, a ratio of a dust collection area of a dust collection electric field anode to a discharge area of a dust collection electric field cathode may be: 1.667:1-1680:1, a step of; 3.334:1-113.34:1, a step of; 6.67:1-56.67:1, a step of; 13.34:1-28.33:1. the embodiment selects the dust collection area of the anode of the dust removal electric field with relatively large area and the discharge area of the cathode of the dust removal electric field with relatively small area, and specifically selects the area ratio, so that the discharge area of the cathode of the dust removal electric field can be reduced, the suction force is reduced, the dust collection area of the anode of the dust removal electric field is enlarged, the suction force is enlarged, namely, the asymmetrical electrode suction force is generated between the cathode of the dust removal electric field and the anode of the dust removal electric field, so that dust falls into the dust collection surface of the anode of the dust removal electric field after charged, the polarity is changed but can not be sucked away by the cathode of the dust removal electric field any more, the electric field coupling is reduced, and the electric field coupling times are less than or equal to 3. The electric field coupling times are less than or equal to 3 when the electric field pole spacing is less than 150mm, the electric field energy consumption is low, the coupling consumption of the electric field to aerosol, water mist, oil mist and loose and smooth particles can be reduced, and the electric energy of the electric field is saved by 30-50%. The dust collection area refers to the area of the working surface of the anode of the dust collection electric field, for example, if the anode of the dust collection electric field is in a hollow regular hexagonal tubular shape, the dust collection area is the inner surface area of the hollow regular hexagonal tubular shape, and the dust collection area is also called as dust accumulation area. The discharge area refers to the area of the working surface of the cathode of the dust removing electric field, for example, if the cathode of the dust removing electric field is in a rod shape, the discharge area is the rod-shaped outer surface area.
In one embodiment of the invention, the length of the dust removing electric field anode can be 10-180 mm, 10-20 mm, 20-30 mm, 60-180 mm, 30-40 mm, 40-50 mm, 50-60 mm, 60-70 mm, 70-80 mm, 80-90 mm, 90-100 mm, 100-110 mm, 110-120 mm, 120-130 mm, 130-140 mm, 140-150 mm, 150-160 mm, 160-170 mm, 170-180 mm, 60mm, 180mm, 10mm or 30mm. The length of the dust removing electric field anode refers to the minimum length from one end to the other end of the working surface of the dust removing electric field anode. The length of the dust removal electric field anode is selected, so that electric field coupling can be effectively reduced.
In one embodiment of the invention, the length of the dust removing electric field anode can be 10-90 mm, 15-20 mm, 20-25 mm, 25-30 mm, 30-35 mm, 35-40 mm, 40-45 mm, 45-50 mm, 50-55 mm, 55-60 mm, 60-65 mm, 65-70 mm, 70-75 mm, 75-80 mm, 80-85 mm or 85-90 mm, and the design of the length can enable the dust removing electric field anode and the electric field device to have high temperature resistance and high efficiency dust collecting capability under high temperature impact.
In one embodiment of the invention, the length of the dedusting electric field cathode can be 30-180 mm, 54-176 mm, 30-40 mm, 40-50 mm, 50-54 mm, 54-60 mm, 60-70 mm, 70-80 mm, 80-90 mm, 90-100 mm, 100-110 mm, 110-120 mm, 120-130 mm, 130-140 mm, 140-150 mm, 150-160 mm, 160-170 mm, 170-176 mm, 170-180 mm, 54mm, 180mm or 30mm. The length of the dust removing electric field cathode refers to the minimum length from one end to the other end of the working surface of the dust removing electric field cathode. The dust removal electric field cathode is selected to be of such a length that electric field coupling can be effectively reduced.
In one embodiment of the invention, the length of the dedusting electric field cathode can be 10-90 mm, 15-20 mm, 20-25 mm, 25-30 mm, 30-35 mm, 35-40 mm, 40-45 mm, 45-50 mm, 50-55 mm, 55-60 mm, 60-65 mm, 65-70 mm, 70-75 mm, 75-80 mm, 80-85 mm or 85-90 mm, and the design of the length can enable the dedusting electric field cathode and the electric field device to have high temperature resistance and high efficiency dust collection capability under high temperature impact.
In one embodiment of the invention, the distance between the dedusting electric field anode and the dedusting electric field cathode 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, 30-40 mm, 40-50 mm, 50-60 mm, 60-70 mm, 70-80 mm, 80-90 mm, 90-100 mm, 100-110 mm, 110-120 mm, 120-130 mm, 130-139.9 mm, 9.9mm, 139.9mm, or 2.5mm. The distance between the field anode and the field cathode is also referred to as the pole pitch. The pole spacing is specifically the minimum vertical distance between the dust removing electric field anode and the dust removing electric field cathode working surface. The selection of the polar distance can effectively reduce electric field coupling and enable the electric field device to have high temperature resistance.
In an embodiment of the present invention, the diameter of the dust-removing electric field cathode is 1-3 mm, and the pole distance between the dust-removing electric field anode and the dust-removing electric field cathode is 2.5-139.9 mm; the ratio of the dust accumulation area of the dust removal electric field anode to the discharge area of the dust removal electric field cathode is 1.667:1-1680:1.
in view of the unique properties of ionized dust removal, ionized dust removal may be suitable for removing particulate matter from a gas. However, through many years of researches of universities, research institutions and enterprises, the existing electric field dust removing device can only remove about 70% of particulate matters, and cannot meet the needs of many industries. In addition, the electric field dust removing device in the prior art is too large in size.
The present inventors have studied and found that the disadvantage of the electric field dust removing device in the prior art is caused by electric field coupling. The invention can obviously reduce the size (i.e. volume) of the electric field dust removing device by reducing the electric field coupling times. For example, the size of the ionization dust removing device provided by the invention is about one fifth of the size of the existing ionization dust removing device. The reason is that in order to obtain an acceptable particle removal rate, the gas flow rate is set to be about 1m/s in the existing ionization dust removing device, and the invention can still obtain a higher particle removal rate under the condition that the gas flow rate is increased to be 6 m/s. When treating a given flow of gas, the electric field dust collector may be reduced in size as the gas velocity increases.
In addition, the present invention can significantly improve particle removal efficiency. For example, the electric field dust removing device of the related art can remove about 70% of particulate matter in the exhaust gas of the engine at a gas flow rate of about 1m/s, but the present invention can remove about 99% of particulate matter even at a gas flow rate of 6 m/s.
The present invention has achieved the above unexpected results, since the inventors have found the effect of electric field coupling and have found a method of reducing the number of electric field coupling.
The ionised dust removal electric field between the dust removal electric field anode and the dust removal electric field cathode is also referred to as the first electric field. In an embodiment of the present invention, a second electric field that is not parallel to the first electric field is further formed between the dust-removing electric field anode and the dust-removing electric field cathode. In another embodiment of the present invention, the second electric field is not perpendicular to the flow channel of the ionization dust removing electric field. The second electric field, also called auxiliary electric field, may be formed by one or two first auxiliary electrodes, which may be placed at the inlet or outlet of the ionised dust removal electric field when the second electric field is formed by one first auxiliary electrode, which may be negatively or positively charged. When the first auxiliary electrode is a cathode, the first auxiliary electrode is arranged at or near an inlet of the ionization dust removal electric field; the first auxiliary electrode and the dust removing electric field anode have an included angle alpha, and alpha is more than or equal to 0 degree and less than or equal to 125 degrees, or alpha is more than or equal to 45 degrees and less than or equal to 125 degrees, or alpha is more than or equal to 60 degrees and less than or equal to 100 degrees, or alpha=90 degrees. When the first auxiliary electrode is an anode, the first auxiliary electrode is arranged at or near an outlet of the ionization dust removal electric field; the first auxiliary electrode and the dedusting electric field cathode have an included angle alpha, and alpha is more than or equal to 0 degree and less than or equal to 125 degrees, or alpha is more than or equal to 45 degrees and less than or equal to 125 degrees, or alpha is more than or equal to 60 degrees and less than or equal to 100 degrees, or alpha=90 degrees. When the second electric field is formed by two first auxiliary electrodes, one of the first auxiliary electrodes may be charged with a negative potential and the other first auxiliary electrode may be charged with a positive potential; one first auxiliary electrode may be placed at the inlet of the ionization electric field and the other first auxiliary electrode at the outlet of the ionization electric field. In addition, the first auxiliary electrode may be a part of the dust-removing electric field cathode or the dust-removing electric field anode, that is, the first auxiliary electrode may be formed by an extension of the dust-removing electric field cathode or the dust-removing electric field anode, where the lengths of the dust-removing electric field cathode and the dust-removing electric field anode are different. The first auxiliary electrode may also be a separate electrode, that is, the first auxiliary electrode may not be part of the dedusting electric field cathode or the dedusting electric field anode, and in this case, the voltage of the second electric field is different from the voltage of the first electric field and may be separately controlled according to the working condition.
The second electric field is capable of applying a force to the negatively charged oxygen ion stream between the dedusting field anode and the dedusting field cathode toward the outlet of the ionization electric field such that the negatively charged oxygen ion stream between the dedusting field anode and the dedusting field cathode has a velocity of movement toward the outlet. In the process that gas flows into an ionization electric field and flows towards the outlet direction of the ionization electric field, negatively charged oxygen ions move towards the anode of the dust removal electric field and towards the outlet direction of the ionization electric field, and the negatively charged oxygen ions are combined with particles in the gas in the process of moving towards the anode of the dust removal electric field and towards the outlet of the ionization electric field, as the oxygen ions have the moving speed towards the outlet, the oxygen ions cannot generate stronger collision when being combined with the particles, so that the stronger collision is avoided, the larger energy consumption is caused, the oxygen ions are ensured to be easily combined with the particles, the charged efficiency of the particles in the gas is higher, more particles can be collected under the action of the anode of the dust removal electric field, and the dust removal efficiency of the electric field device is ensured to be higher. The collection rate of the electric field device for particles entering the electric field along the ion flow direction is nearly doubled compared with that of particles entering the electric field along the counter ion flow direction, so that the dust accumulation efficiency of the electric field is improved, and the electric consumption of the electric field is reduced. In addition, the main reason that the dust collection efficiency of the dust collection electric field in the prior art is lower is that the direction of dust entering the electric field is opposite to or vertically crossed with the direction of ion flow in the electric field, so that the mutual collision of the dust and the ion flow is severe, larger energy consumption is generated, the charge efficiency is influenced, the dust collection efficiency of the electric field in the prior art is further reduced, and the energy consumption is increased. When the electric field device collects dust in the gas, the gas and the dust enter the electric field along the ion flow direction, the dust is charged fully, and the electric field consumption is small; the dust collection efficiency of the monopole electric field can reach 99.99 percent. When gas and dust enter an electric field in the reverse ion flow direction, the dust charge is insufficient, the electric consumption of the electric field is increased, and the dust collection efficiency is 40% -75%. In one embodiment of the invention, the ion flow formed by the electric field device is beneficial to fluid transportation, air intake oxygenation, heat exchange or the like of the unpowered fan.
Along with the continuous collection of particulate matters and the like in the inlet air by the dust removal electric field anode, the particulate matters and the like are accumulated on the dust removal electric field anode to form dust, and the dust thickness is continuously increased, so that the polar distance is reduced. In an embodiment of the present invention, when the electric field is deposited, the electric field device detects the electric field current and performs dust cleaning by any one of the following methods:
(1) When the electric field device detects that the electric field current increases to a given value, the electric field voltage is increased.
(2) When the electric field device detects that the electric field current is increased to a given value, the electric field back corona discharge phenomenon is utilized to finish dust cleaning.
(3) When the electric field device detects that the electric field current increases to a given value, the electric field back corona discharge phenomenon is utilized to increase the electric field voltage and limit the injection current, so that dust cleaning is completed.
(4) When the electric field device detects that the electric field current increases to a given value, the electric field back corona discharge phenomenon is utilized to increase the electric field voltage and limit the injection current, so that the rapid discharge at the carbon deposition position of the anode generates plasma, the plasma enables the dust organic components to be deeply oxidized, polymer bonds to be broken, and micromolecular carbon dioxide and water are formed, so that dust cleaning is completed.
In an embodiment of the present invention, the dust removing electric field anode and the dust removing electric field cathode are respectively electrically connected with two electrodes of the power supply. The voltages applied to the dedusting electric field anode and the dedusting electric field cathode need to be selected to be appropriate voltage levels, and the specific selection of the voltage levels depends on the volume, temperature resistance, dust holding rate and the like of the electric field device. For example, voltages from 1kv to 50kv; during design, firstly, considering temperature-resistant conditions, and parameters of polar distance and temperature: the dust accumulation area is larger than 0.1 square/kilocubic meter/hour, the electric field length is larger than 5 times of a single-tube inscribed circle, and the flow speed of the electric field airflow is controlled to be smaller than 9 meters/second. In one embodiment of the present invention, the dust removing electric field anode is formed by a first hollow anode tube and is honeycomb-shaped. The shape of the first hollow anode tube port may be circular or polygonal. In one embodiment of the invention, the value range of the inscribed circle of the first hollow anode tube is 5-400mm, the corresponding voltage is 0.1-120kv, and the corresponding current of the first hollow anode tube is 0.1-30A; different inscribed circles correspond to different corona voltages, about 1KV/1MM.
In an embodiment of the invention, the electric field device includes a first electric field stage, where the first electric field stage includes a plurality of first electric field generating units, and one or more first electric field generating units may be provided. The first electric field generating unit is also called a first dust collecting unit, and the first dust collecting unit comprises one or more of the dust collecting electric field anode and the dust collecting electric field cathode. When the first electric field level is multiple, the dust collection efficiency of the electric field device can be effectively improved. In the same first electric field stage, anodes of all the dust removing electric fields are of the same polarity, and cathodes of all the dust removing electric fields are of the same polarity. And when the number of the first electric field stages is multiple, the first electric field stages are connected in series. In an embodiment of the invention, the electric field device further includes a plurality of connection housings, and the first electric field stages connected in series are connected through the connection housings; the distance of the first electric field stage of adjacent two stages is greater than 1.4 times of the pole pitch.
In one embodiment of the invention, the electret material is charged with an electric field. When the electric field device fails, the charged electret material is used for dust removal.
In one embodiment of the invention, the electric field device comprises an electret element.
In an embodiment of the present invention, the electret element is disposed in the dust removing electric field anode.
In an embodiment of the present invention, the dust-removing electric field anode and the dust-removing electric field cathode form an ionization dust-removing electric field when the power is turned on, and the electret element is in the ionization dust-removing electric field.
In an embodiment of the invention, the electret element is located close to the electric field device outlet or the electret element is located at the electric field device outlet.
In an embodiment of the present invention, the dust removing electric field anode and the dust removing electric field cathode form a flow channel, and the electret element is disposed in the flow channel.
In an embodiment of the invention, the flow channel comprises a flow channel outlet, and the electret element is close to the flow channel outlet or is arranged at the flow channel outlet.
In an embodiment of the present invention, the electret element has a cross section in the flow channel that is 5% -100% of the cross section of the flow channel.
In one embodiment of the invention, the electret element has a cross-section in the flow channel that is 10% -90%, 20% -80%, or 40% -60% of the cross-section of the flow channel.
In one embodiment of the invention, the ionizing dust removal electric field charges the electret member.
In one embodiment of the invention, the electret element has a porous structure.
In one embodiment of the invention, the electret element is a fabric.
In an embodiment of the present invention, the inside of the dust removing electric field anode is tubular, the outside of the electret element is tubular, and the outside of the electret element is sleeved inside the dust removing electric field anode.
In an embodiment of the present invention, the electret element is detachably connected to the dust removing electric field anode.
In one embodiment of the invention, the electret element material comprises an inorganic compound having electret properties. The electret performance refers to the capability of the electret element that the electret element is charged after being charged by an external power supply and still maintains a certain charge under the condition that the electret element is completely separated from the power supply, so that the electret element can serve as an electrode of an electric field.
In an embodiment of the present invention, the inorganic compound is selected from one or more of an oxygen-containing compound, a nitrogen-containing compound, and glass fiber.
In an embodiment of the present invention, the oxygen-containing compound is selected from one or more of metal-based oxides, oxygen-containing complexes, oxygen-containing inorganic heteropolyacid salts.
In an embodiment of the present invention, the metal-based oxide is selected from one or more of aluminum oxide, zinc oxide, zirconium oxide, titanium oxide, barium oxide, tantalum oxide, silicon oxide, lead oxide, and tin oxide.
In an embodiment of the present invention, the metal-based oxide is alumina.
In an embodiment of the present invention, the oxygen-containing compound is selected from one or more of titanium zirconium composite oxide or titanium barium composite oxide.
In an embodiment of the present invention, the oxygen-containing inorganic heteropolyacid salt is selected from one or more of zirconium titanate, lead zirconate titanate or barium titanate.
In one embodiment of the present invention, the nitrogen-containing compound is silicon nitride.
In one embodiment of the invention, the electret element material comprises an organic compound having electret properties. The electret performance refers to the capability of the electret element that the electret element is charged after being charged by an external power supply and still maintains a certain charge under the condition that the electret element is completely separated from the power supply, so that the electret element can serve as an electrode of an electric field.
In an embodiment of the present invention, the organic compound is selected from one or more of a fluoropolymer, a polycarbonate, PP, PE, PVC, a natural wax, a resin, and a rosin.
In one embodiment of the present invention, the fluoropolymer is selected from one or more of Polytetrafluoroethylene (PTFE), polytetrafluoroethylene (Teflon-FEP), soluble Polytetrafluoroethylene (PFA), polyvinylidene fluoride (PVDF).
In one embodiment of the invention, the fluoropolymer is polytetrafluoroethylene.
The electric field of ionization dust removal is generated under the condition of the power-on driving voltage, the part of the object to be treated is ionized by the electric field of ionization dust removal, particles in the air are adsorbed, meanwhile, the electret element is charged, when the electric field device fails, namely, the power-on driving voltage is not applied, the charged electret element generates an electric field, and the charged electret element is used for adsorbing the particles in the air, namely, the adsorption of the particles can still be carried out under the condition that the electric field of ionization dust removal fails.
In an embodiment of the invention, the air dust removal system further includes a deodorizing device for removing or reducing ozone generated by the electric field device, and the deodorizing device is located between the electric field device outlet and the air dust removal system outlet.
In an embodiment of the invention, the ozone removal device includes an ozone absorber.
In an embodiment of the present invention, the ozone digestion device is at least one selected from the group consisting of an ultraviolet ozone digestion device and a catalytic ozone digestion device.
The air dust removal system also comprises an ozone removal device for removing or reducing ozone generated by the electric field device.
In an embodiment of the present invention, the present invention provides an air dust removal method, including the following steps:
an ionization dust removal electric field generated by passing dust-containing air through a dust removal electric field anode and a dust removal electric field cathode;
and when dust is deposited in the electric field, dust cleaning treatment is carried out.
In one embodiment of the invention, the dust cleaning process is performed when the detected electric field current increases to a given value.
In one embodiment of the present invention, when the electric field is dust-collecting, dust cleaning is performed by any of the following modes:
(1) And finishing dust cleaning treatment by utilizing the electric field back corona discharge phenomenon.
(2) And the electric field back corona discharge phenomenon is utilized to increase the voltage and limit the injection current, so as to finish dust cleaning.
(3) The electric field back corona discharge phenomenon is utilized to increase the voltage and limit the injection current, so that the rapid discharge generated at the anode dust accumulation position generates plasma, the plasma enables the dust organic components to be deeply oxidized, macromolecular bonds to be broken, and micromolecular carbon dioxide and water are formed, so that dust cleaning treatment is completed.
Preferably, the dust is carbon black.
In an embodiment of the invention, the dust removing electric field cathode includes a plurality of cathode wires. The diameter of the cathode wire can be 0.1mm-20mm, and the size parameter is adjusted according to the application occasion and the dust accumulation requirement. In one embodiment of the invention the diameter of the cathode filament is not more than 3mm. In one embodiment of the invention, the cathode wire is made of metal wires or alloy wires which are easy to discharge, and is temperature-resistant, capable of supporting self weight and stable in electrochemistry. In one embodiment of the present invention, the cathode wire is made of titanium. The specific shape of the cathode wire is adjusted according to the shape of the dust removing electric field anode, for example, if the dust accumulation surface of the dust removing electric field anode is a plane, the section of the cathode wire is circular; if the dust accumulation surface of the dust removal electric field anode is an arc surface, the cathode wire needs to be designed into a multi-surface shape. The length of the cathode wire is adjusted according to the anode of the dust removing electric field.
In an embodiment of the invention, the dust removing electric field cathode includes a plurality of cathode bars. In one embodiment of the invention, the diameter of the cathode rod is not more than 3mm. In one embodiment of the present invention, a metal rod or an alloy rod that is easily discharged is used as the cathode rod. The shape of the cathode rod can be needle-shaped, polygonal, burr-shaped, threaded rod-shaped or columnar, etc. The shape of the cathode rod can be adjusted according to the shape of the dust removing electric field anode, for example, if the dust collecting surface of the dust removing electric field anode is a plane, the section of the cathode rod needs to be designed into a round shape; if the dust accumulation surface of the dust removal electric field anode is an arc surface, the cathode rod needs to be designed into a multi-surface shape.
In an embodiment of the present invention, the electric field dust removing cathode is disposed inside the electric field dust removing anode.
In one embodiment of the invention, the dedusting electric field anode comprises one or more hollow anode tubes arranged in parallel. When there are a plurality of hollow anode tubes, all hollow anode tubes form a honeycomb-shaped dust removal electric field anode. In one embodiment of the present invention, the hollow anode tube may have a circular or polygonal cross section. If the section of the hollow anode tube is circular, a uniform electric field can be formed between the dust removal electric field anode and the dust removal electric field cathode, and dust is not easy to accumulate on the inner wall of the hollow anode tube. If the cross section of the hollow anode tube is trilateral, 3 dust accumulation surfaces and 3 far-angle dust holding angles can be formed on the inner wall of the hollow anode tube, and the dust holding rate of the hollow anode tube with the structure is highest. If the section of the hollow anode tube is quadrilateral, 4 dust accumulation surfaces and 4 dust holding angles can be obtained, but the spliced structure is unstable. If the section of the hollow anode tube is hexagonal, 6 dust accumulation surfaces, 6 dust holding angles and the dust accumulation surfaces and the dust holding rate are balanced. If the cross section of the hollow anode tube is more polygonal, more dust accumulation sides can be obtained, but the dust holding rate is lost. In one embodiment of the present invention, the diameter of the inscribed circle of the hollow anode tube is in the range of 5mm to 400mm.
In an embodiment of the present invention, the present invention provides a method for accelerating air, comprising the steps of:
passing air through a flow passage;
an electric field is generated in the flow channel, the electric field being non-perpendicular to the flow channel, the electric field comprising an inlet and an outlet.
Wherein the electric field ionizes the air.
In one embodiment of the invention, the electric field comprises a first anode and a first cathode, the first anode and the first cathode forming the flow channel, the flow channel connecting the inlet and the outlet. The first anode and the first cathode ionize air in the flow channel.
In an embodiment of the invention, the electric field includes a second electrode, and the second electrode is disposed at or near the inlet.
Wherein the second electrode is a cathode and is an extension of the first cathode. Preferably, the second electrode has an angle α with the first anode, and 0 ° < α+.ltoreq.125 °, or 45 ° +.ltoreq.125 °, or 60 ° +.ltoreq.100 °, or α=90°.
In an embodiment of the invention, the second electrode is disposed independently from the first anode and the first cathode.
In an embodiment of the invention, the electric field includes a third electrode, and the third electrode is disposed at or near the inlet or the outlet.
Wherein the third electrode is an anode and the third electrode is an extension of the first anode. Preferably, the third electrode has an angle α with the first cathode, and 0 ° < α+.ltoreq.125 °, or 45 ° +.ltoreq.125 °, or 60 ° +.ltoreq.100 °, or α=90°.
In an embodiment of the invention, the third electrode is disposed independently from the first anode and the first cathode.
In an embodiment of the invention, the first cathode includes a plurality of cathode wires. The diameter of the cathode wire can be 0.1mm-20mm, and the size parameter is adjusted according to the application occasion and the dust accumulation requirement. In one embodiment of the invention the diameter of the cathode filament is not more than 3mm. In one embodiment of the invention, the cathode wire is made of metal wires or alloy wires which are easy to discharge, and is temperature-resistant, capable of supporting self weight and stable in electrochemistry. In one embodiment of the present invention, the cathode wire is made of titanium. The specific shape of the cathode wire is adjusted according to the shape of the first anode, for example, if the dust accumulation surface of the first anode is a plane, the section of the cathode wire is circular; if the dust accumulation surface of the first anode is an arc surface, the cathode wire needs to be designed into a polygonal shape. The length of the cathode wire is adjusted according to the first anode.
In an embodiment of the invention, the first cathode includes a plurality of cathode rods. In one embodiment of the invention, the diameter of the cathode rod is not more than 3mm. In one embodiment of the present invention, a metal rod or an alloy rod that is easily discharged is used as the cathode rod. The shape of the cathode rod can be needle-shaped, polygonal, burr-shaped, threaded rod-shaped or columnar, etc. The shape of the cathode rod can be adjusted according to the shape of the first anode, for example, if the dust accumulation surface of the first anode is a plane, the section of the cathode rod needs to be designed into a round shape; if the dust accumulation surface of the first anode is an arc surface, the cathode rod needs to be designed into a polygonal shape.
In an embodiment of the invention, the first cathode is disposed through the first anode.
In one embodiment of the invention, the first anode comprises one or more hollow anode tubes arranged in parallel. When there are a plurality of hollow anode tubes, all hollow anode tubes constitute a honeycomb-like first anode. In one embodiment of the present invention, 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 dust is not easy to accumulate on the inner wall of the hollow anode tube. If the cross section of the hollow anode tube is trilateral, 3 dust accumulation surfaces and 3 far-angle dust holding angles can be formed on the inner wall of the hollow anode tube, and the dust holding rate of the hollow anode tube with the structure is highest. If the section of the hollow anode tube is quadrilateral, 4 dust accumulation surfaces and 4 dust holding angles can be obtained, but the spliced structure is unstable. If the section of the hollow anode tube is hexagonal, 6 dust accumulation surfaces, 6 dust holding angles and the dust accumulation surfaces and the dust holding rate are balanced. If the cross section of the hollow anode tube is more polygonal, more dust accumulation sides can be obtained, but the dust holding rate is lost. In one embodiment of the present invention, the diameter of the inscribed circle of the hollow anode tube is in the range of 5mm to 400mm.
In one embodiment, the present invention provides a method for reducing air dust removal electric field coupling, comprising the steps of:
an ionization dust removal electric field generated by passing air through a dust removal electric field anode and a dust removal electric field cathode;
and selecting the dust removing electric field anode or/and the dust removing electric field cathode.
In an embodiment of the present invention, the size of the dust removing electric field anode and/or the dust removing electric field cathode is selected to make the electric field coupling frequency less than or equal to 3.
Specifically, the ratio of the dust collection area of the dust collection electric field anode to the discharge area of the dust collection electric field cathode is selected. Preferably, the ratio of the dust accumulation area of the dust removal electric field anode to the discharge area of the dust removal electric field cathode is selected to be 1.667:1-1680:1.
more preferably, the ratio of the dust accumulation area of the dust removal electric field anode to the discharge area of the dust removal electric field cathode is selected to be 6.67-56.67: 1.
in an embodiment of the present invention, the diameter of the dust-removing electric field cathode is 1-3 mm, and the pole distance between the dust-removing electric field anode and the dust-removing electric field cathode is 2.5-139.9 mm; the ratio of the dust accumulation area of the dust removal electric field anode to the discharge area of the dust removal electric field cathode is 1.667:1-1680:1.
preferably, the pole spacing between the dust removing electric field anode and the dust removing electric field cathode is selected to be less than 150mm.
Preferably, the pole spacing between the dust removing electric field anode and the dust removing electric field cathode is selected to be 2.5-139.9 mm. More preferably, the electrode distance between the dust removing electric field anode and the dust removing electric field cathode is selected to be 5.0-100 mm.
Preferably, the length of the anode of the dedusting electric field is selected to be 10-180 mm. More preferably, the length of the anode of the dedusting electric field is selected to be 60-180 mm.
Preferably, the length of the cathode of the dedusting electric field is selected to be 30-180 mm. More preferably, the length of the cathode of the dedusting electric field is selected to be 54-176 mm.
In an embodiment of the invention, the dust removing electric field cathode includes a plurality of cathode wires. The diameter of the cathode wire can be 0.1mm-20mm, and the size parameter is adjusted according to the application occasion and the dust accumulation requirement. In one embodiment of the invention the diameter of the cathode filament is not more than 3mm. In one embodiment of the invention, the cathode wire is made of metal wires or alloy wires which are easy to discharge, and is temperature-resistant, capable of supporting self weight and stable in electrochemistry. In one embodiment of the present invention, the cathode wire is made of titanium. The specific shape of the cathode wire is adjusted according to the shape of the dust removing electric field anode, for example, if the dust accumulation surface of the dust removing electric field anode is a plane, the section of the cathode wire is circular; if the dust accumulation surface of the dust removal electric field anode is an arc surface, the cathode wire needs to be designed into a multi-surface shape. The length of the cathode wire is adjusted according to the anode of the dust removing electric field.
In an embodiment of the invention, the dust removing electric field cathode includes a plurality of cathode bars. In one embodiment of the invention, the diameter of the cathode rod is not more than 3mm. In one embodiment of the present invention, a metal rod or an alloy rod that is easily discharged is used as the cathode rod. The shape of the cathode rod can be needle-shaped, polygonal, burr-shaped, threaded rod-shaped or columnar, etc. The shape of the cathode rod can be adjusted according to the shape of the dust removing electric field anode, for example, if the dust collecting surface of the dust removing electric field anode is a plane, the section of the cathode rod needs to be designed into a round shape; if the dust accumulation surface of the dust removal electric field anode is an arc surface, the cathode rod needs to be designed into a multi-surface shape.
In an embodiment of the present invention, the electric field dust removing cathode is disposed inside the electric field dust removing anode.
In one embodiment of the invention, the dedusting electric field anode comprises one or more hollow anode tubes arranged in parallel. When there are a plurality of hollow anode tubes, all hollow anode tubes form a honeycomb-shaped dust removal electric field anode. In one embodiment of the present invention, the hollow anode tube may have a circular or polygonal cross section. If the section of the hollow anode tube is circular, a uniform electric field can be formed between the dust removal electric field anode and the dust removal electric field cathode, and dust is not easy to accumulate on the inner wall of the hollow anode tube. If the cross section of the hollow anode tube is trilateral, 3 dust accumulation surfaces and 3 far-angle dust holding angles can be formed on the inner wall of the hollow anode tube, and the dust holding rate of the hollow anode tube with the structure is highest. If the section of the hollow anode tube is quadrilateral, 4 dust accumulation surfaces and 4 dust holding angles can be obtained, but the spliced structure is unstable. If the section of the hollow anode tube is hexagonal, 6 dust accumulation surfaces, 6 dust holding angles and the dust accumulation surfaces and the dust holding rate are balanced. If the cross section of the hollow anode tube is more polygonal, more dust accumulation sides can be obtained, but the dust holding rate is lost. In one embodiment of the present invention, the diameter of the inscribed circle of the hollow anode tube is in the range of 5mm to 400mm.
In one embodiment, the present invention provides a method for dedusting air, comprising the steps of:
1) Adsorbing particles in the air by using an ionization dust removal electric field;
2) An electric field of ionization dust removal is used to charge the electret element.
In an embodiment of the invention, the electret element is located close to the electric field device outlet or the electret element is located at the electric field device outlet.
In an embodiment of the present invention, the dust removing electric field anode and the dust removing electric field cathode form a flow channel, and the electret element is disposed in the flow channel.
In an embodiment of the invention, the flow channel comprises a flow channel outlet, and the electret element is close to the flow channel outlet or is arranged at the flow channel outlet.
In one embodiment of the present invention, when the ionization dust removal electric field has no power-on driving voltage, the charged electret element is utilized to adsorb particles in the air.
In one embodiment of the invention, the charged electret element is replaced with a new electret element after it adsorbs some particulate matter in the air.
In one embodiment of the invention, the ionized dust removing electric field is restarted to adsorb particulate matters in the air after being replaced by a new electret element, and the new electret element is charged.
In one embodiment of the invention, the electret element material comprises an inorganic compound having electret properties. The electret performance refers to the capability of the electret element that the electret element is charged after being charged by an external power supply and still maintains a certain charge under the condition that the electret element is completely separated from the power supply, so that the electret element can serve as an electrode of an electric field.
In an embodiment of the present invention, the inorganic compound is selected from one or more of an oxygen-containing compound, a nitrogen-containing compound, and glass fiber.
In an embodiment of the present invention, the oxygen-containing compound is selected from one or more of metal-based oxides, oxygen-containing complexes, oxygen-containing inorganic heteropolyacid salts.
In an embodiment of the present invention, the metal-based oxide is selected from one or more of aluminum oxide, zinc oxide, zirconium oxide, titanium oxide, barium oxide, tantalum oxide, silicon oxide, lead oxide, and tin oxide.
In an embodiment of the present invention, the metal-based oxide is alumina.
In an embodiment of the present invention, the oxygen-containing compound is selected from one or more of titanium zirconium composite oxide or titanium barium composite oxide.
In an embodiment of the present invention, the oxygen-containing inorganic heteropolyacid salt is selected from one or more of zirconium titanate, lead zirconate titanate or barium titanate.
In one embodiment of the present invention, the nitrogen-containing compound is silicon nitride.
In one embodiment of the invention, the electret element material comprises an organic compound having electret properties. The electret performance refers to the capability of the electret element that the electret element is charged after being charged by an external power supply and still maintains a certain charge under the condition that the electret element is completely separated from the power supply, so that the electret element can serve as an electrode of an electric field.
In an embodiment of the present invention, the organic compound is selected from one or more of a fluoropolymer, a polycarbonate, PP, PE, PVC, a natural wax, a resin, and a rosin.
In one embodiment of the present invention, the fluoropolymer is selected from one or more of Polytetrafluoroethylene (PTFE), polytetrafluoroethylene (Teflon-FEP), soluble Polytetrafluoroethylene (PFA), polyvinylidene fluoride (PVDF).
In one embodiment of the invention, the fluoropolymer is polytetrafluoroethylene.
In an embodiment of the present invention, the present invention provides an air dust removal method, including the following steps: the air is subjected to air ionization dust removal to remove or reduce ozone generated by the air ionization dust removal.
In one embodiment of the present invention, ozone generated by ionization and dust removal of air is digested with ozone.
In an embodiment of the present invention, the ozone digestion is at least one selected from ultraviolet digestion and catalytic digestion.
The air dust removal system and method of the present invention are further illustrated by the following specific examples.
Example 1
Referring to fig. 1, a schematic structure of an air dust removal system in an embodiment is shown. The air dust removal system 101 includes an electric field device inlet 1011, a centrifugal separation mechanism 1012, a first water filtering mechanism 1013, an electric field device 1014, an insulation mechanism 1015, a wind homogenizing device, a second water filtering mechanism 1017, and/or an ozone mechanism 1018.
The first water filtering mechanism 1013 and/or the second water filtering mechanism 1017 are optional in the present invention, that is, the air dust removing system provided by the present invention may include the first water filtering mechanism 1013 and/or the second water filtering mechanism 1017, or may not include the first water filtering mechanism 1013 and/or the second water filtering mechanism 1017.
As shown in fig. 1, the electric field device inlet 1011 is disposed on the inlet wall of the centrifugal separation mechanism 1012 to receive gas with particulate matter.
The centrifugal separation mechanism 1012 provided at the lower end of the air dust removal system 101 is a conical cylinder. The junction of the cone and the electric field device 1014 is a vent with a first filter layer for filtering particulate matter disposed thereon. The bottom of the conical cylinder is provided with a powder outlet for receiving the particles.
Specifically, the particulate-containing gas will change from linear to circular motion as it enters the centrifugal separation mechanism 1012 from the electric field device inlet 1011, typically at a velocity of 12-30 m/s. The vast majority of the swirling air flow flows helically down the walls from the cylinder towards the cone. In addition, the particles are thrown against the inner wall of the separating mechanism by centrifugal force, and once the particles are contacted with the inner wall, the momentum of downward axial velocity near the inner wall falls along the wall surface and is discharged from the powder outlet. The descending outward airflow continuously flows into the center part of the separating mechanism during the descending process to form centripetal radial airflow, and the part of the airflow forms upward rotating inward airflow. The rotation directions of the inner and outer rotational flows are the same. Finally, the purified gas is discharged into the electric field device 1014 through a gas outlet and a first filter screen (not shown), and a part of the finer dust particles which are not separated cannot escape.
The first water filtering mechanism 1013 disposed in the centrifugal separation mechanism 1012 comprises a first electrode disposed at the inlet 1011 of the electric field device, which is a conductive mesh plate for conducting electrons to liquid water after power-up. The second electrode for adsorbing the charged liquid water is in this embodiment the anode dust-collecting part of the electric field device 1014, i.e. the dust-removing electric field anode 10141.
Referring to fig. 2, another embodiment of a first water filtering mechanism disposed in the air dust removal system is shown. The first electrode 10131 of the first water filtering mechanism is disposed at the air inlet, and the first electrode 10131 is a conductive screen plate with negative potential. Meanwhile, the second electrode 10132 of the present embodiment is disposed in the air intake device in a planar mesh shape, and the second electrode 10132 has a positive potential, and the second electrode 10132 is also called a collector. In this embodiment, the second electrode 10132 is in a planar mesh shape, and the first electrode 10131 is parallel to the second electrode 10132. In this embodiment, a mesh electric field is formed between the first electrode 10131 and the second electrode 10132. In addition, the first electrode 10131 is a mesh structure made of wire, and the first electrode 10131 is made of wire mesh. The area of the second electrode 10132 is larger than the area of the first electrode 10131 in this embodiment. The electric field device 1014 comprises a dust-removing electric field anode 10141 and a dust-removing electric field cathode 10142 arranged in the dust-removing electric field anode 10141, wherein an asymmetric electrostatic field is formed between the dust-removing electric field anode 10141 and the dust-removing electric field cathode 10142, and after the gas containing the particles enters the electric field device 1014 through the exhaust port, the gas is ionized due to the discharge of the dust-removing electric field cathode 10142, so that the particles obtain negative charges, move towards the dust-removing electric field anode 10141 and are deposited on the dust-removing electric field anode 10141.
Specifically, the inside of the dust removal electric field anode 10141 is composed of a honeycomb-shaped hollow anode tube bundle group, and the shape of the port of the anode tube bundle is hexagonal.
The dust-removing electric field cathode 10142 comprises a plurality of electrode bars which are correspondingly penetrated through each anode tube bundle in the anode tube bundle group one by one, wherein the electrode bars are in the shape of needles, multiple angles, burrs, threaded rods or columns.
In this embodiment, the air outlet end of the electric field cathode 10142 is lower than the air outlet end of the electric field anode 10141, and the air outlet end of the electric field cathode 10142 is flush with the air inlet end of the electric field anode 10141, so that an accelerating electric field is formed inside the electric field device 1014.
The insulation mechanism 1015 includes an insulation portion and a heat insulation portion. The insulating part is made of ceramic material or glass material. The insulating part is an umbrella-shaped string ceramic column or glass column or a columnar string ceramic column or glass column, and glaze is hung inside and outside the umbrella or inside and outside the column.
As shown in fig. 1, in an embodiment of the present invention, a de-dusting electric field cathode 10142 is mounted on a cathode support plate 10143, and the cathode support plate 10143 and the de-dusting electric field anode 10141 are connected by an insulation mechanism 1015. The insulation mechanism 1015 is used to insulate between the cathode support plate 10143 and the de-dusting electric field anode 10141. In one embodiment of the present invention, the de-dusting electric field anode 10141 comprises a first anode portion 101412 and a second anode portion 101411, wherein the first anode portion 101412 is adjacent to the electric field device inlet and the second anode portion 101411 is adjacent to the electric field device outlet. The cathode support plate and the insulation mechanism are arranged between the first anode portion 101412 and the second anode portion 101411, that is, the insulation mechanism 1015 is arranged in the middle of the ionization electric field or in the middle of the dedusting electric field cathode 10142, so that a good support effect can be achieved on the dedusting electric field cathode 10142, and a fixing effect relative to the dedusting electric field cathode 10141 can be achieved on the dedusting electric field cathode 10142, so that a set distance can be kept between the dedusting electric field cathode 10142 and the dedusting electric field anode 10141.
Referring to fig. 3A, 3B and 3C, three implementation structure diagrams of the wind balancing device are shown.
As shown in fig. 3A, when the shape of the dust-removing electric field anode is a cylinder, the wind-homogenizing device 1016 is located between the dust-removing system inlet 1011 and the ionization dust-removing electric field formed by the dust-removing electric field anode and the dust-removing electric field cathode, and is composed of a plurality of wind-homogenizing blades 10161 rotating around the center of the dust-removing system inlet 1011. The air homogenizing device can enable air to uniformly pass through an electric field generated by the dust removal electric field anode. Meanwhile, the internal temperature of the dust removal electric field anode can be kept constant, and oxygen is sufficient.
As shown in fig. 3B, when the shape of the dust-removing electric field anode is cubic, the wind-homogenizing device 1020 includes:
the air inlet pipe 10201 is arranged at one side edge of the dust removal electric field anode; a kind of electronic device with high-pressure air-conditioning system
The air outlet pipe 10202 is arranged on the other side edge of the dust removal electric field anode; wherein, the side of the installation air inlet pipe 10201 is opposite to the other side of the installation air outlet pipe 10202.
As shown in fig. 3C, the air equalizing device 1026 may further include a first venturi plate air equalizing mechanism 1028 disposed at an air inlet end of the dust removal electric field anode and a second venturi plate air equalizing mechanism 1030 disposed at an air outlet end of the dust removal electric field anode (the second venturi plate air equalizing mechanism 1030 (as shown in fig. 3D, a top view of the second venturi plate air equalizing mechanism can be seen to be folded), an air inlet hole is formed in the first venturi plate air equalizing mechanism, an air outlet hole is formed in the second venturi plate air equalizing mechanism, and the air inlet hole and the air outlet hole are arranged in a staggered manner, and the front air inlet side and the air outlet face form a cyclone structure.
In this embodiment, a second filter screen is disposed at the joint of the electric field device 1014 and the second water filtering mechanism 1017 for filtering fine particles with smaller particle diameters that are not treated by the electric field device 1014.
The second water filtering mechanism 1017 disposed at the air outlet end includes: the third filter screen, the pivot and hinder the water ball.
The third filter screen is obliquely arranged at the air outlet end through a rotating shaft, and a water blocking ball is arranged at the position of the third filter screen corresponding to the air outlet. The third filter screen is driven to rotate around the rotating shaft by the gas to be entered, a water film is formed on the third filter screen, and the water blocking ball blocks the air outlet end so as to prevent water from being flushed out.
The ozone mechanism 1018 disposed at the air outlet end of the dust-removing electric field system employs a deodorizing lamp.
Example 2
The electric field device shown in fig. 4 comprises a dust removing electric field anode 10141, a dust removing electric field cathode 10142 and an electret element 205, wherein an ionization dust removing electric field is formed when the dust removing electric field anode 10141 and the dust removing electric field cathode 10142 are powered on, the electret element 205 is arranged in the ionization dust removing electric field, and the arrow direction in fig. 4 is the flow direction of the to-be-treated flow. The electret element is arranged at the outlet of the electric field device. The ionizing, dust removing electric field charges the electret element. The electret element has a porous structure, and the material of the electret element is alumina. The inside of the dust removal electric field anode is tubular, the outside of the electret element is tubular, and the electret element is sleeved inside the dust removal electric field anode. The electret element is detachably connected with the dust removing electric field anode.
A method of dedusting air, comprising the steps of:
a) Adsorbing particles in the air by using an ionization dust removal electric field;
b) An electric field of ionization dust removal is used to charge the electret element.
Wherein the electret element is arranged at the outlet of the electric field device; the electret element is made of alumina; when the ionization dedusting electric field has no power-on driving voltage, the charged electret element is utilized to adsorb particles in the air; after the charged electret element adsorbs certain particulate matters in the air, the charged electret element is replaced by a new electret element; after replacement with a new electret element, the ionisation dust removal electric field is restarted to adsorb particulate matters in the air and charge the new electret element.
Example 3
The electric field device as shown in fig. 5 and 6 comprises a dedusting electric field anode 10141, a dedusting electric field cathode 10142 and an electret element 205, wherein the dedusting electric field anode 10141 and the dedusting electric field cathode 10142 form a flow passage 292, and the electret element 205 is arranged in the flow passage 292, and the arrow direction in fig. 5 is the flow direction of the to-be-treated flow. The flow channel 292 includes a flow channel outlet, which is adjacent to the electret element 205. The cross section of the electret element in the flow channel accounts for 10% of the flow channel cross section, as shown in fig. 7, namely S2/(s1+s2) ×100%, wherein the first cross-sectional area S2 is the cross-sectional area of the electret element in the flow channel, the sum of the first cross-sectional area S1 and the second cross-sectional area S2 is the cross-sectional area of the flow channel, and the first cross-sectional area S1 does not include the cross-sectional area of the dust removal electric field cathode 10142. And when the dust removing electric field anode and the dust removing electric field cathode are connected with a power supply, an ionization dust removing electric field is formed. The ionizing, dust removing electric field charges the electret element. The electret element has a porous structure, and the material of the electret element is polytetrafluoroethylene. The inside of the dust removal electric field anode is tubular, the outside of the electret element is tubular, and the electret element is sleeved inside the dust removal electric field anode. The electret element is detachably connected with the dust removing electric field anode.
In an embodiment of the present invention, a method for removing dust from air includes the following steps:
1) Adsorbing particles in the air by using an ionization dust removal electric field;
2) An electric field of ionization dust removal is used to charge the electret element.
Wherein the electret element is adjacent the flow channel outlet; the electret element is made of polytetrafluoroethylene; when the ionization dedusting electric field has no power-on driving voltage, the charged electret element is utilized to adsorb particles in the air; after the charged electret element adsorbs certain particulate matters in the air, the charged electret element is replaced by a new electret element; after replacement with a new electret element, the ionisation dust removal electric field is restarted to adsorb particulate matters in the air and charge the new electret element.
Example 4
As shown in fig. 8, the air dust removal system includes an electric field device including a dust removal electric field anode 10141 and a dust removal electric field cathode 10142, and a deodorizing device 206 for removing or reducing ozone generated by the electric field device, the deodorizing device being between an electric field device outlet and an air dust removal system outlet. The dust removal electric field anode 10141 and the dust removal electric field cathode 10142 are used to generate an ionization dust removal electric field. The ozone eliminating device comprises an ozone eliminator, wherein the ozone eliminator is used for eliminating ozone generated by the electric field device, the ozone eliminator is an ultraviolet ozone eliminator, and the arrow direction in the figure is the flowing direction of air inlet.
An air dust removal method comprising the steps of: and the air is subjected to air ionization dust removal, then ozone digestion is carried out on ozone generated by the air ionization dust removal, and the ozone digestion is ultraviolet digestion.
The ozone removing device is used for removing or reducing ozone generated by the electric field device, and ozone is formed due to the fact that oxygen in the air participates in ionization.
Example 5
The electric field generating unit in this embodiment may be applied to an electric field device, as shown in fig. 9, and includes a dust removing electric field anode 4051 and a dust removing electric field cathode 4052 for generating an electric field, where the dust removing electric field anode 4051 and the dust removing electric field cathode 4052 are respectively electrically connected with two electrodes of a power supply, the power supply is a dc power supply, and the dust removing electric field anode 4051 and the dust removing electric field cathode 4052 are respectively electrically connected with an anode and a cathode of the dc power supply. The electric field dust anode 4051 in this embodiment has a positive potential and the electric field dust cathode 4052 has a negative potential.
In this embodiment, the dc power supply may be a dc high-voltage power supply. A discharge electric field, which is an electrostatic field, is formed between the dust removing electric field anode 4051 and the dust removing electric field cathode 4052.
As shown in fig. 9, 10 and 11, the dust-removing electric field anode 4051 in this embodiment is hollow and regular hexagonal, the dust-removing electric field cathode 4052 is rod-shaped, and the dust-removing electric field cathode 4052 is inserted into the dust-removing electric field anode 4051.
A method of reducing electric field coupling comprising the steps of: the ratio of the dust collection area of the dust collection electric field anode 4051 to the discharge area of the dust collection electric field cathode 4052 was selected to be 6.67:1, 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 60mm, the length of the dust removing electric field cathode 4052 is 54mm, the dust removing electric field anode 4051 comprises a fluid channel, the fluid channel comprises an inlet end and an outlet end, the dust removing electric field cathode 4052 is arranged in the fluid channel, the dust removing electric field cathode 4052 extends along the direction of the dust collecting electrode fluid channel, the inlet end of the dust removing electric field anode 4051 is flush with the near inlet end of the dust removing electric field cathode 4052, an included angle alpha is formed between the outlet end of the dust removing electric field anode 4051 and the near outlet end of the dust removing electric field cathode 4052, and alpha=118 DEG, so that more substances to be treated can be collected under the action of the dust removing electric field anode 4051 and the dust removing electric field cathode 4052, the electric field coupling times are less than or equal to 3, the coupling consumption of the electric field to aerosol, the mist, the loose and smooth particles can be reduced, and the electric field electric energy can be saved by 30-50%.
In this embodiment, the electric field device includes a plurality of electric field stages formed by a plurality of the electric field generating units, so that dust collecting efficiency of the electric field device is effectively improved by using a plurality of dust collecting units. In the same electric field stage, anodes of all the dust removing electric fields are of the same polarity, and cathodes of all the dust removing electric fields are of the same polarity.
The electric field stages are connected in series, the electric field stages in series are connected through a connecting shell, and the distance between the electric field stages of two adjacent stages is larger than 1.4 times of the pole spacing. As shown in fig. 12, the electric field stage has two stages, i.e., a first-stage electric field and a second-stage electric field, which are connected in series through a connection housing.
In this embodiment, the material to be treated may be granular dust, or may be other impurities to be treated, such as aerosol, mist, oil mist, etc.
Example 6
The electric field generating unit in this embodiment may be applied to an electric field device, as shown in fig. 9, and includes a dust removing electric field anode 4051 and a dust removing electric field cathode 4052 for generating an electric field, where the dust removing electric field anode 4051 and the dust removing electric field cathode 4052 are respectively electrically connected with two electrodes of a power supply, the power supply is a dc power supply, and the dust removing electric field anode 4051 and the dust removing electric field cathode 4052 are respectively electrically connected with an anode and a cathode of the dc power supply. The electric field dust anode 4051 in this embodiment has a positive potential and the electric field dust cathode 4052 has a negative potential.
In this embodiment, the dc power supply may be a dc high-voltage power supply. A discharge electric field, which is an electrostatic field, is formed between the dust removing electric field anode 4051 and the dust removing electric field cathode 4052.
In this embodiment, the dust-removing electric field anode 4051 is in a hollow regular hexagonal tube shape, the dust-removing electric field cathode 4052 is in a rod shape, and the dust-removing electric field cathode 4052 is arranged in the dust-removing electric field anode 4051 in a penetrating manner.
A method of reducing electric field coupling comprising the steps of: the ratio of the dust collection area of the dust collection field anode 4051 to the discharge area of the dust collection field cathode 4052 is selected to be 1680:1, the pole distance between a dust removing electric field anode 4051 and a dust removing electric field cathode 4052 is 139.9mm, the length of the dust removing electric field anode 4051 is 180mm, the length of the dust removing electric field cathode 4052 is 180mm, the dust removing electric field anode 4051 comprises a fluid channel, the fluid channel comprises an inlet end and an outlet end, the dust removing electric field cathode 4052 is arranged in the fluid channel, the dust removing electric field cathode 4052 extends along the direction of the dust collecting electrode fluid channel, the inlet end of the dust removing electric field anode 4051 is flush with the near inlet end of the dust removing electric field cathode 4052, the outlet end of the dust removing electric field anode 4051 is flush with the near outlet end of the dust removing electric field cathode 4052, more substances to be treated can be collected under the action of the dust removing electric field anode 4051 and the dust removing electric field cathode 4052, the electric field coupling times are less than or equal to 3, the coupling consumption of an electric field to aerosol, mist, oil mist and loose and smooth particles can be reduced, and electric field electric energy can be saved by 20-40%.
In this embodiment, the material to be treated may be granular dust, or may be other impurities to be treated, such as aerosol, mist, oil mist, etc.
Example 7
The electric field generating unit in this embodiment may be applied to an electric field device, as shown in fig. 9, and includes a dust removing electric field anode 4051 and a dust removing electric field cathode 4052 for generating an electric field, where the dust removing electric field anode 4051 and the dust removing electric field cathode 4052 are respectively electrically connected with two electrodes of a power supply, the power supply is a dc power supply, and the dust removing electric field anode 4051 and the dust removing electric field cathode 4052 are respectively electrically connected with an anode and a cathode of the dc power supply. The electric field dust anode 4051 in this embodiment has a positive potential and the electric field dust cathode 4052 has a negative potential.
In this embodiment, the dc power supply may be a dc high-voltage power supply. A discharge electric field, which is an electrostatic field, is formed between the dust removing electric field anode 4051 and the dust removing electric field cathode 4052.
In this embodiment, the dust-removing electric field anode 4051 is in a hollow regular hexagonal tube shape, the dust-removing electric field cathode 4052 is in a rod shape, and the dust-removing electric field cathode 4052 is arranged in the dust-removing electric field anode 4051 in a penetrating manner.
A method of reducing electric field coupling comprising the steps of: the ratio of the dust collection area of the dust collection electric field anode 4051 to the discharge area of the dust collection electric field cathode 4052 was selected to be 1.667:1, the pole distance between a dust removing electric field anode 4051 and a dust removing electric field cathode 4052 is 2.4mm, the length of the dust removing electric field anode 4051 is 30mm, the length of the dust removing electric field cathode 4052 is 30mm, the dust removing electric field anode 4051 comprises a fluid channel, the fluid channel comprises an inlet end and an outlet end, the dust removing electric field cathode 4052 is arranged in the fluid channel, the dust removing electric field cathode 4052 extends along the direction of the dust collecting electrode fluid channel, the inlet end of the dust removing electric field anode 4051 is flush with the near inlet end of the dust removing electric field cathode 4052, the outlet end of the dust removing electric field anode 4051 is flush with the near outlet end of the dust removing electric field cathode 4052, more substances to be treated can be collected under the action of the dust removing electric field anode 4051 and the dust removing electric field cathode 4052, the electric field coupling times are less than or equal to 3, the coupling consumption of an electric field to aerosol, mist, oil mist and loose and smooth particles can be reduced, and electric field energy can be saved by 10-30%.
In this embodiment, the material to be treated may be granular dust, or may be other impurities to be treated, such as aerosol, mist, oil mist, etc.
Example 8
The electric field generating unit in this embodiment may be applied to an electric field device, as shown in fig. 9, and includes a dust removing electric field anode 4051 and a dust removing electric field cathode 4052 for generating an electric field, where the dust removing electric field anode 4051 and the dust removing electric field cathode 4052 are respectively electrically connected with two electrodes of a power supply, the power supply is a dc power supply, and the dust removing electric field anode 4051 and the dust removing electric field cathode 4052 are respectively electrically connected with an anode and a cathode of the dc power supply. The electric field dust anode 4051 in this embodiment has a positive potential and the electric field dust cathode 4052 has a negative potential.
In this embodiment, the dc power supply may be a dc high-voltage power supply. A discharge electric field, which is an electrostatic field, is formed between the dust removing electric field anode 4051 and the dust removing electric field cathode 4052.
As shown in fig. 9, 10 and 11, in this embodiment, the dust-removing electric field anode 4051 is in a hollow regular hexagonal tubular shape, the dust-removing electric field cathode 4052 is in a rod shape, the dust-removing electric field cathode 4052 is arranged in the dust-removing electric field anode 4051 in a penetrating manner, and the ratio of the dust collection area of the dust-removing electric field anode 4051 to the discharge area of the dust-removing electric field cathode 4052 is 6.67:1, 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 60mm, the length of the dust removing electric field cathode 4052 is 54mm, the dust removing electric field anode 4051 comprises a fluid channel, the fluid channel comprises an inlet end and an outlet end, the dust removing electric field cathode 4052 is arranged in the fluid channel, the dust removing electric field cathode 4052 extends along the direction of the dust collecting electrode fluid channel, the inlet end of the dust removing electric field anode 4051 is flush with the near inlet end of the dust removing electric field cathode 4052, an included angle alpha is formed between the outlet end of the dust removing electric field anode 4051 and the near outlet end of the dust removing electric field cathode 4052, and alpha=118 DEG is further formed, more substances to be treated can be collected under the action of the dust removing electric field anode 4051 and the dust removing electric field cathode 4052, so that the dust collecting efficiency of the dust collecting unit is higher, and the dust collecting efficiency of the typical tail gas particles pm0.23 is 99.99%.
In this embodiment, the electric field device includes a plurality of electric field stages formed by a plurality of the electric field generating units, so that dust collecting efficiency of the electric field device is effectively improved by using a plurality of dust collecting units. In the same electric field stage, anodes of all the dust removing electric fields are of the same polarity, and cathodes of all the dust removing electric fields are of the same polarity.
The electric field stages are connected in series, the electric field stages in series are connected through a connecting shell, and the distance between the electric field stages of two adjacent stages is larger than 1.4 times of the pole spacing. As shown in fig. 12, the electric field stage is two stages, i.e., a first stage electric field 4053 and a second stage electric field 4054, and the first stage electric field 4053 and the second stage electric field 4054 are connected in series through a connection housing 4055.
In this embodiment, the material to be treated may be granular dust, or may be other impurities to be treated, such as aerosol, mist, oil mist, etc.
Example 9
The electric field generating unit in this embodiment may be applied to an electric field device, as shown in fig. 9, and includes a dust removing electric field anode 4051 and a dust removing electric field cathode 4052 for generating an electric field, where the dust removing electric field anode 4051 and the dust removing electric field cathode 4052 are respectively electrically connected with two electrodes of a power supply, the power supply is a dc power supply, and the dust removing electric field anode 4051 and the dust removing electric field cathode 4052 are respectively electrically connected with an anode and a cathode of the dc power supply. The electric field dust anode 4051 in this embodiment has a positive potential and the electric field dust cathode 4052 has a negative potential.
In this embodiment, the dc power supply may be a dc high-voltage power supply. A discharge electric field, which is an electrostatic field, is formed between the dust removing electric field anode 4051 and the dust removing electric field cathode 4052.
In this embodiment, the dust-removing electric field anode 4051 is in a hollow regular hexagonal tubular shape, the dust-removing electric field cathode 4052 is in a rod shape, the dust-removing electric field cathode 4052 is arranged in the dust-removing electric field anode 4051 in a penetrating manner, and the ratio of the dust collecting area of the dust-removing electric field anode 4051 to the discharge area of the dust-removing electric field cathode 4052 is 1680:1, the pole distance 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 180mm, the length of the dust removing electric field cathode 4052 is 180mm, the dust removing electric field anode 4051 comprises a fluid channel, the fluid channel comprises an inlet end and an outlet end, the dust removing electric field cathode 4052 is arranged in the fluid channel, the dust removing electric field cathode 4052 extends along the direction of the dust collecting electrode fluid channel, the inlet end of the dust removing electric field anode 4051 is flush with the near inlet end of the dust removing electric field cathode 4052, the outlet end of the dust removing electric field anode 4051 is flush with the near outlet end of the dust removing electric field cathode 4052, and further more substances to be treated can be collected under the action of the dust removing electric field anode 4051 and the dust removing electric field cathode 4052, so that the dust collecting efficiency of the electric field device is higher, and the dust collecting efficiency of typical tail gas particles pm0.23 is 99.99%.
In this embodiment, the electric field device includes a plurality of electric field stages formed by a plurality of the electric field generating units, so that dust collecting efficiency of the electric field device is effectively improved by using a plurality of dust collecting units. In the same electric field stage, anodes of all the dust removing electric fields are of the same polarity, and cathodes of all the dust removing electric fields are of the same polarity.
In this embodiment, the material to be treated may be granular dust, or may be other impurities to be treated, such as aerosol, mist, oil mist, etc.
Example 10
The electric field generating unit in this embodiment may be applied to an electric field device, as shown in fig. 9, and includes a dust removing electric field anode 4051 and a dust removing electric field cathode 4052 for generating an electric field, where the dust removing electric field anode 4051 and the dust removing electric field cathode 4052 are respectively electrically connected with two electrodes of a power supply, the power supply is a dc power supply, and the dust removing electric field anode 4051 and the dust removing electric field cathode 4052 are respectively electrically connected with an anode and a cathode of the dc power supply. The electric field dust anode 4051 in this embodiment has a positive potential and the electric field dust cathode 4052 has a negative potential.
In this embodiment, the dc power supply may be a dc high-voltage power supply. A discharge electric field, which is an electrostatic field, is formed between the dust removing electric field anode 4051 and the dust removing electric field cathode 4052.
In this embodiment, the dust-removing electric field anode 4051 is in a hollow regular hexagonal tubular shape, the dust-removing electric field cathode 4052 is in a rod shape, the dust-removing electric field cathode 4052 is arranged in the dust-removing electric field anode 4051 in a penetrating manner, and the ratio of the dust collection area of the dust-removing electric field anode 4051 to the discharge area of the dust-removing electric field cathode 4052 is 1.667:1, the electrode distance between the dust removing electric field anode 4051 and the dust removing electric field cathode 4052 is 2.4mm. The length of the dust removing electric field anode 4051 is 30mm, the length of the dust removing electric field cathode 4052 is 30mm, the dust removing electric field anode 4051 comprises a fluid channel, the fluid channel comprises an inlet end and an outlet end, the dust removing electric field cathode 4052 is arranged in the fluid channel, the dust removing electric field cathode 4052 extends along the direction of the dust collecting electrode fluid channel, the inlet end of the dust removing electric field anode 4051 is flush with the near inlet end of the dust removing electric field cathode 4052, the outlet end of the dust removing electric field anode 4051 is flush with the near outlet end of the dust removing electric field cathode 4052, more substances to be treated can be collected under the action of the dust removing electric field anode 4051 and the dust removing electric field cathode 4052, the dust collecting efficiency of the electric field device is higher, and the dust collecting efficiency of typical tail gas particles pm0.23 is 99.99%.
In this embodiment, the dust-removing electric field anode 4051 and the dust-removing electric field cathode 4052 form a plurality of dust-collecting units, so as to effectively improve the dust-collecting efficiency of the electric field device by using the plurality of dust-collecting units.
In this embodiment, the material to be treated may be granular dust, or may be other impurities to be treated, such as aerosol, mist, oil mist, etc.
Example 11
The air dust removal system of this embodiment includes the electric field device of embodiment 8, embodiment 9 or embodiment 10 described above. The air needs to flow through the electric field device firstly, so that dust in the air is effectively removed by the electric field device, the air is ensured to be cleaner, and the impurities such as dust are less.
Example 12
The electric field generating unit in this embodiment may be applied to an electric field device, as shown in fig. 9, and includes a dust removing electric field anode 4051 and a dust removing electric field cathode 4052 for generating an electric field, where the dust removing electric field anode 4051 and the dust removing electric field cathode 4052 are respectively electrically connected with two electrodes of a power supply, the power supply is a dc power supply, and the dust removing electric field anode 4051 and the dust removing electric field cathode 4052 are respectively electrically connected with an anode and a cathode of the dc power supply. The electric field dust anode 4051 in this embodiment has a positive potential and the electric field dust cathode 4052 has a negative potential.
In this embodiment, the dc power supply may be a dc high-voltage power supply. A discharge electric field, which is an electrostatic field, is formed between the dust removing electric field anode 4051 and the dust removing electric field cathode 4052.
In this embodiment, the dust-removing electric field anode 4051 is in a hollow regular hexagonal tubular shape, the dust-removing electric field cathode 4052 is in a rod shape, the dust-removing electric field cathode 4052 is arranged in the dust-removing electric field anode 4051 in a penetrating manner, the dust-removing electric field anode 4051 is 5cm long, the dust-removing electric field cathode 4052 is 5cm long, the dust-removing electric field anode 4051 comprises a fluid channel, the fluid channel comprises an inlet end and an outlet end, the dust-removing electric field cathode 4052 is arranged in the fluid channel, the dust-removing electric field cathode 4052 extends along the direction of the dust-collecting electrode fluid channel, the inlet end of the dust-removing electric field anode 4051 is flush with the near inlet end of the dust-removing electric field cathode 4052, the outlet end of the dust-removing electric field anode 4051 is flush with the near outlet end of the dust-removing electric field cathode 4052, the pole spacing between the dust-removing electric field anode 4051 and the dust-removing electric field cathode 4052 is 9.9mm, and under the action of the dust-removing electric field anode 4052, more substances to be treated can be collected, and the dust-removing electric field anode 4052 is resistant to high-temperature impact, and the dust-collecting efficiency of the dust-removing electric field generating unit is ensured to be higher. The electric field temperature is 200 ℃ and the corresponding dust collection efficiency is 99.9%; the electric field temperature is 400 ℃ and the corresponding dust collection efficiency is 90%; the electric field temperature was 500 ℃ and the dust collection efficiency was 50%.
In this embodiment, the electric field device includes a plurality of electric field stages formed by a plurality of the electric field generating units, so that dust collecting efficiency of the electric field device is effectively improved by using a plurality of dust collecting units. In the same electric field stage, anodes of all the dust removing electric fields are of the same polarity, and cathodes of all the dust removing electric fields are of the same polarity.
In this embodiment, the material to be treated may be granular dust.
Example 13
The electric field generating unit in this embodiment may be applied to an electric field device, as shown in fig. 9, and includes a dust removing electric field anode 4051 and a dust removing electric field cathode 4052 for generating an electric field, where the dust removing electric field anode 4051 and the dust removing electric field cathode 4052 are respectively electrically connected with two electrodes of a power supply, the power supply is a dc power supply, and the dust removing electric field anode 4051 and the dust removing electric field cathode 4052 are respectively electrically connected with an anode and a cathode of the dc power supply. The electric field dust anode 4051 in this embodiment has a positive potential and the electric field dust cathode 4052 has a negative potential.
In this embodiment, the dc power supply may be a dc high-voltage power supply. A discharge electric field, which is an electrostatic field, is formed between the dust removing electric field anode 4051 and the dust removing electric field cathode 4052.
In this embodiment, the dust-removing electric field anode 4051 is in a hollow regular hexagonal tubular shape, the dust-removing electric field cathode 4052 is in a rod shape, the dust-removing electric field cathode 4052 is arranged in the dust-removing electric field anode 4051 in a penetrating manner, the dust-removing electric field anode 4051 is 9cm long, the dust-removing electric field cathode 4052 is 9cm long, the dust-removing electric field anode 4051 comprises a fluid channel, the fluid channel comprises an inlet end and an outlet end, the dust-removing electric field cathode 4052 is arranged in the fluid channel, the dust-removing electric field cathode 4052 extends along the direction of the dust-collecting electrode fluid channel, the inlet end of the dust-removing electric field anode 4051 is flush with the near inlet end of the dust-removing electric field cathode 4052, the outlet end of the dust-removing electric field anode 4051 is flush with the near outlet end of the dust-removing electric field cathode 4052, the pole spacing between the dust-removing electric field anode 4051 and the dust-removing electric field cathode 4052 is 139.9mm, and under the action of the dust-removing electric field anode 4051 and the dust-removing electric field cathode 4052, more substances to be collected, and the dust-removing electric field cathode 4052 is resistant to high-temperature impact, and the dust-resistant to be more substances to be processed, and the dust-collecting efficiency of the dust-removing electric field generating unit is ensured to be higher. The electric field temperature is 200 ℃ and the corresponding dust collection efficiency is 99.9%; the electric field temperature is 400 ℃ and the corresponding dust collection efficiency is 90%; the electric field temperature was 500 ℃ and the dust collection efficiency was 50%.
In this embodiment, the electric field device includes a plurality of electric field stages formed by a plurality of the electric field generating units, so that dust collecting efficiency of the electric field device is effectively improved by using a plurality of dust collecting units. In the same electric field stage, anodes of all storage electric fields are of the same polarity, and cathodes of all dust removing electric fields are of the same polarity.
In this embodiment, the material to be treated may be granular dust.
Example 14
The electric field generating unit in this embodiment may be applied to an electric field device, as shown in fig. 9, and includes a dust removing electric field anode 4051 and a dust removing electric field cathode 4052 for generating an electric field, where the dust removing electric field anode 4051 and the dust removing electric field cathode 4052 are respectively electrically connected with two electrodes of a power supply, the power supply is a dc power supply, and the dust removing electric field anode 4051 and the dust removing electric field cathode 4052 are respectively electrically connected with an anode and a cathode of the dc power supply. The electric field dust anode 4051 in this embodiment has a positive potential and the electric field dust cathode 4052 has a negative potential.
In this embodiment, the dc power supply may be a dc high-voltage power supply. A discharge electric field, which is an electrostatic field, is formed between the dust removing electric field anode 4051 and the dust removing electric field cathode 4052.
In this embodiment, the dust-removing electric field anode 4051 is in a hollow regular hexagonal tubular shape, the dust-removing electric field cathode 4052 is in a rod shape, the dust-removing electric field cathode 4052 is arranged in the dust-removing electric field anode 4051 in a penetrating manner, the dust-removing electric field anode 4051 is 1cm long, the dust-removing electric field cathode 4052 is 1cm long, the dust-removing electric field anode 4051 comprises a fluid channel, the fluid channel comprises an inlet end and an outlet end, the dust-removing electric field cathode 4052 is arranged in the fluid channel, the dust-removing electric field cathode 4052 extends along the direction of the dust-collecting electrode fluid channel, the inlet end of the dust-removing electric field anode 4051 is flush with the near inlet end of the dust-removing electric field cathode 4052, the outlet end of the dust-removing electric field anode 4051 is flush with the near outlet end of the dust-removing electric field cathode 4052, the pole spacing between the dust-removing electric field anode 4051 and the dust-removing electric field cathode 4052 is 2.4mm, and under the action of the dust-removing electric field anode 4052, more substances to be treated can be collected, and the dust-removing electric field anode 4052 is resistant to high-temperature impact, and the dust-collecting efficiency of the dust-removing electric field generating unit is ensured to be higher. The electric field temperature is 200 ℃ and the corresponding dust collection efficiency is 99.9%; the electric field temperature is 400 ℃ and the corresponding dust collection efficiency is 90%; the electric field temperature was 500 ℃ and the dust collection efficiency was 50%.
In this embodiment, the electric field device includes a plurality of electric field stages formed by a plurality of the electric field generating units, so that dust collecting efficiency of the electric field device is effectively improved by using a plurality of dust collecting units. In the same electric field stage, anodes of all the dust removing electric fields are of the same polarity, and cathodes of all the dust removing electric fields are of the same polarity.
The electric field stages are connected in series, the electric field stages in series are connected through a connecting shell, and the distance between the electric field stages of two adjacent stages is larger than 1.4 times of the pole spacing. The electric field level is two-stage, namely a first-stage electric field and a second-stage electric field, and the first-stage electric field and the second-stage electric field are connected in series through a connecting shell.
In this embodiment, the material to be treated may be granular dust.
Example 15
The electric field generating unit in this embodiment may be applied to an electric field device, as shown in fig. 9, and includes a dust removing electric field anode 4051 and a dust removing electric field cathode 4052 for generating an electric field, where the dust removing electric field anode 4051 and the dust removing electric field cathode 4052 are respectively electrically connected with two electrodes of a power supply, the power supply is a dc power supply, and the dust removing electric field anode 4051 and the dust removing electric field cathode 4052 are respectively electrically connected with an anode and a cathode of the dc power supply. The electric field dust anode 4051 in this embodiment has a positive potential and the electric field dust cathode 4052 has a negative potential.
In this embodiment, the dc power supply may be a dc high-voltage power supply. A discharge electric field, which is an electrostatic field, is formed between the dust removing electric field anode 4051 and the dust removing electric field cathode 4052.
As shown in fig. 9 and 10, in this embodiment, the dust-removing electric field anode 4051 is in a hollow regular hexagonal tubular shape, the dust-removing electric field cathode 4052 is in a rod shape, the dust-removing electric field cathode 4052 is arranged in the dust-removing electric field anode 4051 in a penetrating manner, the dust-removing electric field anode 4051 is 3cm long, the dust-removing electric field cathode 4052 is 2cm long, 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 arranged in the fluid channel, the dust-removing electric field cathode 4052 extends along the direction of the dust-collecting electrode fluid channel, the inlet end of the dust-removing electric field anode 4051 is flush with the near inlet end of the dust-removing electric field cathode 4052, an included angle α is formed between the outlet end of the dust-removing electric field anode 4051 and the near outlet end of the dust-removing electric field cathode 4052, and α=90°, the pole spacing between the dust-removing electric field anode 4051 and the dust-removing electric field cathode 4052 is 20mm, and under the action of the dust-removing electric field anode 4052, the dust-removing electric field anode 4051 and the dust-removing electric field cathode 4052 are made resistant to high-temperature impact, and more substances to be collected, and the dust to be processed can be collected, and the dust-collecting efficiency of the dust-collecting unit is ensured. The electric field temperature is 200 ℃ and the corresponding dust collection efficiency is 99.9%; the electric field temperature is 400 ℃ and the corresponding dust collection efficiency is 90%; the electric field temperature was 500 ℃ and the dust collection efficiency was 50%.
In this embodiment, the electric field device includes a plurality of electric field stages formed by a plurality of the electric field generating units, so that dust collecting efficiency of the electric field device is effectively improved by using a plurality of dust collecting units. In the same electric field level, the dust collection electrodes have the same polarity, and the discharge electrodes have the same polarity.
The electric field stages are connected in series, the electric field stages in series are connected through a connecting shell, and the distance between the electric field stages of two adjacent stages is larger than 1.4 times of the pole spacing. As shown in fig. 12, the electric field stage has two stages, i.e., a first-stage electric field and a second-stage electric field, which are connected in series through a connection housing.
In this embodiment, the material to be treated may be granular dust.
Example 16
The air dust removal system of this embodiment includes the electric field device of embodiment 12, embodiment 13, embodiment 14 or embodiment 15 described above. The air needs to flow through the electric field device firstly, so that dust in the air is effectively removed by the electric field device, and the air is cleaner, and contains less dust and other impurities.
Example 17
The electric field device in this embodiment can be applied to an air dust removal system, and includes a dust removal electric field cathode 5081 and a dust removal electric field anode 5082 electrically connected to a cathode and an anode of a dc power supply, respectively, and an auxiliary electrode 5083 electrically connected to the anode of the dc power supply. The electric field cathode 5081 in this embodiment has a negative potential, and the electric field anode 5082 and the auxiliary electrode 5083 have positive potentials.
Meanwhile, as shown in fig. 13, the auxiliary electrode 5083 is fixedly connected with the dust removing electric field anode 5082 in the present embodiment. After the electric field anode 5082 is electrically connected to the anode of the dc power supply, the auxiliary electrode 5083 is electrically connected to the anode of the dc power supply, and the auxiliary electrode 5083 and the electric field anode 5082 have the same positive potential.
As shown in fig. 13, the auxiliary electrode 5083 may extend in the front-rear direction in the present embodiment, that is, the length direction of the auxiliary electrode 5083 may be the same as the length direction of the dust removing electric field anode 5082.
As shown in fig. 13, in this embodiment, the dust-removing electric field anode 5082 is tubular, the dust-removing electric field cathode 5081 is rod-shaped, and the dust-removing electric field cathode 5081 is disposed in the dust-removing electric field anode 5082. In this embodiment, the auxiliary electrode 5083 is also tubular, and the auxiliary electrode 5083 and the dust-removing electric field anode 5082 form an anode tube 5084. The front end of the anode tube 5084 is flush with the electric field dust removing cathode 5081, the rear end of the anode tube 5084 is extended rearward beyond the rear end of the electric field dust removing cathode 5081, and the portion of the anode tube 5084 extended rearward beyond the electric field dust removing cathode 5081 is the auxiliary electrode 5083. That is, in the present 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 located opposite to each other in the front-rear direction; the auxiliary electrode 5083 is located behind the electric field dust removal anode 5082 and the electric field dust removal cathode 5081. In this way, an auxiliary electric field is formed between the auxiliary electrode 5083 and the dust removing electric field cathode 5081, which applies a rearward force to the flow of negatively charged oxygen ions between the dust removing electric field anode 5082 and the dust removing electric field cathode 5081, so that the flow of negatively charged oxygen ions between the dust removing electric field anode 5082 and the dust removing electric field cathode 5081 has a rearward moving speed. When the gas containing the substance to be treated flows into the anode tube 5084 from front to back, the oxygen ions with negative charges are combined with the substance to be treated in the process of moving to the dedusting electric field anode 5082 and back, and the oxygen ions have a backward moving speed, when being combined with the substance to be treated, the oxygen ions cannot generate stronger collision, so that the stronger collision can be avoided, the larger energy consumption is avoided, the oxygen ions are easy to combine with the substance to be treated, the charge efficiency of the substance to be treated in the gas is higher, and more substances to be treated can be collected under the action of the dedusting electric field anode 5082 and the anode tube 5084, and the dedusting efficiency of the electric field device is higher.
In addition, as shown in fig. 13, an angle α is formed between the rear end of the anode tube 5084 and the rear end of the dust-removing electric field cathode 5081 in this embodiment, and 0 ° < α.ltoreq.125 °, or 45 °. Ltoreq.α.ltoreq.125 °, or 60 °. Ltoreq.α.ltoreq.100 °, or α=90°.
In this embodiment, the dust-removing electric field anode 5082, the auxiliary electrode 5083, and the dust-removing electric field cathode 5081 form a dust-removing unit, and the number of the dust-removing units is plural, so that the dust-removing efficiency of the electric field device is effectively improved by using plural dust-removing units.
In this embodiment, the material to be treated may be granular dust, or other impurities to be treated.
In this embodiment, the dc power supply may be a dc high-voltage power supply. A discharge electric field, which is an electrostatic field, is formed between the dust-removing electric field cathode 5081 and the dust-removing electric field anode 5082. Without the auxiliary electrode 5083, the ion flow in the electric field between the dust-removing electric field cathode 5081 and the dust-removing electric field anode 5082 is in the direction perpendicular to the electrodes, and flows back and forth between the two electrodes, and causes the ion to be consumed back and forth between the electrodes. For this reason, the present embodiment uses the auxiliary electrode 5083 to shift the relative positions of the electrodes, so as to form a relative imbalance between the dedusting electric field anode 5082 and the dedusting electric field cathode 5081, and this imbalance deflects the ion flow in the electric field. The electric field device forms an electric field that can direct an ion flow by using the auxiliary electrode 5083. The electric field device described above is also referred to as an accelerating electric field device in this embodiment. The electric field device has the advantages that the collection rate of the particles entering the electric field along the ion flow direction is nearly doubled compared with that of the particles entering the electric field along the counter ion flow direction, so that the dust accumulation efficiency of the electric field is improved, and the electric power consumption of the electric field is reduced. In addition, the main reason that the dust collection efficiency of the dust collection electric field in the prior art is lower is that the direction of dust entering the electric field is opposite to or vertically crossed with the direction of ion flow in the electric field, so that the mutual collision of the dust and the ion flow is severe, larger energy consumption is generated, the charge efficiency is influenced, the dust collection efficiency of the electric field in the prior art is further reduced, and the energy consumption is increased.
When the electric field device is used for collecting dust in gas, the gas and the dust enter an electric field along the ion flow direction, so that the dust is sufficiently charged, and the electric field consumption is small; the dust collection efficiency of the monopole electric field can reach 99.99 percent. When gas and dust enter an electric field in the reverse ion flow direction, the dust charge is insufficient, the electric consumption of the electric field is increased, and the dust collection efficiency is 40% -75%. In addition, the ion flow formed by the electric field device in the embodiment is beneficial to fluid transportation, oxygenation, heat exchange and the like of the unpowered fan.
Example 18
The electric field device in this embodiment can be applied to an air dust removal system, and includes a dust removal electric field cathode 5081 and a dust removal electric field anode 5082 electrically connected to the cathode and the anode of the dc power supply, respectively, and an auxiliary electrode 5083 electrically connected to the cathode of the dc power supply. In this embodiment, the auxiliary electrode 5083 and the electric field cathode 5081 are both negative, and the electric field anode 5082 is positive.
In this embodiment, the auxiliary electrode 5083 may be fixedly connected to the cathode 5081 of the dust removing electric field. Thus, after the electric connection between the dust removing electric field cathode 5081 and the cathode of the dc power supply is achieved, the electric connection between the auxiliary electrode 5083 and the cathode of the dc power supply is also achieved. Meanwhile, the auxiliary electrode 5083 extends in the front-rear direction in this embodiment.
In this embodiment, the dust-removing electric field anode 5082 is tubular, the dust-removing electric field cathode 5081 is rod-shaped, and the dust-removing electric field cathode 5081 is disposed in the dust-removing electric field anode 5082. Meanwhile, in this embodiment, the auxiliary electrode 5083 is also rod-shaped, and the auxiliary electrode 5083 and the dust-removing electric field cathode 5081 form a cathode rod. The front end of the cathode rod is protruded forward from the front end of the electric field dust removing anode 5082, and the portion of the cathode rod protruded forward from the electric field dust removing anode 5082 is the auxiliary electrode 5083. That is, in the present 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 located opposite to each other in the front-rear direction; the auxiliary electrode 5083 is located in front of the electric field dust removal anode 5082 and the electric field dust removal cathode 5081. In this way, an auxiliary electric field is formed between the auxiliary electrode 5083 and the dust removing electric field anode 5082, which exerts a rearward force on the flow of negatively charged oxygen ions between the dust removing electric field anode 5082 and the dust removing electric field cathode 5081, so that the flow of negatively charged oxygen ions between the dust removing electric field anode 5082 and the dust removing electric field cathode 5081 has a rearward moving velocity. When the gas containing the substance to be treated flows into the tubular dedusting electric field anode 5082 from front to back, oxygen ions with negative charges are combined with the substance to be treated in the process of moving backwards towards the dedusting electric field anode 5082, and as the oxygen ions have backward moving speed, the oxygen ions cannot generate stronger collision when being combined with the substance to be treated, so that larger energy consumption caused by stronger collision is avoided, the oxygen ions are easy to be combined with the substance to be treated, the charge efficiency of the substance to be treated in the gas is higher, and more substances to be treated can be collected under the action of the dedusting electric field anode 5082, and the dedusting efficiency of the electric field device is ensured to be higher.
In this embodiment, the dust-removing electric field anode 5082, the auxiliary electrode 5083, and the dust-removing electric field cathode 5081 form a dust-removing unit, and the number of the dust-removing units is plural, so that the dust-removing efficiency of the electric field device is effectively improved by using plural dust-removing units.
In this embodiment, the material to be treated may be granular dust, or other impurities to be treated.
Example 19
As shown in fig. 14, the electric field device in this embodiment can be applied to an air dust removing system, and the auxiliary electrode 5083 extends in the left-right direction. The length direction of the auxiliary electrode 5083 in this embodiment is different from the length direction of the electric field dust removal anode 5082 and the electric field dust removal cathode 5081. And the auxiliary electrode 5083 may be perpendicular to the dedusting electric field anode 5082.
In this embodiment, the dust removing electric field cathode 5081 and the dust removing electric field anode 5082 are respectively electrically connected with the cathode and the anode of the dc power supply, and the auxiliary electrode 5083 is electrically connected with the anode of the dc power supply. The electric field cathode 5081 in this embodiment has a negative potential, and the electric field anode 5082 and the auxiliary electrode 5083 have positive potentials.
As shown in fig. 14, in the present embodiment, the electric field dust collection cathode 5081 and the electric field dust collection anode 5082 are positioned opposite to each other in the front-rear direction, and the auxiliary electrode 5083 is positioned behind the electric field dust collection anode 5082 and the electric field dust collection cathode 5081. In this way, an auxiliary electric field is formed between the auxiliary electrode 5083 and the dust removing electric field cathode 5081, which applies a rearward force to the flow of negatively charged oxygen ions between the dust removing electric field anode 5082 and the dust removing electric field cathode 5081, so that the flow of negatively charged oxygen ions between the dust removing electric field anode 5082 and the dust removing electric field cathode 5081 has a rearward moving speed. When the gas containing the substance to be treated flows into the electric field between the dust removing electric field anode 5082 and the dust removing electric field cathode 5081 from front to back, oxygen ions with negative charges are combined with the substance to be treated in the process of moving backwards towards the dust removing electric field anode 5082, and the oxygen ions have a backward moving speed, when being combined with the substance to be treated, the oxygen ions cannot generate stronger collision between the oxygen ions and the substance to be treated, so that larger energy consumption caused by stronger collision is avoided, the oxygen ions are easy to combine with the substance to be treated, the charge efficiency of the substance to be treated in the gas is higher, and more substances to be treated can be collected under the action of the dust removing electric field anode 5082, and the dust removing efficiency of the electric field device is higher.
Example 20
As shown in fig. 15, the electric field device in this embodiment can be applied to an air dust removing system, and the auxiliary electrode 5083 extends in the left-right direction. The length direction of the auxiliary electrode 5083 in this embodiment is different from the length direction of the electric field dust removal anode 5082 and the electric field dust removal cathode 5081. And the auxiliary electrode 5083 may be perpendicular to the dedusting electric field cathode 5081.
In this embodiment, the dust removing electric field cathode 5081 and the dust removing electric field anode 5082 are respectively electrically connected with the cathode and the anode of the dc power supply, and the auxiliary electrode 5083 is electrically connected with the cathode of the dc power supply. In this embodiment, the dedusting electric field cathode 5081 and the auxiliary electrode 5083 have negative potentials, and the dedusting electric field anode 5082 has positive potentials.
As shown in fig. 15, in the present embodiment, the electric field dust collection cathode 5081 and the electric field dust collection anode 5082 are positioned opposite to each other in the front-rear direction, and the auxiliary electrode 5083 is positioned in front of the electric field dust collection anode 5082 and the electric field dust collection cathode 5081. In this way, an auxiliary electric field is formed between the auxiliary electrode 5083 and the dust removing electric field anode 5082, which exerts a rearward force on the flow of negatively charged oxygen ions between the dust removing electric field anode 5082 and the dust removing electric field cathode 5081, so that the flow of negatively charged oxygen ions between the dust removing electric field anode 5082 and the dust removing electric field cathode 5081 has a rearward moving velocity. When the gas containing the substance to be treated flows into the electric field between the dust removing electric field anode 5082 and the dust removing electric field cathode 5081 from front to back, oxygen ions with negative charges are combined with the substance to be treated in the process of moving backwards towards the dust removing electric field anode 5082, and the oxygen ions have a backward moving speed, when being combined with the substance to be treated, the oxygen ions cannot generate stronger collision between the oxygen ions and the substance to be treated, so that larger energy consumption caused by stronger collision is avoided, the oxygen ions are easy to combine with the substance to be treated, the charge efficiency of the substance to be treated in the gas is higher, and more substances to be treated can be collected under the action of the dust removing electric field anode 5082, and the dust removing efficiency of the electric field device is higher.
Example 21
The air dust removal system of this embodiment includes the electric field device of the above-described embodiment 17, 18, 19, or 20. The air needs to flow through the electric field device firstly, so that dust in the air is effectively removed by the electric field device, and the air is cleaner, and contains less dust and other impurities.
Example 22 (front electrode)
As shown in fig. 16, the present embodiment provides an electric field device, which includes an electric field device inlet 3085, a flow channel 3086, an electric field flow channel 3087, and an electric field device outlet 3088, wherein the flow channel 3086 is provided with a front electrode 3083, the ratio of the cross-sectional area of the front electrode 3083 to the cross-sectional area of the flow channel 3086 is 99% to 10%, the electric field device further includes a dust removal electric field cathode 3081 and a dust removal electric field anode 3082, and the electric field flow channel 3087 is located between the dust removal electric field cathode 3081 and the dust removal electric field anode 3082. The working principle of the electric field device of the invention is as follows: the gas containing the pollutants enters the flow channel 3086 through the electric field device inlet 3085, the front electrode 3083 arranged in the flow channel 3086 conducts electrons to part of the pollutants, and part of the pollutants are charged, when the pollutants enter the electric field flow channel 3087 from the flow channel 3086, the dust removing electric field anode 3082 applies attractive force to the charged pollutants, the charged pollutants move to the dust removing electric field anode 3082 until the part of the pollutants are attached to the dust removing electric field anode 3082, meanwhile, an ionization dust removing electric field is formed between the dust removing electric field cathode 3081 and the dust removing electric field anode 3082 in the electric field flow channel 3087, the ionization dust removing electric field charges the other part of the pollutants, and therefore the other part of the pollutants are subjected to attractive force applied by the dust removing electric field anode 3082 after being charged and finally attached to the dust removing electric field anode 3082, so that the electric field device is used for enabling the charged efficiency of the pollutants to be higher, further guaranteeing that the dust removing electric field anode 3082 can collect more pollutants, and guaranteeing that the collecting efficiency of the pollutants is higher.
The cross-sectional area of the front electrode 3083 refers to the sum of the areas of the front electrode 3083 along the solid portion of the cross-section. The ratio of the cross-sectional area of the front electrode 3083 to the cross-sectional area of the flow passage 3086 may be 99% to 10%, or 90% to 10%, or 80% to 20%, or 70% to 30%, or 60% to 40%, or 50%.
As shown in fig. 16, in this embodiment, the front electrode 3083 and the dust removing electric field cathode 3081 are both electrically connected to the cathode of the dc power supply, and the dust removing electric field anode 3082 is electrically connected to the anode of the dc power supply. In this embodiment, the front electrode 3083 and the electric field cathode 3081 are both negative, and the electric field anode 3082 is positive.
As shown in fig. 16, the front electrode 3083 in this embodiment may be mesh-shaped. Thus, when the gas flows through the flow channel 3086, the gas and the pollutants are convenient to flow through the front electrode 3083 by utilizing the reticular structural characteristic of the front electrode 3083, and the pollutants in the gas are more fully contacted with the front electrode 3083, so that the front electrode 3083 can conduct electrons to more pollutants, and the charging efficiency of the pollutants is higher.
As shown in fig. 16, in this embodiment, the dust removing electric field anode 3082 is tubular, the dust removing electric field cathode 3081 is rod-shaped, and the dust removing electric field cathode 3081 is disposed in the dust removing electric field anode 3082. The electric field dust anode 3082 and the electric field dust cathode 3081 in this embodiment are asymmetric. When the gas flows into the ionization electric field formed between the dust field cathode 3081 and the dust field anode 3082, the contaminants are charged, and the charged contaminants are collected on the inner wall of the dust field anode 3082 by the attractive force applied by the dust field anode 3082.
In addition, as shown in fig. 16, in the present embodiment, the electric field dust anode 3082 and the electric field dust cathode 3081 both extend in the front-rear direction, and the front end of the electric field dust anode 3082 is located forward of the front end of the electric field dust cathode 3081 in the front-rear direction. And as shown in fig. 16, the rear end of the electric field dust anode 3082 is located rearward of the rear end of the electric field dust cathode 3081 in the front-rear direction. In this embodiment, the length of the electric field anode 3082 is longer along the front-rear direction, so that the area of the adsorption surface on the inner wall of the electric field anode 3082 is larger, so that the attraction to the contaminants with negative potential is larger, and more contaminants can be collected.
As shown in fig. 16, in this embodiment, the electric field cathode 3081 and the electric field anode 3082 form ionization units, and there are a plurality of ionization units, so that more contaminants can be collected by using a plurality of ionization units, and the electric field device has stronger capability of collecting contaminants and higher collection efficiency.
In this embodiment, the contaminants include general dust with weak conductivity, metal dust with strong conductivity, mist droplets, aerosol, and the like. In this embodiment, the electric field device is used for collecting common dust with weak conductivity and pollutants with strong conductivity in gas, and the collecting process is as follows: when the gas flows into the flow channel 3086 through the electric field device inlet 3085, the pollutants such as metal dust, fog drops or aerosol with stronger conductivity in the gas are directly negatively charged when contacting with the front electrode 3083 or reaching a certain range with the front electrode 3083, then all the pollutants enter the electric field flow channel 3087 along with the gas flow, the dust removing electric field anode 3082 applies attractive force to the negatively charged metal dust, fog drops or aerosol and collects part of the pollutants, meanwhile, the dust removing electric field anode 3082 and the dust removing electric field cathode 3081 form an ionization electric field, oxygen ions are obtained through oxygen in the ionization gas by the ionization electric field, and after the negatively charged oxygen ions are combined with common dust, the common dust is negatively charged, the dust removing electric field anode 3082 applies attractive force to the part of the negatively charged dust and collects the part of the pollutants, so that the pollutants with stronger conductivity and weaker conductivity in the gas are collected, the electric field device can collect the types of substances more widely, and has stronger collection capacity.
The dust removing electric field cathode 3081 described above in this embodiment is also referred to as a corona charging electrode. The direct current power supply is specifically a direct current high voltage power supply. Direct-current high voltage is introduced between the front electrode 3083 and the dust removal electric field anode 3082 to form a conductive loop; direct-current high voltage is introduced between the dust removal electric field cathode 3081 and the dust removal electric field anode 3082 to form an ionization discharge corona electric field. The front electrode 3083 in this embodiment is a densely distributed conductor. When the dust easy to be charged passes through the front electrode 3083, the front electrode 3083 directly charges electrons to the dust, and the dust is then adsorbed by the anode 3082 of the dedusting electric field with different poles; meanwhile, uncharged dust passes through an ionization region formed by the dedusting electric field cathode 3081 and the dedusting electric field anode 3082, and ionized oxygen formed by the ionization region can charge electrons to the dust, so that the dust is continuously charged and adsorbed by the dedusting electric field anode 3082 with different poles.
In this embodiment, the electric field device can form two or more power-on modes. For example, in the case of sufficient oxygen in the gas, the pollutants can be charged by using an ionization discharge corona electric field formed between the dust removal electric field cathode 3081 and the dust removal electric field anode 3082 to ionize the oxygen, and then the pollutants are collected by using the dust removal electric field anode 3082; and when the oxygen content in the gas is too low, or the gas is in an oxygen-free state, or the pollutant is conductive dust fog, the front electrode 3083 is used for directly electrifying the pollutant, so that the pollutant is adsorbed by the dust removal electric field anode 3082 after being fully electrified. The electric fields of the two charging modes can be adopted in the embodiment, so that high-resistance dust easy to charge and low-resistance metal dust, aerosol, liquid mist and the like easy to charge can be collected simultaneously. The two power-on modes are used simultaneously, and the application range of the electric field is enlarged.
In summary, the present invention effectively overcomes the disadvantages of the prior art and has high industrial utility value.
The above embodiments are merely illustrative of the principles of the present invention and its effectiveness, and are not intended to limit the invention. Modifications and variations may be made to the above-described embodiments by those skilled in the art without departing from the spirit and scope of the invention. Accordingly, it is intended that all equivalent modifications and variations of the invention be covered by the claims, which are within the ordinary skill of the art, be within the spirit and scope of the present disclosure. For example, in this application, "air" is defined broadly to include all gases such as exhaust gas, exhaust gas. Accordingly, the scope of the claims (e.g., "air dust removal system", "air electric field dust removal method", "air oxygenation method", "air dust removal method") should include all "gases".
Claims (14)
1. The electric field device is characterized by comprising an electric field device inlet, an electric field device outlet, a dust removal electric field cathode and a dust removal electric field anode, wherein the dust removal electric field cathode and the dust removal electric field anode are used for generating an ionization dust removal electric field; the dust removing electric field anode comprises a first anode part and a second anode part, the first anode part is close to the electric field device inlet, the second anode part is close to the electric field device outlet, at least one insulation mechanism is arranged between the first anode part and the second anode part,
The dust removal electric field anode comprises one or more hollow anode tubes which are arranged in parallel, the dust removal electric field cathode penetrates through the dust removal electric field anode, and the ratio of the dust accumulation area of the dust removal electric field anode to the discharge area of the dust removal electric field cathode is 3.334:1-113.34:1, the pole spacing between the dust removing electric field anode and the dust removing electric field cathode is less than 150mm.
2. The electric field device of claim 1, wherein an electric field flow path is formed between the dust removing electric field anode and the dust removing electric field cathode, and the insulating mechanism is disposed outside the electric field flow path.
3. The electric field device of claim 1 or 2, wherein the insulation mechanism comprises an insulation portion and a thermal insulation portion; the insulating part is made of ceramic material or glass material.
4. An electric field device as claimed in claim 3 wherein the insulating portion is an umbrella string ceramic post, an umbrella string glass post, a columnar string ceramic post or a columnar glass post, glazed inside or outside the umbrella or inside or outside the post.
5. The electric field device of claim 4, wherein the distance between the outer edge of the umbrella-shaped string ceramic column or the umbrella-shaped string glass column and the dust removal electric field anode is greater than 1.4 times of the electric field distance, the sum of the distance between the umbrella ribs of the umbrella-shaped string ceramic column or the umbrella-shaped string glass column is greater than 1.4 times of the insulation distance between the umbrella-shaped string ceramic column or the umbrella-shaped string glass column, and the total depth inside the umbrella ribs of the umbrella-shaped string ceramic column or the umbrella-shaped string glass column is greater than 1.4 times of the insulation distance between the umbrella-shaped string ceramic column or the umbrella-shaped string glass column.
6. The electric field device of claim 1, wherein the length of the first anode portion is 1/10 to 1/4 of the length of the dedusting electric field anode.
7. The electric field device of claim 1, wherein the second anode portion comprises a dust accumulation section and a reserved dust accumulation section.
8. The electric field device of claim 1, wherein a ratio of a dust area of the dust field anode to a discharge area of the dust field cathode is 6.67:1-56.67:1.
9. the electric field device of claim 1, wherein the distance between the dedusting electric field anode and the dedusting electric field cathode is 2.5-139.9mm.
10. The electric field device of claim 1, wherein the dust removing electric field anode has a length of 10-180mm.
11. The electric field device of claim 1, wherein the dust removing electric field cathode has a length of 30-180mm.
12. The electric field device of claim 1, wherein the dust removing electric field cathode comprises at least one electrode rod or a number of cathode wires, the diameter of the electrode rod or the cathode wires being no greater than 3mm.
13. The electric field device of claim 1, wherein at least one cathode support plate is disposed between the first anode portion and the second anode portion.
14. An air dust removal system comprising an electric field device as claimed in any one of claims 1 to 13.
Applications Claiming Priority (27)
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| CN201811227550 | 2018-10-22 | ||
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| CN201910636710 | 2019-07-15 | ||
| PCT/CN2019/112312 WO2020083236A1 (en) | 2018-10-22 | 2019-10-21 | Air dust removal system and method |
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| CN201990001104.0U Active CN216857028U (en) | 2018-10-22 | 2019-10-21 | Electric field device and air dust removal system |
| CN201980069634.3A Active CN113438979B (en) | 2018-10-22 | 2019-10-21 | Air dust removal system and method |
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| CN201990001095.5U Active CN216857040U (en) | 2018-10-22 | 2019-10-21 | Air inlet electric field device and air inlet dust removal system |
| CN201980069627.3A Pending CN113286659A (en) | 2018-10-22 | 2019-10-21 | Air dust removal system and method |
| CN201980069644.7A Active CN113423506B (en) | 2018-10-22 | 2019-10-21 | Air dust removal system and method |
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| CN201980069643.2A Active CN113438980B (en) | 2018-10-22 | 2019-10-21 | Air dust removal system and method |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN113366198B (en) * | 2018-10-22 | 2023-08-15 | 上海必修福企业管理有限公司 | Engine emission treatment system and method |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105312154A (en) * | 2015-12-07 | 2016-02-10 | 福建龙净环保股份有限公司 | Wet electric precipitator |
| CN205949064U (en) * | 2016-08-15 | 2017-02-15 | 中冶京诚工程技术有限公司 | Vertical wet -type electrostatic precipitator and hierarchical washing unit thereof |
Family Cites Families (24)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3020872U (en) * | 1995-07-24 | 1996-02-06 | 一也 早川 | Electrostatic air purifier |
| US7025806B2 (en) * | 2003-11-25 | 2006-04-11 | Stri{dot over (o)}nAir, Inc. | Electrically enhanced air filtration with improved efficacy |
| CN1827223A (en) * | 2005-03-04 | 2006-09-06 | 张寅啸 | Dust collector utilizing magnetic confinement of field effect |
| JP2006281135A (en) * | 2005-04-01 | 2006-10-19 | Denso Corp | Dust collector |
| CN201751006U (en) * | 2010-05-10 | 2011-02-23 | 杨莺 | High-frequency power supply controller special for electrostatic dust removal |
| CN101954312A (en) * | 2010-10-11 | 2011-01-26 | 金烈水 | Coulomb electric precipitator |
| CN202500687U (en) * | 2012-02-08 | 2012-10-24 | 宁波市镇海华泰电器厂 | Road PM2.5 clearing device with oil-saving function |
| CN202606276U (en) * | 2012-04-12 | 2012-12-19 | 孙茂华 | Air purification device for collecting dust by virtue of electret characteristics of material |
| CN102974461B (en) * | 2012-04-12 | 2015-09-02 | 孙茂华 | Utilize air cleaning unit and the air purification method of material electret characteristic control of dust |
| CN103566753B (en) * | 2013-11-18 | 2017-01-18 | 沈阳工业大学 | Cooking oil fume integrated treatment system and method |
| JP6126068B2 (en) * | 2014-12-02 | 2017-05-10 | トヨタ自動車株式会社 | Exhaust gas purification device |
| CN204593621U (en) * | 2015-01-27 | 2015-08-26 | 温州市骐邦环保科技有限公司 | With the air cleaning unit of deozonize function |
| CN204866199U (en) * | 2015-06-16 | 2015-12-16 | 东莞市长资实业有限公司 | Air dust -collecting equipment and have air purifier of this equipment convenient to wash |
| CN104971823B (en) * | 2015-06-16 | 2018-04-13 | 东莞市长资实业有限公司 | A kind of air dust-collecting equipment easy to cleaning and the air purifier with the equipment |
| CN204911786U (en) * | 2015-07-08 | 2015-12-30 | 于泽华 | Static removes haze device |
| CN104959234A (en) * | 2015-07-08 | 2015-10-07 | 于泽华 | Electrostatic haze removal apparatus |
| CN105149092B (en) * | 2015-09-02 | 2017-08-29 | 中国科学院过程工程研究所 | It is a kind of to be used for the dust removal method of conductive dust |
| CN205146446U (en) * | 2015-11-04 | 2016-04-13 | 瑞安市林风机电有限公司 | Electrostatic cooking fume purifier |
| CN107020202A (en) * | 2016-01-29 | 2017-08-08 | 黄健伟 | A kind of ultra-clean electro dust removing method and device |
| CN107149981B (en) * | 2016-03-02 | 2019-02-22 | 北京纳米能源与系统研究所 | A kind of sports type rubs electric gas dust-removing device, dust pelletizing system and dust removal method |
| CN105727676B (en) * | 2016-04-12 | 2018-03-06 | 昆明理工大学 | A kind of method and device of electromagnetism collaboration electrofiltration dedusting |
| CN106269256A (en) * | 2016-08-10 | 2017-01-04 | 福建龙净环保股份有限公司 | A kind of electrostatic precipitator for gas cleaning |
| CN106540805A (en) * | 2016-12-29 | 2017-03-29 | 天津钢铁集团有限公司 | A kind of electric dust removing system improved structure |
| CN206793910U (en) * | 2017-05-15 | 2017-12-26 | 江苏瑞洁环境工程科技有限责任公司 | A kind of wet electrical dust precipitator of buck self-cleaning |
-
2019
- 2019-10-21 CN CN201980069626.9A patent/CN113330195B/en active Active
- 2019-10-21 CN CN201990001104.0U patent/CN216857028U/en active Active
- 2019-10-21 CN CN201980069634.3A patent/CN113438979B/en active Active
- 2019-10-21 CN CN201980069641.3A patent/CN113439154B/en active Active
- 2019-10-21 CN CN201990001095.5U patent/CN216857040U/en active Active
- 2019-10-21 CN CN201980069627.3A patent/CN113286659A/en active Pending
- 2019-10-21 CN CN201980069644.7A patent/CN113423506B/en active Active
- 2019-10-21 CN CN201980069629.2A patent/CN113438976B/en active Active
- 2019-10-21 CN CN201980069643.2A patent/CN113438980B/en active Active
- 2019-10-21 CN CN201980069623.5A patent/CN113423505B/en active Active
- 2019-10-21 CN CN201980069640.9A patent/CN113438977B/en active Active
- 2019-10-21 CN CN201980069625.4A patent/CN113438975B/en active Active
- 2019-10-21 CN CN201980069656.XA patent/CN113438978B/en active Active
- 2019-10-21 CN CN201980069639.6A patent/CN113423507B/en active Active
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105312154A (en) * | 2015-12-07 | 2016-02-10 | 福建龙净环保股份有限公司 | Wet electric precipitator |
| CN205949064U (en) * | 2016-08-15 | 2017-02-15 | 中冶京诚工程技术有限公司 | Vertical wet -type electrostatic precipitator and hierarchical washing unit thereof |
Non-Patent Citations (1)
| Title |
|---|
| 张殿印.5.绝缘材料.《除尘器手册》.2015,410-413. * |
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| CN113438978B (en) | 2023-12-22 |
| CN113423505A (en) | 2021-09-21 |
| CN216857040U (en) | 2022-07-01 |
| CN113438976A (en) | 2021-09-24 |
| CN113423507A (en) | 2021-09-21 |
| CN113438977B (en) | 2023-12-22 |
| CN113438980A (en) | 2021-09-24 |
| CN113286659A (en) | 2021-08-20 |
| CN113438977A (en) | 2021-09-24 |
| CN113438979A (en) | 2021-09-24 |
| CN113438978A (en) | 2021-09-24 |
| CN113438975B (en) | 2023-12-22 |
| CN113438980B (en) | 2023-12-22 |
| CN216857028U (en) | 2022-07-01 |
| CN113439154B (en) | 2023-08-15 |
| CN113330195B (en) | 2023-08-15 |
| CN113439154A (en) | 2021-09-24 |
| CN113438975A (en) | 2021-09-24 |
| CN113423507B (en) | 2023-12-22 |
| CN113423506A (en) | 2021-09-21 |
| CN113438976B (en) | 2023-12-22 |
| CN113438979B (en) | 2023-12-22 |
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