TWM452229U - Assembly type smoke decomposition discharge reactor - Google Patents

Description

Combined soot decomposition discharge reactor

The present invention relates to a combined soot decomposition discharge reactor, which belongs to the technical field of high pressure discharge application.

In many families, housewives are often the protagonists of the kitchen, but some housewives have headaches, chest tightness, itchy eyes, stuffy nose, tinnitus, etc. after a long time in the kitchen. If the kitchen time is concentrated, the time is long, and if it is serious, It can lead to insomnia, memory loss, bronchitis, pneumonia and other "drunk oil syndrome", which is mainly caused by the pollution of oil smoke in the kitchen. Cooking oil and food produce a large amount of "thermal oxidative decomposition products" under high temperature cooking. The decomposition products are dispersed into the air in the form of smoke to form oil fumes, and the composition of the oil fumes is very complicated, mainly including aldehydes, ketones, hydrocarbons, fatty acids, alcohols, aromatic compounds, esters, lactones, heterocyclic compounds, etc., including Benzopyrene, volatile nitrosamines, heterocyclic amine compounds and the like are known to be highly carcinogenic.

Studies have shown that oil condensate produced by cooking oil to about 270 °C can cause chromosome damage in human cells, and the incidence of lung cancer in women may be one of the important factors. In recent years, some large cities in China have been on lung cancer. In the investigation of the incidence, it was found that the long-term cooking of housewives has a high incidence of lung cancer. In addition, the cooking staff who cook in the kitchen with high concentration of soot are not only easy to cause lung cancer, but also to their intestines. The damage of the brain and nerves is also obvious.

Not only kitchen fumes, but also smoke generated by mechanical processing such as cigarette smoke, factory floor lubricants, insulating oil and cutting oil, which have serious pollution to the environment, threaten people's health and have potential cancer risk. .

Most of the existing range hood equipment is used to pump the soot out of the kitchen to the outdoor air. Although the indoor soot is reduced, the oil smoke discharged to the outside still pollutes the outdoor air.

In view of the practical difficulties and the lack of improvement of the above-mentioned conventional hood equipment, the creator hopes to provide a breakthrough design to enhance the practical effect, and is devoted to research and design, and has been engaged in related products for many years. Designing the professional technical knowledge and practical experience of production and sales and the results of the research and design, I finally developed a combined soot decomposition and discharge reactor to provide users.

The creation reactor is composed of a plurality of processing unit combinations and an outer casing with flue gas inlet and outlet. The processing unit is composed of a hollow cylindrical electrode or a spiral electrode, a rod electrode and a supporting mechanism, and the supporting mechanism is supported by a support frame and a support. The rod is assembled, and the hollow cylindrical electrode and the rod electrode are all mounted on the support frame, and the two support frames are fixedly mounted on the inlet and outlet plates of the reactor shell by a plurality of support rods, thereby achieving low power consumption and low working temperature. High safety, long service life and no ozone at work.

The purpose of this creation is to design a device that can decompose and treat soot according to the defects of the existing range hood, and eliminate the environmental pollution of the oil smoke indoors and outdoors.

In order to make your review board more aware of the structural features and efficacy of this creation, we will cooperate with the schema and elaborate on it later.

The technical solution of the present invention is that the combined soot decomposition discharge reactor is composed of a plurality of processing units (1) combined with a casing (2) with flue gas inlet and outlet (3), (4), the processing unit ( 1) It consists of a hollow cylindrical electrode (17) or a spiral electrode (14) and a rod electrode (12) and a supporting mechanism. The supporting mechanism is assembled by a support frame (15) and a support rod (16), and a hollow cylindrical electrode ( 17) or the spiral electrode (14) and the rod electrode (12) are both mounted on the support frame (15), and the two support frames (15) are fixedly mounted on the reactor casing (2) by a plurality of support rods (16), In and out (3), (4) board surface.

The reactor is a high-pressure discharge reactor, and the processing unit (1) is designed as a rod electrode (12) for short-distance high-voltage discharge of a hollow cylindrical electrode (17) or a spiral electrode (14), wherein the surface of the rod electrode (12) is A tapered annular body is provided, and a surface of the outer hollow electrode (11) is also provided with a tapered annular body. The tapered annular body is provided with a lateral groove (13), and the groove (13) can be aligned with the rod electrode (12) Vertically, it can also be at an angle to the axis of the rod electrode (12), and the outer portion of the hollow cylindrical electrode (17) is processed into a uniform conical annular body and is provided with lateral grooves (13), direction and rod shape. Electrode (12) staggered, a hollow cylindrical electrode (17) Another large hollow cylindrical electrode (17) can be arranged outside, and several layers of concentric circular hollow cylinders can be formed in sequence, and the rod electrode (12) receives a high voltage, the voltage is 6kv-500kv, and the circuit is connected. In the open circuit, the cone-shaped annular body of each layer generates a high-voltage discharge, and the lateral groove (13) on the tapered annular body provides a passage for uniformly distributing the undissolved soot through the entire discharge reactor, and the soot is dispersed to each discharge layer. For the decomposition work, the hollow cylindrical electrode (17) or the spiral electrode (14) forms several layers of concentric circles, and several layers are required to be determined according to the difficulty of actually decomposing the soot, and those which are not easily decomposed may be provided with several layers.

The power source can be connected to the rod electrode (12), and can also be connected to the concentric circles of each discharge layer. Since the power source is connected by an open circuit, no ozone is generated after the discharge.

Each layer of cone-shaped annular body generates high-pressure discharge to release high-concentration ion current, which carries high-energy electron kinetic energy, which can decompose the soot into water, carbon dioxide, nitrogen and other stable substances and then discharge it outside, reducing the pollution of the soot to the environment.

The processing unit (1) of the reactor is configured as a rod electrode (12) and a multilayer hollow cylindrical electrode (17) or a spiral electrode (14) discharge structure, and the array processing unit (1) can be combined in parallel to form a circle, a rectangle or the like. The irregular shape combination processing unit (1), and the array combination processing unit (1) are arranged side by side into a combined soot decomposition discharge reactor of various shape sizes.

The power connection can be divided into a high voltage and a positive high voltage. The voltage is 6kv-500kv, and the distance between the rod electrode (12) and the hollow cylindrical electrode (17) or the center of the spiral electrode (14) is 0-100mm. Adjusted by height.

The present combined combination fume decomposition discharge reactor: In the single rod electrode (12) to the hollow cylindrical electrode (17) discharge structure, the material of the hollow cylindrical electrode (17) is a good electrical conductor, and the hollow cylindrical electrode (17) has an inner diameter of 10-2000 mm, and the outer diameter is slightly The inner diameter of the hollow cylindrical electrode (17) is 0.05 mm or more, and the rod electrode (12) is disposed at the inner center of the hollow cylindrical electrode (17), that is, through the hollow cylindrical electrode (17), the hollow cylindrical electrode (17) The outer hollow cylindrical electrode (17) can be further sleeved to form a multi-layer concentric circle structure, and the hollow cylindrical electrode (17) can also be replaced with a spiral electrode (14), the rod electrode (12) and the hollow The material of the cylindrical electrode (17) or the spiral electrode (14) is a good electrical conductor, the structure is rod-shaped and tubular, and the tapered annular body on the circumference is a high-voltage discharge end.

The hollow cylindrical electrode (17) is processed into a lateral groove (13), the direction is staggered with the rod electrode (12), and the lateral groove (13) on the tapered annular body provides a passage so that the soot is dispersed to each discharge layer for efficient use. break down.

The hollow cylindrical electrode (17) or the spiral electrode (14) of the multi-layer concentric structure is provided with an insulating material at a position of 1-100 mm outside of the modular application, and the shape of the insulating material can be circular, rectangular or other shapes as needed. Such as insulating sleeve (20).

The array has a single multi-layer concentric circle structure, and is combined into a circular, rectangular or other irregular shaped combination processing unit (1), and then the array combination processing unit (1) is arranged side by side into various shapes and sizes of soot decomposition discharge reaction. The specific quantity depends on the speed requirement of the decomposition of the soot and the type of the soot.

The power connection can be divided into a high voltage and a positive high voltage, and the voltage is 6kv-500kv. The open circuit is connected to the rod electrode (12) or connected to each discharge layer. On the center of the circle, each discharge layer generates a high voltage discharge.

The soot is guided into the discharge reactor in the discharge, and the soot flows through the processing unit (1), and the discharge reactor effectively decomposes the passing soot, and the decomposition efficiency thereof is over 95%.

The discharge reactor has no unexpected product due to electrolytic reaction and is free of ozone.

The beneficial effect of the present invention compared with the prior art is that the discharge reactor adopts a modular design, and the size can be adjusted according to the type of soot and the amount of soot per unit time required to adjust the hollow cylindrical electrode (17) or spiral in the reactor. The size of the electrode (14), the voltage level, the distance between the rod electrode (12) and the hollow cylindrical electrode (17) or the spiral electrode (14), the pulse discharge frequency and the power supply power, etc., achieve the purpose of continuously decomposing the soot continuously. The creation consumes little power and is only one-twentieth of the electrostatic oil collection technology. The creation temperature is low, which is a low-temperature reaction treatment and high safety. The discharge needle of the present invention does not oxidize, has a long service life, and does not generate ozone during work. .

This creation is suitable for the decomposition of smoke from kitchen fumes, oily exhaust gases from vehicles, cigarette smoke and workshop lubricants, insulating oils and cutting oils due to machining.

Example 1: This embodiment is shown in the second figure.

This embodiment consists of a combined soot decomposition discharge reactor consisting of four treatment units (1) combined with a circular outer casing (2) with flue gas inlet and outlet (3), (4), the treatment unit (1) ) by hollow cylindrical electrode (17) and rod electrode (12) Composed of.

In this embodiment, the hollow cylindrical electrode (17) of the processing unit (1) is a single-layer hollow cylindrical electrode (17). As shown in the fourth figure, the inner diameter of the hollow cylindrical electrode (17) is 120 mm, and the hollow cylindrical electrode (17) The thickness of the hollow cylindrical electrode (17) and the rod electrode (12) is 10 mm apart, and the outer portion of the hollow cylindrical electrode (17) is processed into a uniform tapered annular body with lateral grooves uniformly distributed thereon. (13), the direction is staggered with the rod electrode (12), the hollow cylindrical electrode (17) is mounted on the support frame (15), and the outer surface of the hollow cylindrical electrode (17) is laid with a 3 mm insulating protective layer.

In this embodiment, the rod electrode (12) of the processing unit (1) is disposed at the inner center of the hollow cylindrical electrode (17), that is, through the hollow cylindrical electrode (17), the rod electrode (12) and the hollow cylindrical electrode ( 17) The materials are all good conductors of electricity. The surface of the rod electrode (12) is evenly covered with a cone-shaped annular body, and the surface of the outer hollow electrode (11) is also covered with a cone-shaped annular body, and the cone-ring groove (13) is The rod electrode (12) has an axis at an angle of 90°. As shown in the third figure, the tapered annular body on the circumference is a high pressure discharge end.

During operation, the rod electrode (12) is connected to the negative electrode and the applied voltage is 8 kV.

Example 2: This embodiment is shown in the first figure.

This embodiment consists of a combined soot decomposition discharge reactor consisting of four treatment units (1) combined with a square casing (2) with flue gas inlet and outlet (3), (4), the treatment unit (1) By hollow cylindrical electrode (17) and rod electrode (12) Composed of.

In the present embodiment, the hollow cylindrical electrode (17) of the processing unit (1) is a two-layer hollow cylindrical electrode (17) having different inner diameters. As shown in the fifth figure, the inner diameter of the inner hollow cylindrical electrode (17) is 100 mm. The hollow cylindrical electrode (17) has a thickness of 2 mm, the outer hollow cylindrical electrode (17) is concentric with the inner hollow cylindrical electrode (17), and the inner and outer hollow cylindrical electrodes (17) are radially apart from each other by 10 mm, and the hollow cylindrical electrode (17) The outer portion is processed into a uniform tapered annular body and is provided with lateral grooves (13) thereon, the direction is staggered with the rod electrode (12), and the inner and outer hollow cylindrical electrodes (17) are mounted on the support frame (15) Upper, the outer surface of the outer hollow cylindrical electrode (17) is laid with a 3 mm insulating protective layer.

In this embodiment, the rod electrode (12) of the processing unit (1) is disposed at the inner center of the hollow cylindrical electrode (17), that is, through the hollow cylindrical electrode (17), the rod electrode (12) and the hollow cylindrical electrode ( 17) The materials are all good conductors of electricity. The surface of the rod electrode (12) is evenly covered with a cone-shaped annular body, and the surface of the outer hollow electrode (11) is also covered with a cone-shaped annular body, and the cone-ring groove (13) is The rod electrode (12) is perpendicular to the axis, and as shown in the seventh figure, the tapered annular body on the circumference is a high pressure discharge end.

During operation, the rod electrode (12) is connected to the negative electrode and the applied voltage is 10 kV.

Example 3: This embodiment is shown in the second figure.

This embodiment consists of a combined soot decomposition discharge reactor consisting of four treatment units (1) combined with a circular outer casing (2) with flue gas inlet and outlet (3), (4). The processing unit (1) consists of a hollow cylindrical electrode (17) and a rod electrode (12).

In the present embodiment, the hollow cylindrical electrode (17) of the processing unit (1) is three hollow cylindrical electrodes (17) of different inner diameters, as shown in the sixth and sixth figures, the inner hollow cylindrical electrode (17) The inner diameter is 80mm, the thickness of the hollow cylindrical electrode (17) is 2mm, and the hollow cylindrical electrodes 1 and 2 (18) and (19) of the middle and outer layers are concentric with the inner hollow cylindrical electrode (17), and the inner, middle and outer hollows are hollow. Cylindrical electrode (17), hollow cylindrical electrode one (18), hollow cylindrical electrode two (19) with a diameter of 10 mm, inner, middle and outer hollow cylindrical electrode (17), hollow cylindrical electrode one (18), hollow cylinder The outer part of the electrode (19) is made of a conical annular body which is processed into a uniform cloth and is provided with a lateral groove (13) thereon, and the direction is interlaced with the rod electrode (12), and the inner, middle and outer hollow cylindrical electrodes (17) The hollow cylindrical electrode one (18) and the hollow cylindrical electrode two (19) are all mounted on the support frame (15), and the outer surface of the outer hollow cylindrical electrode two (19) is laid with a 3 mm insulating protective layer.

In this embodiment, the rod electrode (12) of the processing unit (1) is disposed at the inner center of the hollow cylindrical electrode (17), that is, through the hollow cylindrical electrode (17), the rod electrode (12) and the hollow cylindrical electrode ( 17), the hollow cylindrical electrode one (18), the hollow cylindrical electrode two (19) are all good electrical conductors, the surface of the rod electrode (12) is evenly covered with a cone-shaped body, and the surface of the outer hollow electrode (11) A tapered annular body is also provided, the tapered ring groove (13) being at an angle of 30 to the axis of the rod electrode (12). As shown in the eighth figure, the tapered annular body on the circumference is a high pressure discharge end.

During operation, the rod electrode (12) is connected to the positive electrode and the applied voltage is 15 kV.

Example 4: This embodiment is shown in the ninth and tenth drawings, in which the spiral electrode (14) shown in the fourth figure is wound and fixed by a bracket (142) to form a spiral hollow electrode (141), and a spiral hollow electrode ( 141) Insulation material shall be added to the outer 1-100mm position. The shape of the insulation material may be circular, rectangular or other shapes as required, such as insulating sleeve with flue gas inlet and outlet (3), (4) (20) The power supply is directly connected to the spiral hollow electrode (141), and the spiral hollow electrode (141) also includes a plurality of discharge rings (1411) each having a discharge sharp edge and being spirally connected in series shape.

Example 5: The present embodiment is shown in FIG. 11 , which is to fix the spiral electrode ( 14 ) shown in FIG. 4 with a bracket ( 144 ) to form a circular hollow spiral electrode ( 143 ), and to form a circular hollow with the bracket ( 144 ). The spiral electrode (143) is fixed in an insulating casing (21) made of an insulating material and having flue gas inlet and outlet ports (211) and (212), and directly connecting the power source to the circular hollow spiral electrode (143). The circular hollow spiral electrode (143) also includes a plurality of discharge rings (1431) each having a discharge sharp edge and being spirally connected in series.

Example 6: Combined soot decomposition The reactor was composed of a plurality of processing units (1) combined with a casing (2) with flue gas inlet and outlet (3), (4).

The present embodiment, as shown in FIG. 12, provides an engine fume decomposition device (A) for processing exhaust gas discharged from an engine, which includes a processing unit (6) And a casing with flue gas inlet and outlet (5), (7), the treatment unit (6) comprises a high pressure discharge reactor (61), a pretreatment module (62) and a waste recycling module (63).

As shown in the twelfth and thirteenth figures, the pretreatment module (62) is disposed between the flue gas inlet (5) and the processing unit (6), and includes a centrifugal fan (621) and a waste intercepting device. a tank (622) and a waste discharge port (623) for blocking and recovering solid or liquid waste taken out by the centrifugal fan (621), the waste discharge port (623) being used for The solid or liquid waste is discharged.

As shown in Fig. 12, the waste recycling module (63) is disposed under the pretreatment module (62) and includes a waste guiding groove (631) and a waste re-discharging port (632). A channel (631) is used to direct solid or liquid waste to the waste re-vent (632).

When installing, firstly, the front end and the rear end of the processing unit (6) are respectively connected to the inlet (5) and the outlet (7) through a connecting member (8), and then the inlet (5) and the exhaust of the engine are exhausted. The port is connected, and finally the high-pressure discharge reactor (61) and the centrifugal fan (621) are connected to a power source.

In use, the high pressure discharge reactor (61) and the centrifugal fan (621) are turned on; the centrifugal fan (621) extracts automobile exhaust gas through the inlet (5), and passes the solid or liquid waste through the waste intercepting tank (622). And pretreating the waste discharge port (623), and the remaining solid or liquid waste after the pretreatment is subjected to centrifugation and reprocessing to the waste recovery module (63), and the pretreated gas passes through the high pressure discharge. The reactor (61) is electrolyzed due to hollow The surface of the electrode is applied with high-voltage electricity of several tens of kilovolts, so that the molecular bond can be completely interrupted, carbon monoxide is converted into carbon and oxygen, and the hydrocarbon is finally converted into carbon, oxygen and water, and the nitrogen oxide is converted into Nitrogen and oxygen, etc.

Therefore, the engine fume decomposition device (A) of the present invention can achieve the exhaust gas purification effect that cannot be achieved by the catalyst and the filter in the prior art, that is, not only does not generate greenhouse gas carbon dioxide, but also can supplement oxygen in the air.

In summary, the creative combined soot decomposition discharge reactor can effectively decompose the smoke generated by the kitchen fume, the oily exhaust gas discharged from the vehicle, the cigarette smoke, the workshop lubricating oil, the insulating oil and the cutting oil, etc. due to mechanical processing. The novelty, the progressiveness and the application for industrial application have already met the requirements for the granting of new patents. The patent application was filed according to law, and the review committee of the member of the committee can review it in detail, and the patent for this case will be granted as soon as possible. Will.

The above is only the preferred embodiment of the present invention. When it is not possible to limit the scope of this creation, the equivalent changes and modifications made by the patent application scope of this creation should still belong to this creation patent. Within the scope of coverage.

(1) ‧‧‧Processing unit

(11)‧‧‧ hollow electrode

(12)‧‧‧ rod electrodes

(13) ‧‧‧ trench

(14)‧‧‧Spiral electrode

(141)‧‧‧Spiral hollow electrode

(1411) (1431) ‧ ‧ discharge ring

(142) (144) ‧‧‧ bracket

(143)‧‧‧Circle type hollow spiral electrode

(15)‧‧‧Support frame

(16)‧‧‧Support rod

(17)‧‧‧ hollow cylindrical electrode

(18)‧‧‧ hollow cylindrical electrode

(19)‧‧‧ hollow cylindrical electrode II

(2) (21) ‧ ‧ shell

(20)‧‧‧Insulated sleeves

(211)(3)(5)‧‧‧ Import

(212)(4)(7)‧‧‧Export

(6) ‧‧‧Processing unit

(61)‧‧‧High-voltage discharge reactor

(62) ‧‧‧Pretreatment module

(621)‧‧‧ Centrifugal fans

(622) ‧‧ ‧ Scrap Interceptor

(623) ‧‧‧Waste discharge

(63)‧‧‧ scrap recycling module

(631)‧‧‧Waste guiding groove

(632) ‧‧ ‧ scrap re-export

(8)‧‧‧Connecting parts

(A)‧‧‧Engine fume decomposition unit

The first figure is a schematic diagram of the structure of the square combination processing unit of the creation.

The second figure is a schematic diagram of the structure of the circular combination processing unit of the present creation.

The third figure is a schematic diagram of the first structure of the creation processing unit, and the discharge layer is a hollow cylindrical electrode.

The fourth figure is a second structural diagram of the creation processing unit, and the discharge layer is a spiral electrode.

The fifth figure is a schematic diagram of the structure of the two-layer electrode processing unit of the present creation.

The sixth figure is a schematic diagram of the structure of the three-layer electrode processing unit of the present creation.

The sixth figure is a perspective exploded view of the sixth figure.

The seventh figure is a schematic diagram of the rod electrode structure of the vertical axis of the groove.

The eighth figure is a schematic diagram of the rod electrode structure in which the groove is angled with the axis.

The ninth drawing is a perspective view of an embodiment in which the spiral electrode shown in the fourth figure is fixed by a bracket to form a spiral hollow electrode.

Figure 10 is a partial cross-sectional view showing the structure shown in Figure IX.

The eleventh figure is a perspective view of an embodiment in which the spiral electrode shown in the fourth figure is fixed by a bracket to form a circular hollow spiral electrode.

The twelfth figure is a perspective view of an embodiment of the present application applied to an engine fume decomposition apparatus.

The thirteenth figure is a perspective view of the pre-processing module of the engine fume decomposition device of the twelfth figure.

(1) ‧‧‧Processing unit

(12)‧‧‧ rod electrodes

(15)‧‧‧Support frame

(17)‧‧‧ hollow cylindrical electrode

(2) ‧‧‧ Shell

(3)‧‧‧ Import

(4) ‧ ‧ exports

Claims (15)

A combined soot decomposition discharge reactor, the main feature of which is that the reactor is composed of a plurality of processing unit combinations and an outer casing with flue gas inlet and outlet, the processing unit consists of a hollow cylindrical electrode and a rod electrode and a support The mechanism is composed of a support frame and a support rod assembled by the support frame and the support rod. The hollow cylindrical electrode and the rod electrode are all mounted on the support frame, and the two support frames are fixedly mounted on the inlet and outlet plates of the reactor shell by a plurality of support rods. Upper, the rod electrode is disposed at the center of the inner portion of the hollow cylindrical electrode, that is, through the hollow cylindrical electrode, and the materials of the rod electrode and the hollow cylindrical electrode are good electrical conductors. The combined soot decomposition discharge reactor according to claim 1, wherein the hollow cylindrical electrode is processed into a uniform tapered ring body and is provided with lateral grooves, directions and rods thereon. The electrodes are staggered, and the tapered annular body on the circumference is a high-voltage discharge end, and the direction is staggered with the rod-shaped electrode. Another hollow cylindrical electrode of a larger size can be disposed outside the hollow cylindrical electrode, and several concentric circles can be formed in sequence. Multi-layer hollow cylindrical electrode. The combined soot decomposition discharge reactor according to claim 1, wherein the distance between the rod electrode and the center of the hollow cylindrical electrode is 0-100 mm. The combined soot decomposition discharge reactor according to claim 1, wherein the surface of the rod electrode is uniformly provided with a tapered annular body. The combined soot decomposition discharge reactor according to claim 1, wherein the rod electrode is connected to a power source, and may be coupled to each discharge. On the concentric circles of the layer, the voltage is 6kv-500kv. The combined soot decomposition discharge reactor of claim 1, wherein the outer casing is circular or square. The combined soot decomposition discharge reactor according to claim 1, wherein the processing unit is composed of a hollow spiral electrode, a rod electrode and a support mechanism. The combined soot decomposition discharge reactor according to claim 1, wherein the hollow cylindrical electrode of the processing unit is three hollow cylindrical electrodes of different inner diameters, hollow cylindrical electrodes and inner layers of the inner and outer layers. The hollow cylindrical electrodes are concentric, and the inner, middle and outer hollow cylindrical electrodes are separated by a radial interval of 10 mm, and the inner, middle and outer hollow cylindrical electrodes are respectively processed into a uniform conical annular body and horizontal grooves are arranged thereon. The direction is staggered with the rod electrodes, and the inner, middle and outer hollow cylindrical electrodes are all mounted on the support frame, and the outer surface of the outer hollow cylindrical electrode 2 is provided with an insulating protective layer. The combined soot decomposition discharge reactor according to claim 1, wherein the processing unit is composed of a spiral hollow electrode and a supporting mechanism, wherein the spiral hollow electrode is a long spiral electrode The spiral hollow electrode is fixed by spirally winding on the bracket, and an insulating material is added at a position of 1-100 mm outside the spiral hollow electrode, and the shape of the insulating material can be circular, rectangular or other shapes as needed, such as The insulating sleeve of the flue gas inlet and outlet connects the power source directly to the spiral hollow electrode. The combined soot decomposition reaction reaction as described in claim 9 The spiral hollow electrode also includes a plurality of discharge rings each having a discharge sharp edge and being connected in series in a spiral shape. The combined soot decomposition discharge reactor according to claim 1, wherein the processing unit is composed of a circular hollow spiral electrode and a supporting mechanism, and the circular hollow spiral electrode is a long strip. The hollow spiral electrode is spirally wound on the bracket to be fixed to form a circular hollow spiral electrode, and the circular hollow spiral electrode is fixed by a bracket to an insulating material made of an insulating material and having a flue gas inlet and outlet, and the power source is Directly connected to the circular hollow spiral electrode. The combined soot decomposition discharge reactor according to claim 11, wherein the circular hollow spiral electrode also includes a plurality of discharge rings each having a discharge tip and connected in series Spiral. A combined soot decomposition discharge reactor characterized in that it comprises a processing unit and a casing with inlet and outlet of flue gas, wherein the treatment unit is constituted by a high-pressure discharge reactor, so that the exhaust gas passes through the The inlet of the flue gas, the outlet of the high-pressure discharge reactor and the outlet of the flue gas, the front end and the rear end of the processing unit are respectively connected with the inlet of the flue gas and the outlet of the flue gas through a connecting member, and then the inlet of the flue gas is The engine's exhaust port is connected to handle the exhaust from an engine. The combined soot decomposition discharge reactor of claim 13, wherein the processing unit comprises the features of the processing unit of any one of claims 1-10. The combined soot decomposition reaction reaction described in claim 13 of the patent application scope The processing unit further includes a pre-processing module and a waste recycling module. The pre-processing module is disposed between the inlet of the flue gas and the processing unit, and includes a centrifugal fan and a waste intercepting device. a tank and a waste discharge port for blocking and recovering solid or liquid wastes discharged from the centrifugal fan, the waste discharge ports for discharging the solid or liquid waste, the waste recycling mold The assembly is disposed under the pretreatment module and includes a waste guiding slot and a waste re-discharging outlet. The front end and the rear end of the processing unit are respectively connected to the inlet of the flue gas and the outlet of the flue gas through a connecting component. And then connecting the inlet of the flue gas to the exhaust port of the engine, and finally connecting the high-pressure discharge reactor and the centrifugal fan to the power source; in use, the high-pressure discharge reactor and the centrifugal fan are turned on, and the centrifugal fan passes The inlet of the flue gas extracts exhaust gas of the automobile engine, and the solid or liquid waste is pretreated through the waste intercepting trough and the waste discharge port, and the remaining solid or liquid after the pretreatment The waste is centrifuged, reprocessed to the waste recycling module, and discharged from the waste re-discharging port through the waste guiding tank. The pretreated gas is electrolyzed through the high-pressure discharge reactor due to the surface of the high-pressure discharge reactor. Applying high-voltage electricity of several tens of kilovolts, it can completely break the molecular bonds, convert carbon monoxide into carbon and oxygen, and finally convert hydrocarbons into carbon, oxygen and water, and convert nitrogen oxides into nitrogen and oxygen. Wait, finally discharged from the outlet of the flue gas.