CN205948620U - Waste gas treatment system - Google Patents

Abstract

The utility model relates to a gas purification technique field provides a waste gas treatment system, including the fluid actuating device and the wet -type high voltage static device that are used for mixing and magnetization waste gas, wet -type high voltage static device communicates in fluid actuating device, waste gas flow through in proper order fluid actuating device and wet -type high voltage static device, and fluid actuating device includes fluid mixing subassembly and a plurality of fluid magnetizing apparatus subassembly. The utility model provides a waste gas treatment system, earlier with the different waste gas process fluid actuating device of composition, carry out mixing and magnetization activation, get into wet -type high voltage static device by magnetic mixing waste gas, in high voltage electrostatic field's environment, by magnetic oxygen, the electron that high voltage electrostatic field ionization goes out, decomposition reaction all takes place with waste gas for ion and free radical, waste gas through activation has reduced the intermolecular force, thereby the energy that the greatly reduced exhaust purification process consumed, the efficiency of exhaust -gas treatment is improved.

Description

Exhaust treatment system

Technical field

The utility model is related to gas purification technique field, more particularly, to a kind of exhaust treatment system.

Background technology

People all can manufacture different waste gas in daily production and life process.Different according to gas componant, can be divided into VOC, gas with foreign flavor, dust granules thing and flue gas etc., it is presently used for process for producing or life waste gas Equipment be divided into two categories below：First, Pintsch process kind equipment, using light wave producer treat process waste gas bombarded and Apply heating power, then burnt so that the macromolecular gas in waste gas and imflammable gas catalytic pyrolysis, turn after being substantially oxidized Turn to carbon dioxide, thus reaching the purpose of purification；Second, high-pressure electrostatic kind equipment, made big in waste gas by high-pressure electrostatic Particulate matter polarization, thus adsorption electrode plate surface, to reach the purpose of purification.But, either Pintsch process class sets Standby still high-pressure electrostatic kind equipment, is required to expend the substantial amounts of energy to process waste gas, that is, there is power consumption height, the low disadvantage of the feature of environmental protection End.

Utility model content

In sum, the purpose of this utility model is to provide a kind of exhaust treatment system it is intended to solve existing waste gas Cleaning equipment has that power consumption height, the feature of environmental protection are low.

The utility model is achieved in that exhaust treatment system, swashs including the fluid for mixing and magnetizing waste gas Removable mounting is put and is connected with described fluid activating device and for purifying the wet type high voltage electrostatic device of waste gas, and waste gas flows through successively Described fluid activating device and described wet type high-voltage electrostatic treating device, described fluid activating device include fluid mix assembly with And multiple fluid magnetic assembly.

Specifically, described fluid mix assembly include being communicated in the first sleeve of described wet type high voltage electrostatic device located at Mixing structure in described first sleeve, multiple described fluid magnetic assemblies are sequentially arranged in described mixing structure from top to bottom, Each described fluid magnetic assembly includes arranging with central shaft and located at the described retainer ring mixing in structure with the described structure that mixes And multiple centered on the vertical axis of described retainer ring be in circumferentially distributed magnetic part in described retainer ring；

Or, described fluid mix assembly include being communicated in described wet type high voltage electrostatic device first sleeve and located at Mixing structure in described first sleeve, each described fluid magnetic assembly radially crosses located at described first sleeve and in vertical Can rotate relative to described first sleeve in plane, each described fluid magnetic assembly is located at the described top mixing structure, described stream Body magnetising assembly includes being arranged in the rotary shaft of described first sleeve along described first sleeve radial direction, some parallel interval set In the fixed bin in described rotary shaft and multiple magnetic part in each described fixed bin, described rotary shaft is around central shaft Line rotates relative to described first sleeve, and at least described in one, fixed bin is located in described sleeve pipe.

Specifically, the described structure that mixes is a hollow tube arranging with central shaft with described first sleeve, described hollow The caliber of body is incremented by from middle part step by step to two ends, and described hollow tube offers the engraved structure for mixing gas.

Preferably, described magnetic part is bar magnet, and each described fluid magnetic assembly includes four described bar magnets, four Between individual described bar magnet, 90 ° of angles enclose in described retainer ring each other.

Preferably, described magnetic part be bar magnet, each described bar magnet side by side in corresponding described fixed bin, The magnetic pole of two adjacent described bar magnets is different.

Further, described wet type high voltage electrostatic device includes process chamber, the suspension being communicated in described fluid mixing assembly Process indoor high-pressure electrostatic reactor and the control power supply group for providing described high-pressure electrostatic reactor in described.

Specifically, described high-pressure electrostatic reactor includes multiple being suspended from and described process indoor and be parallel to each other and interval setting Anode collecting plate and the multiple cathodic discharge lines between two adjacent described anode collecting plates, each described anode collection dusting Plate and each described cathodic discharge line are electrically connected to described control power supply group.

Further, the gas also including between described fluid activating device and described wet type high voltage electrostatic device divides In bulk put, described gas dispersion apparatus include connecting the second of described fluid activating device and described wet type high voltage electrostatic device Sleeve pipe and multiple gas diffusion plate in described second sleeve pipe arranged in parallel.

Further, also liquid waste treating apparatus are included, described second sleeve pipe is filled to described liquid waste processing by a collector tube Put discharge waste liquid, described liquid waste treating apparatus include casing, for separate waste liquid in solid particulate matter solid-liquor separation groove and For realizing in waste liquid the detached oil spilling groove of water oil, described solid-liquor separation groove is corresponding with waste liquid source direction and located at described case In vivo, the top end face of described solid-liquor separation groove is concordant with the top end face of described casing, described oil spilling groove in described casing and It is disposed adjacent with described solid-liquor separation groove, the top end face of described oil spilling groove is concordant with the top end face of described casing.

Compared with prior art, the exhaust treatment system that the utility model provides, its operation principle is as follows：First, composition Different waste gas, through fluid activating device, is mixed and is magnetized activation, wherein, mix waste gas in oxygen be magnetic susceptibility relatively High paramagnetic gas, under the magnetic fields that fluid magnetic assembly is formed, the activation energy of the oxygen in mixing waste gas is by significantly Improve；Secondly, the mixing waste gas being magnetized enters wet type high voltage electrostatic device, in the environment of high-voltage electrostatic field, is magnetized Electronics, ion and the free radical that oxygen, high-pressure electrostatic FI go out all with waste gas in macromolecular particle and micro-molecular gas Decompose reaction；Finally, waste gas is decomposed into small molecule grease, carbon dioxide and water vapour.Waste gas through activation activation Reducing intermolecular force, thus substantially reducing the energy that waste gas purification process is consumed, improve exhaust treatment efficiency.

Brief description

Fig. 1 is the front view of the exhaust treatment system that the utility model embodiment one provides；

Fig. 2 is the sectional view at A-A in Fig. 1；

Fig. 3 is the explosive view of the fluid activating device that the utility model embodiment one provides；

Fig. 4 is the top view of the fluid magnetic assembly that the utility model embodiment one provides；

Fig. 5 is another top view of the fluid magnetic assembly that the utility model embodiment one provides；

Fig. 6 is the partial sectional view of the wet type high voltage electrostatic device that the utility model embodiment one provides；

Fig. 7 is the structural representation of the high temperature electrostatic reactor that the utility model embodiment one provides；

Fig. 8 is the enlarged drawing at B in Fig. 7；

Fig. 9 is the profile of the second negative electrode line segment that the utility model embodiment one provides；

Figure 10 is the structural representation of the suspender that the utility model embodiment one provides；

Figure 11 is the structural representation of the gas diffusion plate that the utility model embodiment one provides；

Figure 12 is the structural representation of the liquid waste treating apparatus that the utility model embodiment one provides；

Figure 13 is the enlarged drawing at C in Figure 12；

Figure 14 is the structural representation of the fluid magnetic assembly that the utility model embodiment two provides；

Figure 15 is the explosive view of the fluid magnetic assembly that the utility model embodiment two provides；

Figure 16 is the structural representation of the fluid activating device that the utility model embodiment two provides.

Specific embodiment

In order that the purpose of this utility model, technical scheme and advantage become more apparent, below in conjunction with accompanying drawing and enforcement Example, is further elaborated to the utility model.It should be appreciated that specific embodiment described herein is only in order to explain The utility model, is not used to limit the utility model.

It should be noted that when element is referred to as on " being fixed on " or " being arranged at " another element, it can be direct On another element or be connected on another element.When an element is known as " connection " another element, it can To be to be directly connected to another element or be indirectly connected on this another element.

Also, it should be noted the orientation term such as left and right, upper and lower, top in the present embodiment, bottom, it is only relatively general each other Read or with the normal operating condition of product as reference, and should not be regarded as restrictive.

Below in conjunction with specific embodiment, realization of the present utility model is described in detail.

Embodiment one

Refer to Fig. 1 and Fig. 2, the exhaust treatment system that the utility model embodiment provides, including for mixing and magnetic Change the fluid activating device 1 of waste gas and the wet type high voltage electrostatic device 2 for purifying waste gas, wet type high voltage electrostatic device 2 is even Lead in fluid activating device 1, waste gas flows through fluid activating device 1 and wet type high voltage electrostatic device 2 successively, and high via wet type Pressure electrostatic equipment 2 is expelled to outside, and fluid activating device 1 includes fluid and mixes assembly 11 and multiple fluid magnetic assembly 12.

The exhaust treatment system that the utility model embodiment provides, its operation principle is as follows：First, waste gas swashs through fluid Removable mounting puts 1, is mixed and magnetized activation, and wherein, the oxygen mixing in waste gas is the higher paramagnetic gas of magnetic susceptibility, in stream Under the magnetic fields that body magnetising assembly 12 is formed, the activation energy mixing the oxygen in waste gas is greatly improved；Secondly, it is magnetized Mix waste gas and enter wet type high voltage electrostatic device 2, in the environment of high-voltage electrostatic field, the oxygen being magnetized, high-voltage electrostatic field are electric Electronics, ion and the free radical separating out all with waste gas in macromolecular particle and micro-molecular gas decompose reaction；Finally, Waste gas is decomposed into small molecule grease, carbon dioxide and water vapour.Reduce intermolecular force through the waste gas of activation activation, Thus substantially reducing the energy that waste gas purification process is consumed, improve exhaust treatment efficiency.

It should be noted that in fluid activating device 1, each fluid magnetic assembly 12 can mix assembly 11 located at fluid Interior, also can mix outside assembly 11 located at fluid.

Specifically, refer to Fig. 2 to Fig. 5, in the present embodiment, fluid mix assembly 11 include first sleeve 111 and Mixing structure 112 in first sleeve 111, first sleeve 111 is communicated in wet type high voltage electrostatic device 2, multiple fluid magnetic Change assembly 12 to be sequentially arranged in from top to bottom in mixing structure 112, each fluid magnetic assembly 12 includes consolidating in mixing structure Determine ring 121 and multiple magnetic part 122, retainer ring 121 is arranged with central shaft with mixing structure 112, each magnetic part 122 is with fixation It is in circumferentially distributed centered on the vertical axis of ring 121 in retainer ring 121.When waste gas enters in first sleeve 111, by mixing Even structure 112 mixes, and, the multiple magnetic parts 122 enclosing in retainer ring 121 form toroidal magnetic field, and so, waste gas then may be used While mixing, also activation is magnetized by toroidal magnetic field, be that pretreatment work is carried out in the purification of waste gas.Preferably, refer to figure, , from top to bottom located at the outside mixing structure 112, multiple magnetic parts 122 are then with the central shaft of retainer ring 121 for multiple retainer ring 121 Centered on enclose in retainer ring 121 in circumference.Certainly, according to actual real needs, each retainer ring 121 also can be tied located at mixing Inside structure 112.

Preferably, refer to Fig. 2 to Fig. 5, in the present embodiment, mixing structure 112 is one in first sleeve 111 Hollow tube, hollow tube is arranged with central shaft with first sleeve 111, and the caliber of hollow tube is passed from middle part step by step to two ends Increase, that is, be in be further opened with some engraved structure 11a for mixing gas in hourglass shape, and, hollow tube.Here, flow Body mixes assembly 11 and is in the state that vertically erects, and waste gas then enters from the bottom of first sleeve 111 under unpowered power-assisted, according to Venturi principle, air-flow when narrow space, accelerate, and that is, when waste gas is in the middle part of hollow tube, flow velocity adds by its flow velocity Hurry up, meanwhile, engraved structure 11a can increased the collision probability of waste gas and hollow tube tube wall, improves the mixing dynamics of waste gas. Wherein it is preferred to, refer to figure, engraved structure 11a is multiple from hollow tube bottom spiral to hollow tube top The slot in portion, each slot equal spacings centered on the vertical axis of hollow tube set on hollow tube, So, waste gas, when through hollow tube, produces spiral thrust, also shortens and flow through fluid while improving Blending Efficiency of Blending Mix the time of assembly 11, improve waste gas early stage treatment effeciency.

Preferably, refer to Fig. 4, in the present embodiment, magnetic part 122 is bar magnet, and each fluid magnetic assembly 12 wraps Include four bar magnets, between four bar magnets, 90 ° of angles enclose in retainer ring 121 each other.Specifically, four bar shaped magnetic Iron is respectively the first bar magnet 12a, the second bar magnet 12b, Article 3 shape magnet 12c and Article 4 shape magnet 12d, phase 90 ° of angles each other between adjacent two bar magnets, that is, the first bar magnet 12a and Article 3 shape magnet 12c be oppositely arranged, Article 2 Shape magnet 12b is oppositely arranged with Article 4 shape magnet 12d, and, adjacent two bar magnets magnetic portion magnetic pole inequality outwardly, i.e. The magnetic portion of the first bar magnet 12a is oppositely arranged with the magnetic portion different pole of Article 3 shape magnet 12c, the second bar magnet 12b's Magnetic portion is oppositely arranged with the magnetic portion different pole of Article 4 shape magnet 12d.Specifically, the specification of each bar magnet is 5*3*0.5cm, A diameter of 20cm of first sleeve 111, records：The magnetic flux of the center (i.e. at inwall 10cm) of first sleeve 111 For 0.81-0.95mt；In first sleeve 111, the magnetic flux at inwall 3cm is 0.63-0.82mt；Outside first sleeve 111 external distance Magnetic flux at wall 3cm is 0.25-0.43mt.

Preferably, refer to Fig. 5, in the present embodiment, magnetic part 122 is bar magnet, and each fluid magnetic assembly 12 wraps Include six bar magnets, between six bar magnets, 60 ° of angles enclose in retainer ring 121 each other.Specifically, six bar shaped magnetic Iron is the first bar magnet 12a, the second bar magnet 12b, Article 3 shape magnet 12c, Article 4 shape magnet 12d, Article 5 shape 60 ° of angles each other between magnet 12e and Article 6 shape magnet 12f, i.e. the first bar magnet 12a and Article 4 shape magnet 12d It is oppositely arranged, the second bar magnet 12b is oppositely arranged with Article 5 shape magnet 12e, Article 3 shape magnet 12c and Article 6 shape Magnet 12f is oppositely arranged, and, adjacent two bar magnets magnetic portion magnetic pole inequality outwardly, i.e. the magnetic of the first bar magnet 12a Portion is oppositely arranged with the magnetic portion different pole of Article 3 shape magnet 12c, the magnetic portion of the second bar magnet 12b and Article 4 shape magnet The magnetic portion different pole of 12d is oppositely arranged, the magnetic portion different pole phase of the magnetic portion of Article 3 shape magnet 12c and Article 6 shape magnet 12f To setting.Specifically, the specification of each bar magnet is 5*3*0.5cm, a diameter of 20cm of first sleeve 111, records：First set The magnetic flux of the center (i.e. at inwall 10cm) of pipe 111 is 0.85-1.05mt；Away from inwall 3cm in first sleeve 111 The magnetic flux at place is 4.6-5.5mt；Magnetic flux at first sleeve 111 external distance outer wall 3cm is 1.53-2.56mt.

Further, refer to Fig. 6 to Figure 10, in the present embodiment, wet type high voltage electrostatic device 2 includes being communicated in fluid Mix the process chamber 21 of assembly 11, hang on high-pressure electrostatic reactor 22 in process chamber 21 and for high-pressure electrostatic reaction The control power supply group 23 of device 22 power supply, controls power supply group 23 to be electrically connected to high-pressure electrostatic reactor 22.When filling through liquid activation After putting 1, waste gas is sufficiently mixed and wherein oxygen is magnetized activation, and the waste gas after mixing is decomposed in process chamber 21 Reaction, that is, the waste gas of mixing is decomposed into little point in the higher oxygen atmosphere of activation energy by the high-pressure electrostatic reactor 22 after being energized Seed oil fat, carbon dioxide and water vapour, in whole process, power consumption is low, and the feature of environmental protection is high.

Specifically, refer to Fig. 6 to Figure 10, high-pressure electrostatic reactor 22 includes multiple being parallel to each other and spaced sun Pole collecting plate 222 and multiple cathodic discharge line 223 between two adjacent anode collecting plates 222, each anode collecting plate 222 It is electrically connected to control power supply group 23 with each cathodic discharge line 223.So, when each anode collecting plate 222 and each cathodic discharge line After 223 energisings, surrounding's generation high voltage electric field of cathodic discharge line 223, decomposes the waste gas after mixing, is broken down into small molecule oil Fat, carbon dioxide and water vapour, and, wherein obtain electrical bulky grain molecule be also adsorbed on anode collecting plate 222 or On cathodic discharge line 223.

Further, refer to Fig. 6 to Figure 10, cathodic discharge line 223 includes first negative electrode with marginal discharge function Line segment 2231 and be connected to the first negative electrode line segment 2231 and there is the second negative electrode line segment 2232 of dust collection function.Specifically, exist In whole electrostatic course of reaction, the first negative electrode line segment 2231 is strong point discharge section and the second negative electrode line segment 2232 is strong dust Functional section, so, has efficiently controlled the point discharge balance of whole cathodic discharge line 22, prevents its primer balance high pressure quiet Electrical breakdown electric field and cause high-pressure electrostatic reaction damage.Wherein, the first negative electrode line segment 2231 includes the first noumenon 223a, and first Body 223a has some first discharge electrode 223b, and each first discharge electrode 223b is the convex of the first noumenon 223a outward formation Point, the width of the first discharge electrode 223b is in successively decrease step by step towards deviating from the first noumenon 223a direction.So, when the first noumenon 223a's During power supply state, taper off to a point at each first discharge electrode 223b electric discharge.Preferably, according to specific point discharge needs, first Discharge electrode 223b is triangular in shape, i.e. the first negative electrode line segment 2231 is prickle wire.Second negative electrode line segment 2232 includes the second body 223c, the second body 223c have some second discharge electrode 223d, and each second discharge electrode 223d is with the axis of the second body 223c Centered on line be in circumferentially distributed, and by the second body 223c bottom spiral to the second body 223c top ends.This Sample, when the second body 223c is in power supply state, taper off to a point at each second discharge electrode 223d electric discharge, and two adjacent Form debris collection area between two discharge electrode 223d.Preferably, refer to figure, the cross section of the secondth discharge lines 2232 is in tri-star Shape, that is, the second negative electrode line segment 2232 is astroid.

Further, refer to Fig. 6 to Figure 10, in the present embodiment, one end of the first negative electrode line segment 2231 passes through one even Fitting 224 is connected to one end of the second negative electrode line segment 2232.So, when the first negative electrode line segment 2231 or the second negative electrode line segment 2232 When damaged occur, under first negative electrode line segment 2231 or the second negative electrode line segment 2232 being dismantled at connector 224, change new First negative electrode line segment 2231 or the second negative electrode line segment 2232.Preferably, connector 224 is an installing plate, the first negative electrode line segment 2231 and second negative electrode line segment 2232 be connected to the both sides of installing plate.

Further, refer to Fig. 6 to Figure 10, in the present embodiment, each anode collecting plate 222 and each cathodic discharge line 223 are suspended from process interior by a suspender 221, and suspender 221 is electrically connected to control power supply group.So, by controlling power supply Group is powered to suspender 221, then powers to respectively each anode collecting plate 222 and each cathodic discharge line 223 by suspender 221, when When breakage in anode collecting plate 222 or cathodic discharge line 223, can be by disassembling, assembling and replacing direct on suspender 221.

Specifically, refer to Fig. 6 to Figure 10, in the present embodiment, suspender 221 is a rectangular slab, and rectangular slab is provided with Some spliced eye 221a for the grafting of each anode collecting plate 222, be provided between two adjacent spliced eye 221a multiple for fixing The installing hole 221b of cathodic discharge line 223.So, realize the dismounting of each anode collecting plate 222 by each spliced eye 221a, lead to Cross the dismounting that each installing hole 221b realizes each cathodic discharge line 223.

Further, refer to Fig. 2 and Figure 11, in the present embodiment, also include high with wet type located at fluid activating device 1 Gas dispersion apparatus 5 between pressure electrostatic equipment 2, this gas dispersion apparatus 5 includes connecting fluid activating device 1 and wet type high pressure Second sleeve pipe 51 of electrostatic equipment 2, and it is provided with multiple gas diffusion plates 52 arranged in parallel in the second sleeve pipe 51.Mix And the waste gas being activated is through diffusion after the scattered depressed structure 52a on gas diffusion plate 52 separately, and enter wet type high-pressure electrostatic dress Put in 2, so, be conducive to high-pressure electrostatic reactor 22 fully to decompose waste gas.Preferably, refer to figure, in the second sleeve pipe 51 It is provided with two to be parallel to each other and spaced gas diffusion plate 52, the scattered depressed structure 52a on gas diffusion plate 52 is row in matrix The regular hexagon of row, when a large amount of waste gas rising uniformly diffuse into wet type high voltage electrostatic device after gas diffusion plate 52 In 2.

Preferably, in figure is not shown, in the present embodiment, is provided with annular magnet in the scattered depressed structure 52a of gas diffusion plate 52. When waste gas passes through from prose style free from parallelism structure 52a, the annular magnet being located at scattered depressed structure 52a magnetizes activation further, that is, carry out Secondary magnetization, improves the magnetization efficiency of waste gas further, reduces the power consumption of wet type high voltage electrostatic device 2.

Further, refer to Figure 12 and Figure 13, in the present embodiment, also include liquid waste treating apparatus 6, the second sleeve pipe 51 Waste liquid is discharged to liquid waste treating apparatus 6 by a collector tube 4, liquid waste treating apparatus 6 include casing 61, for separating in waste liquid admittedly The solid-liquor separation groove 62 of body particulate matter and being used for realizes the detached oil spilling groove 63 of water oil, solid-liquor separation groove 62 and waste liquid in waste liquid Source direction is corresponding and in casing 61, and the top end face of solid-liquor separation groove 62 is concordant with the top end face of casing 61, oil spilling groove 63 are disposed adjacent in casing 61 and with solid-liquor separation groove 62, and the top end face of oil spilling groove 63 is concordant with the top end face of casing 61. Initially enter solid-liquor separation groove 62 from the waste liquid of collector tube 4, here, the solid particulate matter of major diameter by solid-liquor separation groove 62 every Separate out and stay in solid-liquor separation groove 62, the waste liquid after separating enters in casing 61, constantly comes together in casing with waste liquid 61, liquid level gradually go up the top end face to casing 61 when, the fluid floating on the superiors enters in oil spilling groove 63 at first, and is stranded in Wherein, thus staying the waste liquid in casing 61 to be, impurity content is few and the liquid of the recoverable of without grease, so, will give up Liquid separates again, retains the part wherein having value.

Further, refer to Figure 12 and Figure 13, in the present embodiment, the bottom of solid-liquor separation groove 62 offers and some is in First point of fluid apertures 62a of matrix distribution, solid-liquor separation groove 62 is communicated in casing 61 by each first point of fluid apertures 62a.So, when having When waste liquid enters solid-liquor separation groove 62, and major diameter solid particulate matter is solid due to cannot be trapped in liquid by first point of fluid apertures 62a In separating tank 62, that is, pass through solid-liquor separation groove 62 and waste liquid source is carried out filtering for the first time, the waste liquid after filtration is by solid-liquor separation First point of fluid apertures 62a of groove 62 bottom enters in casing 61.Preferably, first point of fluid apertures 62a is circular port, the diameter of circular port Can be changed accordingly with being actually needed.Certainly, first point of fluid apertures 62a is alternatively other shapes.

Further, refer to Figure 12 and Figure 13, in the present embodiment, oil spilling groove 63 is towards the side of solid-liquor separation groove 62 Some second point of fluid apertures 63a in matrix distribution are offered on wall, oil spilling groove 63 is communicated in casing by each second point of fluid apertures 63a 61.Enter in casing 61 with waste liquid after being filtered by, the liquid level of waste liquid go up the top ends to casing 61 when, density is less Fluid then passes through second point of fluid apertures 63a and enters in oil spilling groove 63, thus being effectively collected to fluid.

Further, refer to Figure 12, in the present embodiment, also include the oil sump tank 64 located at casing 61 outside, oil-collecting Case 64 is communicated in oil spilling groove 63.So, the fluid being gathered in oil spilling groove 63 can finally converge in oil sump tank 64, and, works as There is a small amount of waste liquid when second point of fluid apertures 63a flows into oil sump tank 64, fluid can be driven to move, provide transmission power for fluid.

Further, refer to Figure 12, in the present embodiment, also include a draining valve 65, draining valve 65 is located at casing 61 Outside and be communicated in casing 61.So, when needing using waste liquid after filtering, directly open draining valve 65.

Further, refer to Figure 12, in the present embodiment, also include a draining valve 66, draining valve 66 is located at described collection Fuel tank 64 outside and be communicated in oil sump tank 64.Similarly, when the fluid in oil sump tank 64 is filled, can be discharged by draining valve 66 To outside.

Further, refer to Fig. 1, in the present embodiment, also include being communicated in fluid activating device 1 clears up room 7, raw Rubbish of living clears up reaction generation waste liquid and waste gas clearing up, and in waste liquid convergence rubbish reative cell 7, waste gas then flows through the room 7 in Fluid activating device 1 is magnetized activation.

Further, refer to Fig. 1 and Figure 12, in the present embodiment, liquid waste treating apparatus 6 located at clearing up above room 7, and And the draining valve 65 of liquid waste treating apparatus 6 is communicated in and clears up room 7.So, the useless of generation is purified by wet type high voltage electrostatic device 2 Liquid, after liquid waste treating apparatus 6 separate, the aqueous water having value is back to again and clears up in room 7, supplement is cleared up anti- Moisture required for answering, thus realize waste liquid effectively recycling, reduces the cost during domestic rubbish disposal.

Embodiment two

Refer to Figure 14 to Figure 16, part unlike the embodiments above is, fluid mixes assembly 11 ＇ and includes first sleeve 111 ＇ and mixing structure 112 ＇ in first sleeve 111 ＇, each fluid magnetic assembly 12 ＇ radially cross located at First sleeve 111 ＇, and can rotate relative to first sleeve 111 in perpendicular, each fluid magnetic assembly 12 ＇ is located at mixing The top of structure 112 ＇.Here, fluid mixes assembly 11 ＇ is vertical setting, and waste gas initially enters fluid mixing assembly 11 ＇ to be carried out Mix, enter line activating magnetization through fluid magnetizer again after mixing, and according to intensity of magnetization needs, each fluid can be adjusted The rotational angle relative to first sleeve 111 ＇ for magnetising assembly 12 ＇, thus obtain different activation effects.

Specifically, refer to Figure 14 to 16, in the present embodiment, fluid magnetic assembly 12 ＇ includes the footpath along first sleeve To direction be arranged in the rotary shaft 123 of first sleeve 111 ＇, fixed bin 124 in rotary shaft 123 for some parallel interval with And magnetic part 122 ＇ in each fixed bin 124, rotary shaft 123 rotates relative to first sleeve 111 ＇ around its center axis, and And at least one fixed bin 124 is located in first sleeve 111 ＇.So, fixed bin 124 is with rotary shaft 123 for center of rotation phase To first sleeve 111 ＇ rotation so that the angle between magnetic part 122 ＇ in fixed bin 124 and first sleeve 111 ＇ becomes Change, that is, the magnetic field around first sleeve 111 ＇ changes with the rotation of rotary shaft 123, to obtain different magnetization intensity of activations.Excellent Selection of land, refer to figure, and rotary shaft 123 is laterally arranged in first sleeve 111 ＇ along the radial direction of first sleeve 111 ＇, and is provided with altogether Three fixed bins 124, including the first fixed bin 124a located at rotary shaft 123 two ends and outside first sleeve 111 ＇ and Located at rotary shaft 123 middle part and the second fixed bin 124b of being located in first sleeve 111 ＇, and, two first fixed bin 124a and All there is magnetic part 122 ＇ of two settings side by side up and down, here, magnetic part 122 ＇ is bar magnet, has in second fixed bin 124b Six bar magnets, the magnetic pole of each bar magnet being wherein located at first row is towards identical, the magnetic of each bar magnet of second row Pole is contrary towards identical and with first row bar magnet magnetic pole direction.

In the present embodiment, remaining non-description section is identical with implementing one, repeats no more here.

The foregoing is only preferred embodiment of the present utility model, not in order to limit the utility model, all this Any modification, equivalent and improvement made within the spirit of utility model and principle etc., should be included in the utility model Protection domain within.

Claims (10)

1. exhaust treatment system it is characterised in that include fluid activating device for mixing and magnetizing waste gas and with institute State fluid activating device connection and the wet type high voltage electrostatic device for purifying waste gas, waste gas flows through described liquid activation dress successively Put and described wet type high-voltage electrostatic treating device, described fluid activating device includes fluid and mixes assembly and multiple fluid magnetic Assembly.

2. exhaust treatment system as claimed in claim 1 it is characterised in that described fluid mix assembly include being communicated in described Mixing structure in described first sleeve for the first sleeve of wet type high voltage electrostatic device, multiple described fluid magnetic assemblies are certainly Upper and under be sequentially arranged in described mixing structure, each described fluid magnetic assembly includes arranging with central shaft with described mixing structure And located at described mix structure on retainer ring and multiple centered on the vertical axis of described retainer ring be in circumferentially distributed Magnetic part in described retainer ring.

3. exhaust treatment system as claimed in claim 1 it is characterised in that described fluid mix assembly include being communicated in described The first sleeve of wet type high voltage electrostatic device and the mixing structure in described first sleeve, each described fluid magnetic assembly Radially cross located at described first sleeve and can rotate relative to described first sleeve in perpendicular, each described fluid magnetic Assembly includes being arranged in institute along described first sleeve radial direction located at the described top mixing structure, described fluid magnetic assembly State the rotary shaft of first sleeve, some parallel interval fixed bin in described rotary shaft and multiple located at each described fixation Magnetic part in box, described rotary shaft rotates relative to described first sleeve around its center axis, and fixed bin position at least described in In described sleeve pipe.

4. exhaust treatment system as claimed in claim 2 or claim 3 is it is characterised in that described mixing structure is one and described first The hollow tube that sleeve pipe is arranged with central shaft, the caliber of described hollow tube is incremented by from middle part step by step to two ends, described hollow tube Engraved structure for mixing gas is offered on body.

5. exhaust treatment system as claimed in claim 2 it is characterised in that described magnetic part be bar magnet, each described stream Body magnetising assembly includes four described bar magnets, and between four described bar magnets, 90 ° of angles enclose located at described fixation each other On ring.

6. exhaust treatment system as claimed in claim 3 it is characterised in that described magnetic part be bar magnet, each described bar , side by side in corresponding described fixed bin, the magnetic pole of two adjacent described bar magnets is different for shape magnet.

7. exhaust treatment system as claimed any one in claims 1 to 3 is it is characterised in that described wet type high-pressure electrostatic fills Put including the process chamber being communicated in described fluid mixing assembly, hang on the described high-pressure electrostatic reactor processing interior and use In the control power supply group providing described high-pressure electrostatic reactor.

8. exhaust treatment system as claimed in claim 7 is it is characterised in that described high-pressure electrostatic reactor includes multiple being suspended from Described process indoor and be parallel to each other and spaced anode collecting plate and between two adjacent described anode collecting plates Multiple cathodic discharge lines, each described anode collection dusting plate and each described cathodic discharge line are electrically connected to described control power supply Group.

9. exhaust treatment system as claimed in claim 7 is it is characterised in that also include located at described fluid activating device and institute State the gas dispersion apparatus between wet type high voltage electrostatic device, described gas dispersion apparatus include connecting described fluid activating device Expand with the second sleeve pipe of described wet type high voltage electrostatic device and multiple gas in described second sleeve pipe arranged in parallel Fall apart.

10. exhaust treatment system as claimed in claim 9 is it is characterised in that also include liquid waste treating apparatus, described second set Manage and waste liquid is discharged to described liquid waste treating apparatus by a collector tube, described liquid waste treating apparatus include casing, give up for separating In liquid, the solid-liquor separation groove of solid particulate matter and being used for realizes the detached oil spilling groove of water oil in waste liquid, described solid-liquor separation groove with Waste liquid source direction is corresponding and in described casing, and the top end face of described solid-liquor separation groove is put down with the top end face of described casing Together, described oil spilling groove is disposed adjacent in described casing and with described solid-liquor separation groove, the top end face of described oil spilling groove and institute The top end face stating casing is concordant.