CN202427314U - Dust-removing equipment - Google Patents
Dust-removing equipment Download PDFInfo
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- CN202427314U CN202427314U CN2012200166516U CN201220016651U CN202427314U CN 202427314 U CN202427314 U CN 202427314U CN 2012200166516 U CN2012200166516 U CN 2012200166516U CN 201220016651 U CN201220016651 U CN 201220016651U CN 202427314 U CN202427314 U CN 202427314U
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 174
- 239000007789 gas Substances 0.000 claims description 58
- 239000007921 spray Substances 0.000 claims description 32
- 230000001105 regulatory effect Effects 0.000 claims description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 4
- 239000001301 oxygen Substances 0.000 claims description 4
- 229910052760 oxygen Inorganic materials 0.000 claims description 4
- 230000008859 change Effects 0.000 claims description 3
- 230000015572 biosynthetic process Effects 0.000 claims description 2
- 238000000746 purification Methods 0.000 claims description 2
- 239000000428 dust Substances 0.000 abstract description 27
- 239000004744 fabric Substances 0.000 description 12
- 239000002912 waste gas Substances 0.000 description 11
- 230000000694 effects Effects 0.000 description 10
- 238000000926 separation method Methods 0.000 description 7
- PXFBZOLANLWPMH-UHFFFAOYSA-N 16-Epiaffinine Natural products C1C(C2=CC=CC=C2N2)=C2C(=O)CC2C(=CC)CN(C)C1C2CO PXFBZOLANLWPMH-UHFFFAOYSA-N 0.000 description 6
- 239000002699 waste material Substances 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 3
- 230000003993 interaction Effects 0.000 description 3
- 229920003023 plastic Polymers 0.000 description 3
- 239000004033 plastic Substances 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000005498 polishing Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 239000004575 stone Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 241000282326 Felis catus Species 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003500 flue dust Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
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- 230000010148 water-pollination Effects 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
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Abstract
Dust-removing equipment comprises an auxiliary cyclone tower, a main cyclone tower and a water tank, wherein the auxiliary cyclone tower comprises an auxiliary tower air inlet, an auxiliary tower air outlet and an auxiliary tower water sprinkling and atomizing device, the auxiliary tower air inlet is formed at the lateral upper part of the auxiliary cyclone tower, the auxiliary tower air outlet is formed at the top of the auxiliary cyclone tower and the auxiliary tower water sprinkling and atomizing device is arranged above the auxiliary cyclone tower; the main cyclone tower comprises a main tower air inlet, a main tower water sprinkling and atomizing device and flow guide units, the main tower air inlet is formed at the lateral upper part of the main cyclone tower and connected with the air outlet of the auxiliary cyclone tower, the main tower water sprinkling and atomizing device is arranged at the top of the main cyclone tower, and a plurality of groups of flow guide units are arranged in the middle of the main cyclone tower from the top down; and the water tank is arranged below the auxiliary cyclone tower and the main cyclone tower and forms a closed whole together with the two towers. Compared with the prior art, the dust-removing equipment can achieve high-efficiency removal of wax-bearing dust.
Description
Technical field
The utility model belongs to environmental protection cleaner field, is specifically related to a kind of cleaner.
Background technology
Traditional content of wax dirt firmly admittedly refers to the band wax dust that meeting forms the cloth bag obstruction of physics, is often referred to the metal of use buffing wax or the polishing dirt of plastics.But in the work of reality, the inventor finds that also other situation also can produce the obstruction of cloth bag, like the particle of plastics, cutting flue dust etc., also can make cloth bag all block in a short period of time and can not clear up.To be plastics be accompanied by high temperature to its reason in broken, cutting process produced chemical reaction, forms the chemical substance of some high viscosities.Therefore, in present patent application, consolidate the dust that dirt is defined as the cloth bag obstruction that can form physics or chemistry to the content of wax firmly.
At present, generally adopt showering deduster or pocked stone pagoda formula deduster to remove content of wax dirt firmly admittedly, but the efficiency of dust collection of above-mentioned two kinds of dedusters is lower, generally its efficiency of dust collection≤75%.And owing to contain a large amount of cloth suede, shred or cloth waste sheet etc. in the polishing dirt; In traditional showering deduster or pocked stone pagoda formula deduster, very easily produce the conglomeration blockage problem of cloth suede, shred or cloth waste sheet, cause deduster can't normally move use.
Therefore, seek that a kind of can to solve the content of wax cleaner that blockage problem and the efficiency of dust collection of dirt is high firmly admittedly imperative.
The utility model content
The purpose of the utility model is to overcome shortcoming of the prior art with not enough, provides a kind of and consolidates the cleaner that dirt is realized the high efficiency dedusting firmly to the content of wax.
The utility model is to realize through following technical scheme: a kind of cleaner comprises whirlwind secondary tower, eddy flow king-tower and pond.Wherein, The whirlwind secondary tower comprises secondary tower air inlet, secondary tower gas outlet and secondary tower water spray atomising device, and this secondary tower air inlet is arranged on the upper lateral part of this whirlwind secondary tower; This secondary tower gas outlet is arranged on the top of this whirlwind secondary tower, and this secondary tower water spray atomising device is arranged on the top of this whirlwind secondary tower; This eddy flow king-tower comprises king-tower air inlet, king-tower water spray atomising device and flow guiding unit; This king-tower air inlet is arranged on the upper lateral part of this eddy flow king-tower; Be connected through the gas outlet of guide duct with the whirlwind secondary tower; This king-tower water spray atomising device is arranged on the top of this eddy flow king-tower, organizes the middle part that flow guiding unit is arranged on this eddy flow king-tower from top to bottom more, thereby forms a plurality of water conservancy diversion layers; This pond is arranged on the below of this whirlwind secondary tower and eddy flow king-tower, and constitutes a sealed whole body jointly.
This eddy flow king-tower also comprises the dewatering plate of a plurality of strips, and it is arranged on the below of this flow guiding unit.
This cleaner also comprises gas and water separator; It is arranged on the top in this pond; With sealed whole body of the common formation in this whirlwind secondary tower, eddy flow king-tower and pond, this gas and water separator comprises the multilayer dewatering unit of the portion of setting within it, and the pure qi (oxygen) gas outlet that is arranged on the one of which side.
This cleaner also comprises the air water preseparator, and it is arranged on this eddy flow king-tower and the dirt gas passage between the gas and water separator on the water termination in this pond, and this air water preseparator comprises the preparatory dewatering unit of multiple row.
Also comprise water circulating pump, the water pipe of this water circulating pump is connected with this secondary tower water spray atomising device and king-tower water spray atomising device respectively, and water purification is imported to this whirlwind secondary tower and the eddy flow king-tower sprays processing to dirt gas.This water circulating pump also comprises filter and water regulating valve, and this filter is netted, is arranged near its water inlet, and this water regulating valve is arranged on the water pipe of shower nozzle that secondary tower water spray atomising device and king-tower water sprays atomising device.
This cleaner also comprises water purifying tank, and this water purifying tank is arranged on a side in this pond and keeps being communicated with this pond, and the water inlet of this water circulating pump is arranged on the side of water purifying tank near its bottom.
Further, this flow guiding unit is made up of a plurality of water conservancy diversion flaps, and this water conservancy diversion flap comprises fixed head at an angle to each other and deflector, and a plurality of fixed heads are tiled at interval an annular in the horizontal direction, this deflector downward-sloping with this fixed head at angle.Fixed head and the angle between the deflector at the water conservancy diversion flap of different water conservancy diversion layers are different, and the fixed head of this multilayer flow guiding unit and the gradual change from top to bottom of the angle between the deflector reduce.
This gas and water separator comprises 6-12 pull-up water unit, and this dewatering unit is made up of the equidistant dense arrangement of a plurality of " V " template spares, and its plane of the opening is towards the pond, and " V " the template spare that falls of the dewatering unit of neighbouring layer is interspersed.
The preparatory dewatering unit of 3-6 row is set in this air water preseparator; This preparatory dewatering unit is made up of a plurality of " V " template spare dense arrangement; Its plane of the opening is vertical with the water termination in this pond also to be the direction of facining the wind; And " V " template spare of the preparatory dewatering unit of front and back adjacent columns is interspersed, and " V " template spare of each row is that the non-equidistance that dredge middle close both sides is arranged.
With respect to prior art, the cleaner of the utility model can solve the content of wax and consolidate the blockage problem of dirt to cleaner firmly to content of wax dirt realization high efficiency dedusting firmly admittedly simultaneously, it is hereby ensured efficiently normally operation of cleaner.
In order to understand the utility model more clearly, below accompanying drawings is set forth the specific embodiment of the utility model.
Description of drawings
Fig. 1 is the structural representation of the cleaner of the utility model.
Fig. 2 is the vertical view of flow guiding unit 23 shown in Figure 1.
Fig. 3 is the structural representation of water conservancy diversion flap 232 shown in Figure 2.
Fig. 4 is the cutaway view of Fig. 2 along the C-D direction.
Fig. 5 is the structure for amplifying sketch map of the dewatering unit of gas and water separator.
The specific embodiment
See also Fig. 1, it is the structural representation of the cleaner of the utility model.This cleaner comprises whirlwind secondary tower 10,80.This pond 50 is arranged on the below of this whirlwind secondary tower 10, eddy flow king-tower 20 and gas and water separator 40.Dust-laden exhaust gas carries out dust removal process through this whirlwind secondary tower 10, eddy flow king-tower 20, air water preseparator 30 and gas and water separator 40 in regular turn, makes dust fall into pond 50.The waste water in this pond 50 flows into this water purifying tank 70 through filtering the back, and water circulating pump 60 imports to this whirlwind secondary tower 10 through its water pipe respectively with the water of water purifying tank 70 and sprays processing with 20 pairs of dirt gas of eddy flow king-tower.
This whirlwind secondary tower 10 is a hollow columnar structures, and particularly, its top is cylinder, and the bottom is the little stage body of the big under shed of upper shed.This whirlwind secondary tower 10 comprises secondary tower air inlet 11, secondary tower gas outlet 12 and secondary tower water spray atomising device 13.This secondary tower air inlet 11 is arranged on the upper lateral part on these whirlwind secondary tower 10 tops; This secondary tower air inlet 11 is a tubulose; Section is a rectangle; The less one side of its length, makes waste gas pass through this secondary tower air inlet 11 and in whirlwind secondary tower 10, forms the eddy flow wind under the clockwise tangential in conjunction with the structure of this whirlwind secondary tower 10 from the horizontal by downward-sloping this whirlwind secondary tower 10 that stretches into of certain angle.This secondary tower gas outlet 12 is arranged on the top of this whirlwind secondary tower 10.This secondary tower water spray atomising device 13 is arranged on the top of this whirlwind secondary tower 10; Comprise 4-6 shower nozzle composition that evenly distributes and be connected with this water circulating pump 60; The position of the corresponding shower nozzle of these whirlwind secondary tower 10 cats head has spray apertures, sealed wall is set to connect shower nozzle around the spray apertures.The bottom of this whirlwind secondary tower 10 is tightly connected through the flange on the stage body that is arranged on these whirlwind secondary tower 10 bottoms 14 and this pond 50.In use, make the bottom of this whirlwind secondary tower 10 insert the water termination 55 following 400mm in pond 50, make the sealing surface of water termination 55 as this whirlwind secondary tower 10.
This eddy flow king-tower 20 is similarly hollow columnar structures, and particularly, its top is cylinder, and the middle part is that the little stage body of the big under shed of upper shed, bottom are the big stage body of the little under shed of upper shed.This eddy flow king-tower 20 comprises king-tower air inlet 21, king-tower water spray atomising device 22, flow guiding unit 23, dewatering plate 24 and access hole 27.This king-tower air inlet 21 is arranged on the upper lateral part of this eddy flow king-tower 20; Be connected with the gas outlet 12 of whirlwind secondary tower 10 through guide duct 80, this guide duct 80 comprises that specifically one section cross section is tightly connected and forms for circular 90 ° of bend pipes and one section section become square reducer pipe by circle.This king-tower water spray atomising device 22 is arranged on the top of this eddy flow king-tower 20, comprises 4-6 shower nozzle composition that evenly distributes and be connected with this water circulating pump 60.Many group flow guiding units 23 are arranged on the middle part of this eddy flow king-tower 20 from top to bottom, thereby form up big and down small a plurality of water conservancy diversion layers, wherein, generally at this eddy flow king-tower 20 4-8 group flow guiding unit 23 are set.Air-flow moves towards identical in the trend of this flow guiding unit 23 with the air-flow of this king-tower air inlet 21, is the direction under the clockwise tangential.This dewatering plate 24 is a strip, and its vertical welding is arranged on the decurrence section of the middle part stage body of this eddy flow king-tower 20, the i.e. below of this flow guiding unit 23.The bottom of this eddy flow king-tower 20 is tightly connected through flange 26 and pond 50.This access hole 27 is arranged on the top of this eddy flow king-tower 20.
See also Fig. 2, it is the vertical view of flow guiding unit 23 shown in Figure 1.The flow guiding unit 23 of each layer is arranged in annular louvered structure in regular turn by the identical water conservancy diversion flap 232 of a plurality of structures.Please consult Fig. 3 simultaneously, it is the structural representation of water conservancy diversion flap 232 shown in Figure 2.This water conservancy diversion flap 232 comprises fixed head 232a at an angle to each other and deflector 232b, and this fixed head 232a and deflector 232b are fan-shaped.Please consult Fig. 4 simultaneously, it is the cutaway view of Fig. 2 along the C-D direction.A plurality of fixed head 232a equal intervals in the horizontal direction are tiled into an annular at interval, have trapezoidal space between the adjacent fixed plate 232a; This deflector 232b downward-sloping with this fixed head 232a α at angle; Form the guide flow path of fixed-direction; Make this deflector 232b of dirt gas downward-sloping with this fixed head 232a α at angle, form the guide flow path of fixed-direction, the wind direction that makes dirt gas is clockwise eddy flow wind.The area of this deflector 232b be this fixed head 232a area 4-6 doubly.At the outer shroud of this flow guiding unit 23 and interior ring bracing frame being set all supports and fixedly installs.Have the gap between the inwall of this flow guiding unit 23 and this eddy flow king-tower 20, this gap is generally 10-20mm, so that current descend along this gap eddy flow.
The flow guiding unit 23 that is arranged in one deck comprises two kinds of gas gaps excessively, the gas gap excessively that constitutes between gas gap excessively that promptly constitutes between the adjacent fixed plate 232a and the adjacent baffle 232b.Wherein, what constitute between the adjacent baffle 232b crosses the gas interval area greater than the area of crossing the gas gap that constitutes between the adjacent fixed plate 232a, crosses the benchmark reference of gas interval area as control waste gas wind speed what constitute between with adjacent baffle 232b in the design.Because the middle part of this eddy flow king-tower 20 is the little stage body of the big under shed of upper shed; The annulus area that the fixed head 232a of multilayer flow guiding unit 23 constitutes reduces rapidly from top to bottom; The gas interval area of crossing that constitutes between this deflector 232b also reduces thereupon, thus the increase rapidly in the process of the flow guiding unit 23 through different layers in regular turn from top to bottom of the wind speed that makes waste gas and flow rate of water flow.Controlled for the accelerator of the wind speed that makes waste gas and flow rate of water flow, need realize through the fixed head 232a of control multilayer flow guiding unit and the angle [alpha] between the deflector 232b.Particularly; The fixed head 232a of this multilayer flow guiding unit and the angle [alpha] gradual change from top to bottom between the deflector 232b reduce; Fixed head 232a and the angle between the deflector 232b from the nearer flow guiding unit 23 of king-tower air inlet 21 are bigger; Be traditionally arranged to be 145 °～160 °, make its guide flow path milder; Fixed head 232a and the angle between the deflector 232b from king-tower air inlet 21 flow guiding unit 23 far away are less, are traditionally arranged to be 135 °～145 °, make its guide flow path straight steep, thereby wind speed and flow rate of water flow are increased progressively gradually.Generally, need be controlled at 16-28m/s with wind speed and water velocity in this flow guiding unit 23, and are increased gradually from following wind speed by last.
This gas and water separator 40 is a square box, and it is arranged on the top in this pond 50 and is tightly connected through flange 41 and this pond 50.This gas and water separator 40 comprises the multilayer dewatering unit 42 of the portion of setting within it, the dewatering unit 42 of operated by rotary motion 6-12 layer, and to make the angle between dewatering unit 42 and the water termination 55 be 45 °.See also Fig. 5, it is the structure for amplifying sketch map of the dewatering unit of this gas and water separator.The dewatering unit 42 of each layer is made up of a plurality of " V " template spare 421 equidistant dense arrangement of falling, and its opening is the windward side, promptly the opening surface of " V " template spare towards the pond 50 water termination 55.Wherein, " V " the template spare 421 that falls of the dewatering unit 42 of neighbouring layer is interspersed.The interior angle of " V " template spare 421 is 60 °～130 °.Pure qi (oxygen) gas outlet 43 is arranged on a side of this gas and water separator 40.
Further, water termination 55 tops in this pond 50 are a dirt gas passage 56, and this air water preseparator 30 is arranged on the dirt gas passage 56 between this eddy flow king-tower 20 and the gas and water separator 40.This air water preseparator 30 comprises the preparatory dewatering unit 32 of multiple row, the preparatory dewatering unit 32 of operated by rotary motion 3-6 row.The preparatory dewatering unit 32 of each row is made up of a plurality of " V " template spare dense arrangement, and its opening is the air inducing face, and the plane of the opening that promptly is somebody's turn to do " V " template spare is vertical with the water termination 55 in this pond 50.Wherein, " V " template spare of the preparatory dewatering unit 32 of front and back adjacent columns is interspersed, and " V " template spare of each row is that non-equidistance is arranged, but middle close both sides dredge, so that play equal wind action simultaneously.
And constitute a sealed whole body jointly.The bottom in this pond 50 is a funnel structure, and be provided with a discharge outlet 51 in the bottom of funnel structure clean to guarantee pond 50 drainings, on this discharge outlet 51, disposes a drainage valve 52.These pond 50 sidewalls are provided with access hole 53 and near the baffle plate 54 that is arranged on the access hole 53, and this baffle plate 54 inserts water terminations 55 following 400mm, when preventing work owing to negative pressure acts on the gas leakage that this access hole 51 causes water level decline.Thus, this dirt gas passage 56 is the baffle plate 54 common confined spaces that constitute of this eddy flow king-tower 20, gas and water separator 40, water termination 55 and 50 both sides, pond.
This water purifying tank 70 is arranged on a side in this pond 50, discharge outlet 51 height such as grade in the bottom of this water purifying tank 70 and this pond 50, and this water purifying tank 70 keeps being communicated with this pond 50 through the water hole 72 of its bottom.Further, pond 50 1 sides above this water hole 72 also are provided with one group of angle-inserting type and washable screen pack 73, can be with the dust-filtering in the pond 50 so that get into the water cleaning of water purifying tank 70.
This water circulating pump 60 comprises the pump housing 61, water inlet 62, filter 63, water pipe 64 and water regulating valve 65.This water inlet 62 is arranged on the side of water purifying tank 70 near its bottom.This filter 63 is netted, and it is neighbouring to guarantee to get into the water cleaning of this water circulating pump 60 to be arranged on water inlet 62.Between this water inlet 62 and the pump housing 61; And the pump housing 61 and secondary tower water spray atomising device 13, and king-tower water spray atomising device 22 between be connected through water pipe 64; This water regulating valve 65 is arranged on the water pipe of the secondary tower water spray atomising device 13 and the shower nozzle of king-tower water spray atomising device 22, with the injection flow rate of control secondary tower water spray atomising device 13 and king-tower water spray atomising device 22.
Below specify the dust-cleaning principle of cleaner of the present invention.
When content of wax dust passed through secondary tower air inlet 11 these whirlwind secondary towers 10 of entering, the water spraying and dedusting strength intersection superposition that cyclone dust removal strength that this whirlwind secondary tower 10 produces and secondary tower water spray atomising device 13 produce carried out the dedusting effect to content of wax dust.The cloth suede of the very easily suction weightening finish in the content of wax dust, shred, cloth waste sheet equal-volume is big and the impurity dust of light specific gravity, is very easily fallen into by cyclone dust removal superposition water spraying and dedusting force action to obtain in the pond 50 removing.Like this, the dedusting effect through this whirlwind secondary tower 10 gets in the dust-laden exhaust gas of eddy flow king-tower 20, does not have impurity dust such as big or long cloth suede, shred, cloth waste sheet basically, but with in carefully to the fine particle size content of wax firmly admittedly dirt be main.Avoided blockage problem thus, also done preliminary immixture preparation simultaneously for next step affinity interaction that content of wax is consolidated dirt and water firmly at this eddy flow king-tower 20.
Consolidate dirt waste gas entering eddy flow king-tower 20 firmly through the elementary dedusting of whirlwind secondary tower 10 and the content of wax of elementary dirt water immixture.At first; Under the pressure eddy flow guide effect of the multilayer flow guiding unit 23 of this eddy flow king-tower 20, affinity interaction has taken place through repeatedly violent extruding, eddy flow, collision effect between dirt and the water in airborne water and dirt; Final the two so that affine be one, do not separate mutually.When dirt with water is affine when being one, just set up the state of matter basis that the purpose of dedusting is converted into the purpose of gas-water separation.Can know that by general general knowledge gas-water separation can reach very high efficient, and then can reach very high efficiency of dust collection.Therefore, the leading role of this eddy flow king-tower 20 is to be one with dirt and water are affine, forms the state of matter basis of dirt water one, prepares for the gas-water separation effect in the gas and water separator 40 of next step performs the basis.In addition; Because most of eddy flow water becomes boundling current at a high speed under the effect of dewatering plate 24; Directly fall into the pond and Returning flow no longer; Therefore, most of carse, medium and small particle diameter content of wax dust is effectively separated in the waste gas, have only few part with water affine for one carefully to the fine particle size content of wax firmly admittedly dirt float on to be brought in the air with waste gas and further separate removing in the gas and water separator 40.
Whether wherein, the waste gas flow velocity of the deflector in this eddy flow king-tower 20 and the number of plies of flow guiding unit 23 are two relatively The key factor, can make the content of wax consolidate dirt and water completion affinity interaction firmly and promptly depend on this two factors.Generally speaking these two factors also depend on the content of wax of handling dirt characteristic firmly admittedly.If the content of wax of handling firmly admittedly dirt itself be possess hydrophilic property, then the deflector wind speed can hang down, the number of plies of flow guiding unit 23 also can be less.On the contrary, if the content of wax dust of handling itself promptly has not hydrophily, then the deflector wind speed should be high, and the number of plies of flow guiding unit 23 also should be some more.Generally speaking, the wind speed of deflector is controlled between the 16-28m/s, the number of plies of flow guiding unit 23 is set to the 4-8 layer.Concrete parameter can be adjusted according to the hydrophilic characteristics of processing dust.
After handling through eddy flow king-tower 20 with water affine content of wax dirt waste gas firmly admittedly; After the air water pre-separation and equal wind effect of dirt gas passage 56 through air water preseparator 30; Get in the gas and water separator 40; Under the effect of the dewatering unit 42 of the multilayer of this gas and water separator 40, realize the high efficiency gas-water separation, thereby realize that high efficiency dirt gas separates.Dust-laden waste water flows in the pond 50 along inclination direction along falling the inside groove of " V " template spare 421, and " clean " exhaust gas 43 is discharged from the pure qi (oxygen) gas outlet.Wherein, with water affine the content of wax flow velocity of dirt waste gas in dewatering unit 42 and the number of plies of dewatering unit 42 (being waste gas break-in number of times) firmly admittedly, determined the efficient of gas-water separation.General flow velocity in this dewatering unit 42 is higher, and the more then gas-water separation efficient is higher for the break-in number of times, but its energy consumption is also just big.Therefore, generally its flow velocity is set between the 22-28m/s, dewatering unit 42 is traditionally arranged to be the 6-12 layer.Also can confirm this two parameters according to the characteristic of content of wax dust.
With respect to prior art, cleaner of the present invention can solve the blockage problem of content of wax dust to cleaner simultaneously to content of wax dirt realization high efficiency dedusting firmly admittedly, it is hereby ensured efficiently normally operation of cleaner.In addition, can also be applied to the high-effective dust-removing in other dedusting fields.The efficiency of dust collection of cleaner of the present invention can reach>=and 99.99%, dust removing effects reaches dust content≤25mg/m3 in the " clean " exhaust gas, reaches the efficiency of dust collection and the effect that are similar to bag-type dust equipment.This cleaner running resistance≤1200pa is suitable with general bag-type dust equipment energy consumption.
The present invention is not limited to above-mentioned embodiment; If various changes of the present invention or distortion are not broken away from the spirit and scope of the present invention; If these changes and distortion belong within claim of the present invention and the equivalent technologies scope, then the present invention also is intended to comprise these changes and distortion.
Claims (15)
1. a cleaner is characterized in that: comprise
---the whirlwind secondary tower; Comprise secondary tower air inlet, secondary tower gas outlet and secondary tower water spray atomising device; This secondary tower air inlet is arranged on the upper lateral part of this whirlwind secondary tower, and this secondary tower gas outlet is arranged on the top of this whirlwind secondary tower, and this secondary tower water spray atomising device is arranged on the top of this whirlwind secondary tower;
---the eddy flow king-tower; Comprise king-tower air inlet, king-tower water spray atomising device and flow guiding unit; This king-tower air inlet is arranged on the upper lateral part of this eddy flow king-tower, is connected through the gas outlet of guide duct with the whirlwind secondary tower, and this king-tower water spray atomising device is arranged on the top of this eddy flow king-tower; Many group flow guiding units are arranged on the middle part of this eddy flow king-tower from top to bottom, thereby form a plurality of water conservancy diversion layers;
---the pond, it is arranged on the below of this whirlwind secondary tower and eddy flow king-tower, and constitutes a sealed whole body jointly.
2. cleaner according to claim 1 is characterized in that: this eddy flow king-tower also comprises the dewatering plate of a plurality of strips, and it is arranged on the below of this flow guiding unit.
3. cleaner according to claim 2; It is characterized in that: this cleaner also comprises gas and water separator; It is arranged on the top in this pond; With sealed whole body of the common formation in this whirlwind secondary tower, eddy flow king-tower and pond, this gas and water separator comprises the multilayer dewatering unit of the portion of setting within it, and the pure qi (oxygen) gas outlet that is arranged on the one of which side.
4. cleaner according to claim 3; It is characterized in that: this cleaner also comprises the air water preseparator; It is arranged on this eddy flow king-tower and the dirt gas passage between the gas and water separator on the water termination in this pond, and this air water preseparator comprises the preparatory dewatering unit of multiple row.
5. cleaner according to claim 4; It is characterized in that: also comprise water circulating pump; The water pipe of this water circulating pump is connected with this secondary tower water spray atomising device and king-tower water spray atomising device respectively, and water purification is imported to this whirlwind secondary tower and the eddy flow king-tower sprays processing to dirt gas.
6. according to the described cleaner of arbitrary claim in the claim 1 to 5; It is characterized in that: this flow guiding unit is made up of a plurality of water conservancy diversion flaps; This water conservancy diversion flap comprises fixed head at an angle to each other and deflector; A plurality of fixed heads are tiled at interval an annular in the horizontal direction, this deflector downward-sloping with this fixed head at angle.
7. cleaner according to claim 6 is characterized in that: the area of this deflector be this fixed head area 4-6 doubly.
8. cleaner according to claim 6 is characterized in that: fixed head and the angle between the deflector at the water conservancy diversion flap of different water conservancy diversion layers are different, and the fixed head of this multilayer flow guiding unit and the gradual change from top to bottom of the angle between the deflector reduce.
9. cleaner according to claim 6 is characterized in that: the wind speed of deflector is controlled between the 16-28m/s, and is increased gradually by last oneself following wind speed.
10. cleaner according to claim 6 is characterized in that: the number of plies of this flow guiding unit is set to the 4-8 layer.
11. cleaner according to claim 3; It is characterized in that: this gas and water separator comprises 6-12 pull-up water unit; This dewatering unit is made up of the equidistant dense arrangement of a plurality of " V " template spares; Its plane of the opening is towards the pond, and " V " the template spare that falls of the dewatering unit of neighbouring layer is interspersed.
12. cleaner according to claim 11 is characterized in that: the interior angle of " V " template spare is 60 °～130 °.
13. cleaner according to claim 4; It is characterized in that: the preparatory dewatering unit that the 3-6 row are set in this air water preseparator; This preparatory dewatering unit is made up of a plurality of " V " template spare dense arrangement; Its plane of the opening is vertical with the water termination in this pond and for facining the wind direction, and " V " template spare of the preparatory dewatering unit of front and back adjacent columns is interspersed, and " V " template spare of each row is that the non-equidistance that dredge middle close both sides is arranged.
14. cleaner according to claim 5 is characterized in that: this cleaner also comprises water purifying tank, and this water purifying tank is arranged on a side in this pond and keeps being communicated with this pond, and the water inlet of this water circulating pump is arranged on the side of water purifying tank near its bottom.
15. cleaner according to claim 5; It is characterized in that: this water circulating pump also comprises filter and water regulating valve; This filter is netted; Be arranged near its water inlet, this water regulating valve is arranged on the water pipe of shower nozzle that secondary tower water spray atomising device and king-tower water sprays atomising device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200166516U CN202427314U (en) | 2012-01-13 | 2012-01-13 | Dust-removing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200166516U CN202427314U (en) | 2012-01-13 | 2012-01-13 | Dust-removing equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202427314U true CN202427314U (en) | 2012-09-12 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012200166516U Expired - Fee Related CN202427314U (en) | 2012-01-13 | 2012-01-13 | Dust-removing equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202427314U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102527181A (en) * | 2012-01-13 | 2012-07-04 | 黄清豹 | Dust removal equipment |
| CN104128886A (en) * | 2014-07-07 | 2014-11-05 | 长兴华锐机械设备有限公司 | Polishing and dedusting workbench |
-
2012
- 2012-01-13 CN CN2012200166516U patent/CN202427314U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102527181A (en) * | 2012-01-13 | 2012-07-04 | 黄清豹 | Dust removal equipment |
| CN104128886A (en) * | 2014-07-07 | 2014-11-05 | 长兴华锐机械设备有限公司 | Polishing and dedusting workbench |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Foshan Renju Environmental Protection Engineering Co., Ltd. Assignor: Huang Qingbao Contract record no.: 2013440000397 Denomination of utility model: Spot inspection method for dust-cleaning pulse valve of dust-removing equipment Granted publication date: 20120912 License type: Exclusive License Record date: 20130802 |
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| LICC | Enforcement, change and cancellation of record of contracts on the licence for exploitation of a patent or utility model | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20160120 Address after: 528226, No. 10, middle laurel Road, Luen Industrial Park, Luo town, Nanhai District, Guangdong, Foshan Patentee after: Foshan Renju Environmental Protection Engineering Co., Ltd. Address before: 528226, No. 10, middle laurel Road, Luen Industrial Park, Luo town, Nanhai District, Guangdong, Foshan Patentee before: Huang Qingbao |
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| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120912 Termination date: 20170113 |