CN204911088U - Special dust remover of water -curtain -type living beings - Google Patents
Special dust remover of water -curtain -type living beings Download PDFInfo
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- CN204911088U CN204911088U CN201520707503.2U CN201520707503U CN204911088U CN 204911088 U CN204911088 U CN 204911088U CN 201520707503 U CN201520707503 U CN 201520707503U CN 204911088 U CN204911088 U CN 204911088U
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- spray head
- water
- water tank
- dust
- mouth
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 133
- 239000000428 dust Substances 0.000 title claims abstract description 67
- 239000003546 flue gas Substances 0.000 claims abstract description 41
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 40
- 239000007921 spray Substances 0.000 claims description 85
- 125000004122 cyclic group Chemical group 0.000 claims description 25
- 239000010865 sewage Substances 0.000 claims description 15
- 238000013517 stratification Methods 0.000 claims description 15
- 238000007599 discharging Methods 0.000 claims description 8
- 238000006477 desulfuration reaction Methods 0.000 abstract description 13
- 230000023556 desulfurization Effects 0.000 abstract description 13
- 230000008901 benefit Effects 0.000 abstract description 5
- 235000019504 cigarettes Nutrition 0.000 description 7
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- 238000005406 washing Methods 0.000 description 6
- 239000003500 flue dust Substances 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 238000001914 filtration Methods 0.000 description 4
- 230000003116 impacting effect Effects 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 239000013589 supplement Substances 0.000 description 4
- 239000004744 fabric Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 230000002285 radioactive effect Effects 0.000 description 3
- 238000012935 Averaging Methods 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 238000006386 neutralization reaction Methods 0.000 description 2
- 230000035699 permeability Effects 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 230000001360 synchronised effect Effects 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 230000003009 desulfurizing effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 230000000763 evoking effect Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 230000008595 infiltration Effects 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 235000011837 pasties Nutrition 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
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- Treating Waste Gases (AREA)
Abstract
The utility model discloses a special dust remover of water -curtain -type living beings, it relates to the supporting dust collecting equipment technical field of boiler. The fixed support that is provided with in below of barrel, the top of barrel is provided with into mouth, the inside of support has set gradually first shower head under to from last, the second shower head, the third shower head, first flue gas water conservancy diversion sombrero and second flue gas water conservancy diversion sombrero are installed respectively to the below of second shower head and third shower head, be provided with first convergent vortex mouth between second shower head and the third shower head, the below of third shower head is provided with second convergent vortex mouth, the below of second convergent vortex mouth is provided with the toper water knockout drum, toper water knockout drum below is provided with the dehydrator, the dehydrator is connected with outlet flue one end, the outlet flue other end is connected with the draught fan, the draught fan top is connected with the flue, its fan resistance is little, and no secondary pollution. Has desulfurization dust removal economic benefits and social benefits function, high use efficiency and less dosage. Easy operation, the operation is reasonable, high durability. Small occupied area.
Description
Technical field
The utility model relates to a kind of water curtain type living beings special dust seperator, belongs to the technical field of dust removal equipment of boiler matching.
Background technology
At present, domesticly there is no living beings special dust seperator, the basic sack cleaner of coal-burning boiler that adopts replaces using.Sack cleaner is filtration dust catcher, and it is under the effect of blower fan gravitation, by dust collection in cloth bag, according to the size of dust stratification amount, removes dust stratification on time.Flue gas after filtering, enters flue after being drawn by air-introduced machine.The dust removal efficiency of sack cleaner is higher, generally more than 90%, but without desulfurizing function.
1, sack cleaner adopts filtering type dedusting, is applicable to coal-burning boiler or mine crushing material dedusting, because the dust that fire coal and crushing material produce, is graininess body, and good air permeability is applicable to filtering type sack cleaner.But after biomass fuel combustion, the dust produced is sheet body, and lighter weight, have certain viscosity, depend on cloth bag inwall, clear up more difficult, poor air permeability, increase blower fan resistance, power consumption is large, reduces the service life of blower fan.
2, sack cleaner belongs to dry dust removal, if the dust that cleaning is got rid of does not adopt wet leaching, then in deashing and transhipment, deposit in process and produce the secondary pollution of flying upward property.
3, sack cleaner can not desulfurization, and cloth bag belongs to consumable part, needs periodic replacement, increases the operating use cost of equipment.
Summary of the invention
For the problems referred to above, the technical problems to be solved in the utility model is to provide a kind of water curtain type living beings special dust seperator.
Water curtain type living beings special dust seperator of the present utility model, it comprises into mouth, cylindrical shell, spray head, flue gas water conservancy diversion umbrella crown, convergent flow-disturbing mouth, dehydrator, dust stratification funnel, sewage discharging regulation valve, taper water knockout drum, outlet flue, bearing, drain guide pipe, spray control valve, Sprayer Circulation pipe, laying dust water tank and cyclic water tank, sewage water discharge valve, communicating pipe, communicating valve, clear water blowoff valve, water circulating pump, altitude valve, air-introduced machine and flue, described spray head is divided into the first spray head, second spray head, 3rd spray head, described flue gas water conservancy diversion umbrella crown is divided into the first flue gas water conservancy diversion umbrella crown and the second flue gas water conservancy diversion umbrella crown, described convergent flow-disturbing mouth is divided into the first convergent flow-disturbing mouth and the second convergent flow-disturbing mouth, the below of cylindrical shell is fixedly installed bearing, the top of cylindrical shell is provided with into mouth, and the inside of bearing is disposed with the first spray head from top to bottom, second spray head, 3rd spray head, the below of the second spray head and the 3rd spray head is separately installed with the first flue gas water conservancy diversion umbrella crown and the second flue gas water conservancy diversion umbrella crown, the first convergent flow-disturbing mouth is provided with between second spray head and the 3rd spray head, the below of the 3rd spray head is provided with the second convergent flow-disturbing mouth, the below of the second convergent flow-disturbing mouth is provided with taper water knockout drum, the below of taper water knockout drum is provided with dehydrator, dehydrator is connected with one end of outlet flue, the other end of outlet flue is connected with air-introduced machine, the top of air-introduced machine is connected with flue, the bottom of cylindrical shell is arranged and dust stratification funnel, dust stratification funnel is communicated with laying dust water tank by drain guide pipe, drain guide pipe is provided with sewage discharging regulation valve, laying dust water tank side is provided with cyclic water tank, the top of cyclic water tank is provided with altitude valve, and laying dust water tank is connected by communicating pipe with between cyclic water tank, communicating pipe is provided with communicating valve, the below of laying dust water tank is connected with sewage water discharge valve, the below of cyclic water tank is connected with clear water blowoff valve.
As preferably, described cyclic water tank is connected with the first spray head, the second spray head, the 3rd spray head by Sprayer Circulation pipe, and the junction of Sprayer Circulation pipe and the first spray head, the second spray head, the 3rd spray head is provided with spray control valve.
As preferably, described Sprayer Circulation pipe the junction of cyclic water tank is provided with water circulating pump.
As preferably, the inside of described dehydrator is provided with water strainer and inner bag.
The beneficial effects of the utility model: 1, blower fan resistance is little; The spray direction of multi-stage spray is consistent with flow of flue gas direction, reduces air inducing resistance, reduces air-introduced machine load, saves electric energy.
2, non-secondary pollution; The design adopts Wet-type desulfurize and dust removing, and dust is pasty state after getting rid of precipitation, forms caking after dry, is convenient to store and transport, can not cause the secondary pollution of airborne dust.
3, there is desulfurization and dedusting economic benefits and social benefits function; What the design adopted is alkali lye spray desulfurization and dedusting method, and mixing wastewater with air desulfurization and dedusting method.While desulfurization, carry out dedusting again.
4, service efficiency is high; The desulfurization degree of equipment is 100%, and dust removal efficiency is 100%, and recirculated water utilization rate is 100%.
5, simple to operate, run rationally; After rigging up and debugging is qualified, spray and blower fan synchronous averaging, need not adjust.
6, durable in use; Equipment complete machine adopts acid and alkali-resistance stainless steel material, and service life can reach more than 15 years.
7, floor space is few;
accompanying drawing illustrates:
For ease of illustrating, the utility model is described in detail by following concrete enforcement and accompanying drawing.
Fig. 1 is the utility model structural representation;
Fig. 2 is the structural representation of dehydrator in the utility model;
Fig. 3 is the structural representation of water strainer in the utility model;
Fig. 4 is flue gas flow structural representation of the present utility model;
Fig. 5 is spray flow process theory structure schematic diagram of the present utility model;
Fig. 6 is desulfurization and dedusting theory structure schematic diagram of the present utility model.
1-enters mouth; 2-cylindrical shell; 3-spray head; 4-flue gas water conservancy diversion umbrella crown; 5-convergent flow-disturbing mouth; 6-dehydrator; 7-dust stratification funnel; 8-sewage discharging regulation valve; 9-taper water knockout drum; 10-outlet flue; 11-bearing; 12-drain guide pipe; 13-sprays control valve; 14-Sprayer Circulation pipe; 15-laying dust water tank; 15-1-cyclic water tank; 16-sewage water discharge valve; 17-communicating pipe; 18-communicating valve; 19-clear water blowoff valve; 20-water circulating pump; 21-altitude valve; 22-air-introduced machine; 23-flue.
detailed description of the invention:
As Figure 1-3, this detailed description of the invention by the following technical solutions: it comprises into mouth 1, cylindrical shell 2, spray head 3, flue gas water conservancy diversion umbrella crown 4, convergent flow-disturbing mouth 5, dehydrator 6, dust stratification funnel 7, sewage discharging regulation valve 8, taper water knockout drum 9, outlet flue 10, bearing 11, drain guide pipe 12, spray control valve 13, Sprayer Circulation pipe 14, laying dust water tank 15 and cyclic water tank 15-1, sewage water discharge valve 16, communicating pipe 17, communicating valve 18, clear water blowoff valve 19, water circulating pump 20, altitude valve 21, air-introduced machine 22 and flue 23, described spray head 3 is divided into the first spray head 3A, second spray head 3B, 3rd spray head 3C, described flue gas water conservancy diversion umbrella crown 4 is divided into the first flue gas water conservancy diversion umbrella crown 4A and the second flue gas water conservancy diversion umbrella crown 4B, described convergent flow-disturbing mouth 5 is divided into the first convergent flow-disturbing mouth 5A and the second convergent flow-disturbing mouth 5B, the below of cylindrical shell 2 is fixedly installed bearing 11, the top of cylindrical shell 2 is provided with into mouth 1, and the inside of cylindrical shell 2 is disposed with the first spray head 3A from top to bottom, second spray head 3B, 3rd spray head 3C, the below of the second spray head 3B and the 3rd spray head 3C is separately installed with the first flue gas water conservancy diversion umbrella crown 4A and the second flue gas water conservancy diversion umbrella crown 4B, the first convergent flow-disturbing mouth 5A is provided with between second spray head 3B and the 3rd spray head 3C, the below of the 3rd spray head 3C is provided with the second convergent flow-disturbing mouth 5B, the below of the second convergent flow-disturbing mouth 5B is provided with taper water knockout drum 9, the below of taper water knockout drum 9 is provided with dehydrator 6, dehydrator 6 is connected with one end of outlet flue 10, the other end of outlet flue 10 is connected with air-introduced machine 22, the top of air-introduced machine 22 is connected with flue 23, the bottom of cylindrical shell 2 is arranged and dust stratification funnel 7, dust stratification funnel 7 is communicated with laying dust water tank 15 by drain guide pipe 12, drain guide pipe 12 is provided with sewage discharging regulation valve 8, laying dust water tank 15 side is provided with cyclic water tank 15-1, the top of cyclic water tank 15-1 is provided with altitude valve 21, and be connected by communicating pipe 17 between laying dust water tank 15 with cyclic water tank 15-1, be provided with communicating valve 18 communicating pipe 17, the below of laying dust water tank 15 is connected with sewage water discharge valve 16, the below of cyclic water tank 15-1 is connected with clear water blowoff valve 19.
As preferably, described cyclic water tank 15-1 is connected with the first spray head 3A, the second spray head 3B, the 3rd spray head 3C by Sprayer Circulation pipe 14, and the junction of Sprayer Circulation pipe 14 and the first spray head 3A, the second spray head 3B, the 3rd spray head 3C is provided with and sprays control valve 13.
As preferably, 14 of described Sprayer Circulation pipe are provided with water circulating pump 20 with the junction of cyclic water tank 15-1.
As preferably, the inside of described dehydrator 6 is provided with water strainer 6-1 and inner bag 6-2.
The operation principle of this detailed description of the invention is: with reference to Fig. 4, flue gas flow principle is: boiler tail flue gas is under the effect of air-introduced machine suction, enter from the top of water curtain type living beings special dust seperator in mouth 1 access arrangement cylindrical shell 2, vertical impact cigarette water water conservancy diversion umbrella crown 4, impact the flue gas of umbrella crown be hampered after baffling, by umbrella crown radioactive ray direction, by the outside circumferencial direction scattering in center, form air horn, flow downward along barrel; When flue gas flow to the first convergent flow-disturbing mouth 5A, along with the convergent direction of convergent flow-disturbing mouth, to body centre portion baffling, form the high pressure draught converged; When high pressure draught impacts cigarette water water conservancy diversion umbrella crown 4B, form again second time outwards radioactive ray direction baffling.When flue gas flows downward along barrel, when impacting the second convergent flow-disturbing mouth 5B, define again second time to body centre portion baffling, produce the high pressure draught converged, when high pressure draught impacts taper water knockout drum 9, flue gas third time outside radioactive ray direction baffling, flow downward after impacting circumference barrel, under the effect of air-introduced machine gravitation, dehydrator 6 is entered from bottom to top containing wet flue gas, by water strainer 6-1, a large amount of drop separation is deviate from, time inside smoke-shock to the bullet at dehydrator 6 top, due to the suction-operated of the temperature difference and moist flue gas, water capacity in flue gas, at bullet inwall, form condensed water, fall in dust stratification funnel 7 along dehydrator 6 cylinder inboard wall, flue gas after dehydration, from top to bottom, after entering the inner bag 6-2 of dehydrator 6, discharged by smoke outlet flue 23.
With reference to Fig. 5, spray flow process principle is: under the effect of water circulating pump pressure, the scattering waterline drop that spray head 3 sprays, impact on the first cigarette water water conservancy diversion umbrella crown 4A, along with the angle of scattering of umbrella crown, current converge and form horn-like cascade, flow downwards along cylindrical shell 2 inwall, impact the first convergent flow-disturbing mouth 5A, form the annular cascade that the high pressure of inwardly tiltedly below convergence is intensive, when the center of annular cascade and the second spray head 3B supplements intensive waterline drop, when impacting the second cigarette water water conservancy diversion umbrella crown 4B, produce again second time loudspeaker cascade, after washing away inwall, with the waterline drop of the 3rd spray head 3C, impact the second convergent flow-disturbing mouth 5B, form again the intensive annular cascade of high pressure that the inside tiltedly below of second time is converged, when annular cascade and spray impact taper water knockout drum 9, along with water knockout drum angle of taper, scattering from inside to outside, form third time horn-like cascade, after washing away cylindrical shell 2 inwall and dehydrator 6 outer wall, fall in dust stratification funnel along cylinder inboard wall, uninterruptedly flow into laying dust water tank 15 by blow-off pipe 12 and flow into cyclic water tank 15-1, by circulating pump 20 reciprocation cycle, on cyclic water tank 15-1 top, water level controller 21 is housed, supplement the water yield of high temperature evaporation, ensure the normal operation of water circulation.
With reference to Fig. 6, desulfurization and dedusting principle: a, boiler tail flue gas are under the effect of air-introduced machine suction, mouth 1 is entered from the top of water curtain type living beings special dust seperator, in access arrangement cylindrical shell 2, the scattering waterline droplets mixing (air-introduced machine and the chain synchronous averaging of circulating pump) that vertical impact first cigarette water water conservancy diversion umbrella crown 4A and the first spray head 3A sprays, the waterline drop of mixed flue dust and scattering, impact on the first cigarette water water conservancy diversion umbrella crown 4A simultaneously, make flue dust fully be mixed infiltration with the globule evoked, water smoke.The mixture of flue dust, water, under the effect impacted, forms the flue dust of a large amount of water vapo(u)r bubble parcel, makes the SO-in flue gas
---
2's neutralize by akaline liquid.Water-dust mixture, along with the angle of scattering of umbrella crown, forms outside centrifugal force, forms horn-like cascade, flow downward along cylindrical shell 2 inwall after current converge, in flow process, and bubbles burst, and produce SO
2with the neutralization reaction of akaline liquid; Through the flue gas effusion of neutralization, dust is after washing process, and water-dust mixture impacts the first convergent flow-disturbing mouth 5A, along with the convergent direction of convergent flow-disturbing mouth, to body centre part baffling, produces centripetal force.Due to reducing gradually of circulation area, form the high pressure annular cascade of inwardly tiltedly below convergence, the circular scattering drop that the second spray head 3B sprays, supplements the central space of high pressure annular cascade, flue dust is fully tackled, mixes, complete the desulfurization and dedusting of the first link;
B, when high pressure annular cascade and the center of the second spray head 3B supplement intensive waterline drop, when impacting the second cigarette water water conservancy diversion umbrella crown 4B, produce again the outside loudspeaker cascade of second time, after washing away cylindrical shell 2 inwall, the waterline drop of the 3rd spray head 3C simultaneously, impact convergent flow-disturbing mouth 5B, form again the intensive annular cascade of high pressure that the inside tiltedly below of second time is converged, make the SO of flue gas
2and dust is neutralized further and removes, complete the desulfurization and dedusting of the second link;
C, when the waterline droplet impact of intensive annular cascade and the 3rd spray head 3C is to taper water knockout drum 9, along with water knockout drum angle of taper, scattering from inside to outside, form third time horn-like cascade, after washing away cylindrical shell 2 inwall and dehydrator 6 outer wall, form small one and large one two annular cascades, more thoroughly remove the SO in flue gas
2and dust, complete the desulfurization and dedusting of the 3rd link;
D, qualified flue gas after process enters in dehydrator 6 from the bottom to top, air-introduced machine 21 entrance is entered by outlet flue 10, flue 23 is entered through air-introduced machine 21, dirt after washing, aqueous mixtures falls in dust stratification funnel 7, enter in laying dust water tank ~ cyclic water tank 15 by sewage discharging regulation valve 8 and the continual circulation of drain guide pipe 12, by the water of circulating pump 20 for power suction cyclic water tank 15, spray is provided to supply water, form the circulatory system of spray and blowdown, except flue gas heat of vaporization and precipitation dust water capacity except, recirculated water utilization rate is 100%, desulfurization degree is 100%, dust removal efficiency is 100%.
More than show and describe general principle of the present utility model and principal character and advantage of the present utility model.The technical staff of the industry should understand; the utility model is not restricted to the described embodiments; what describe in above-described embodiment and description just illustrates principle of the present utility model; under the prerequisite not departing from the utility model spirit and scope; the utility model also has various changes and modifications, and these changes and improvements all fall within the scope of claimed the utility model.The claimed scope of the utility model is defined by appending claims and equivalent thereof.
Claims (4)
1. a water curtain type living beings special dust seperator, it is characterized in that: it comprises into mouth (1), cylindrical shell (2), spray head (3), flue gas water conservancy diversion umbrella crown (4), convergent flow-disturbing mouth (5), dehydrator (6), dust stratification funnel (7), sewage discharging regulation valve (8), taper water knockout drum (9), outlet flue (10), bearing (11), drain guide pipe (12), spray control valve (13), Sprayer Circulation pipe (14), laying dust water tank (15) and cyclic water tank (15-1), sewage water discharge valve (16), communicating pipe (17), communicating valve (18), clear water blowoff valve (19), water circulating pump (20), altitude valve (21), air-introduced machine (22) and flue (23), described spray head (3) is divided into the first spray head (3A), second spray head (3B), 3rd spray head (3C), described flue gas water conservancy diversion umbrella crown (4) is divided into the first flue gas water conservancy diversion umbrella crown (4A) and the second flue gas water conservancy diversion umbrella crown (4B), described convergent flow-disturbing mouth (5) is divided into the first convergent flow-disturbing mouth (5A) and the first convergent flow-disturbing mouth (5B), the below of cylindrical shell (2) is fixedly installed bearing (11), the top of cylindrical shell (2) is provided with into mouth (1), the inside of cylindrical shell (2) is disposed with the first spray head (3A) from top to bottom, second spray head (3B), 3rd spray head (3C), the below of the second spray head (3B) and the 3rd spray head (3C) is separately installed with the first flue gas water conservancy diversion umbrella crown (4A) and the second flue gas water conservancy diversion umbrella crown (4B), the first convergent flow-disturbing mouth (5A) is provided with between second spray head (3B) and the 3rd spray head (3C), the below of the 3rd spray head (3C) is provided with the second convergent flow-disturbing mouth (5B), the below of the second convergent flow-disturbing mouth (5B) is provided with taper water knockout drum (9), the below of taper water knockout drum (9) is provided with dehydrator (6), dehydrator (6) is connected with one end of outlet flue (10), the other end of outlet flue (10) is connected with air-introduced machine (22), the top of air-introduced machine (22) is connected with flue (23), the bottom of cylindrical shell (2) is arranged and dust stratification funnel (7), dust stratification funnel (7) is communicated with laying dust water tank (15) by drain guide pipe (12), drain guide pipe (12) is provided with sewage discharging regulation valve (8), laying dust water tank (15) side is provided with cyclic water tank (15-1), the top of cyclic water tank (15-1) is provided with altitude valve (21), and by being connected communicating pipe (17) between laying dust water tank (15) with cyclic water tank (15-1), be provided with communicating valve (18) communicating pipe (17), the below of laying dust water tank (15) is connected with sewage water discharge valve (16), the below of cyclic water tank (15-1) is connected with clear water blowoff valve (19).
2. according to a kind of water curtain type living beings special dust seperator according to claim 1, it is characterized in that: described cyclic water tank (15-1) is connected with the first spray head (3A), the second spray head (3B), the 3rd spray head (3C) by Sprayer Circulation pipe (14), Sprayer Circulation pipe (14) is provided with the junction of the first spray head (3A), the second spray head (3B), the 3rd spray head (3C) and sprays control valve (13).
3. according to a kind of water curtain type living beings special dust seperator according to claim 1, it is characterized in that: (14) of described Sprayer Circulation pipe and the junction of cyclic water tank (15-1) are provided with water circulating pump (20).
4. according to a kind of water curtain type living beings special dust seperator according to claim 1, it is characterized in that: the inside of described dehydrator (6) is provided with water strainer (6-1) and inner bag (6-2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520707503.2U CN204911088U (en) | 2015-09-14 | 2015-09-14 | Special dust remover of water -curtain -type living beings |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520707503.2U CN204911088U (en) | 2015-09-14 | 2015-09-14 | Special dust remover of water -curtain -type living beings |
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| Publication Number | Publication Date |
|---|---|
| CN204911088U true CN204911088U (en) | 2015-12-30 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520707503.2U Expired - Fee Related CN204911088U (en) | 2015-09-14 | 2015-09-14 | Special dust remover of water -curtain -type living beings |
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| CN (1) | CN204911088U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105056669A (en) * | 2015-09-14 | 2015-11-18 | 叶宏 | Water curtain type special dust remover for biomass |
| CN106861319A (en) * | 2017-04-21 | 2017-06-20 | 苏州金澄精密铸造有限公司 | A kind of explosion-proof dedusting job shop |
| CN110913972A (en) * | 2017-08-01 | 2020-03-24 | 阿法拉伐股份有限公司 | Scrubber for cleaning gas |
| CN110917863A (en) * | 2019-12-27 | 2020-03-27 | 浙江德创环保科技股份有限公司 | Sintering flue gas is treatment system in coordination |
-
2015
- 2015-09-14 CN CN201520707503.2U patent/CN204911088U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105056669A (en) * | 2015-09-14 | 2015-11-18 | 叶宏 | Water curtain type special dust remover for biomass |
| CN105056669B (en) * | 2015-09-14 | 2017-01-25 | 叶宏 | Water curtain type special dust remover for biomass |
| CN106861319A (en) * | 2017-04-21 | 2017-06-20 | 苏州金澄精密铸造有限公司 | A kind of explosion-proof dedusting job shop |
| CN110913972A (en) * | 2017-08-01 | 2020-03-24 | 阿法拉伐股份有限公司 | Scrubber for cleaning gas |
| US11141691B2 (en) | 2017-08-01 | 2021-10-12 | Alfa Laval Corporate Ab | Scrubber for cleaning of a gas |
| CN110917863A (en) * | 2019-12-27 | 2020-03-27 | 浙江德创环保科技股份有限公司 | Sintering flue gas is treatment system in coordination |
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