CN103143216B - Turbulent-flow type dust-removing desulfurization system - Google Patents
Turbulent-flow type dust-removing desulfurization system Download PDFInfo
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- CN103143216B CN103143216B CN201310073590.6A CN201310073590A CN103143216B CN 103143216 B CN103143216 B CN 103143216B CN 201310073590 A CN201310073590 A CN 201310073590A CN 103143216 B CN103143216 B CN 103143216B
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- soluble
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- 238000006477 desulfuration reaction Methods 0.000 title abstract description 5
- 230000023556 desulfurization Effects 0.000 title abstract 4
- 238000004140 cleaning Methods 0.000 claims abstract description 41
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 38
- 239000010410 layer Substances 0.000 claims description 32
- 238000005507 spraying Methods 0.000 claims description 20
- 238000010410 dusting Methods 0.000 claims description 16
- 239000007921 spray Substances 0.000 claims description 15
- 239000011229 interlayer Substances 0.000 claims description 7
- 230000000977 initiatory effect Effects 0.000 claims description 3
- 239000007789 gas Substances 0.000 abstract description 29
- 239000002912 waste gas Substances 0.000 abstract description 16
- 239000003344 environmental pollutant Substances 0.000 abstract description 7
- 231100000719 pollutant Toxicity 0.000 abstract description 7
- 230000006872 improvement Effects 0.000 description 9
- 239000000779 smoke Substances 0.000 description 8
- 230000000694 effects Effects 0.000 description 7
- 239000003517 fume Substances 0.000 description 3
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 238000004056 waste incineration Methods 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 241000883990 Flabellum Species 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 230000001351 cycling effect Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000003500 flue dust Substances 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000000505 pernicious effect Effects 0.000 description 1
- 230000002085 persistent effect Effects 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Abstract
The invention discloses a turbulent-flow type dust-removing desulfurization system. The turbulent-flow type dust-removing desulfurization system mainly consists of a turbulent-flow tower, an air blower, an annular cleaning device and a water dissolving treatment device, wherein a system head gas inlet is formed in the turbulent-flow tower; a turbulent-flow gas outlet of the turbulent-flow tower is connected with an air inlet of the air blower; an air outlet of the air blower is connected with a cleaning gas inlet of the annular cleaning device; a cleaning gas outlet of the annular cleaning device is connected with the water dissolving gas inlet of the water dissolving treatment device; and a system head gas outlet is formed in the water dissolving treatment device. The turbulent-flow type dust-removing desulfurization system disclosed by the invention can be used for sufficiently maintaining the waste gas inside, so that the pollutants contained in the waste gas are effectively removed.
Description
Technical field
The present invention relates to exhaust-gas treatment field, be specifically related to a kind of turbulence type dusting and desulfuring system.
Background technology
Along with social development, the discharge capacity of the waste gas that industrial waste gas and waste incineration produce is increasing, if industrial enterprise and waste incineration station are not processed just and are directly discharged in atmosphere these waste gas, will make the content of airborne poisonous and harmful substances and fine particle increase, cause air to be subject to polluting, affecting health, the discharge capacity of therefore controlling waste gas has become society to the pollution of environment and has needed one of environmental problem of solution badly.
Applicant has applied for a kind of " water dissolving separating exhaust gas treating apparatus " (patent No. is ZL200720080927.6) on September 3rd, 2008, it is mainly comprised of the fused mechanism of aqueous vapor and water-air separation structure.Wherein the fused structure of aqueous vapor comprises the blower fan with flabellum, and the air inlet of blower fan is connected to air inlet pipe, is also connected with water inlet pipe in blower fan.Aqueous vapor separating mechanism comprises split cavity, and its top is provided with blast pipe, and its bottom is provided with drainpipe, and blast pipe enters split cavity and stretches to the bottom of split cavity, and the apopore of blower fan is connected by pipeline with the inlet port on split cavity top.The sewage of discharging is via the external treatment tank of drainpipe.Because the structure of this emission-control equipment is comparatively simple, the time of staying of waste gas in device is shorter, so the effect that this device absorbs processing to the gaseous state in waste gas and fume is not satisfactory, is further improved.
Summary of the invention
Technical problem to be solved by this invention be to provide a kind of can allow waste gas within it portion fully stop, effectively to remove the turbulence type dusting and desulfuring system of pollutant contained in waste gas.
For addressing the above problem, the present invention is achieved by the following scheme:
A turbulence type dusting and desulfuring system, it is mainly comprised of turbulent tower, blower fan, annular cleaning device and water-soluble treating apparatus;
Above-mentioned turbulent tower comprises the cylindrical shell of airtight hollow and is fixed on spraying ring pipe in cylindrical shell inner chamber and multilayer turbulent flow baffle independently; Spraying ring pipe is positioned at the top of cylindrical shell inner chamber, and multilayer turbulent flow baffle stacks the below that is arranged at spraying ring pipe; Spraying ring pipe is connected with outside oral siphon; Each turbulent flow baffle all comprises a turbosphere and a guide layer, and turbosphere is positioned at the top of guide layer; Turbosphere is formed by the horizontal ordered arrangement of several turbulent pipe, on the tube wall of the above-mentioned turbulent pipe that is positioned at intermediate layer, offers aperture, and these are opened foraminate turbulent pipe and are all communicated with outside oral siphon; Guide layer is formed by the vertical ordered arrangement of several spray straight tubes, on the tube wall of each spray straight tube, all offers aperture, and all spray straight tubes are all communicated with outside oral siphon; The bottom of cylindrical shell offers the total air inlet of system and turbulent flow discharge outlet, and the top of cylindrical shell offers turbulent flow gas outlet;
Above-mentioned annular cleaning device comprises the toroidal shell of airtight hollow and is movably arranged on several rotating wash bowls in toroidal shell inner chamber; The bottom of toroidal shell offers to be cleaned air intake and cleans discharge outlet, and the top of toroidal shell offers cleans gas outlet; Above-mentioned cleaning air intake direction and cleaning gas outlet direction are all tangent with the circumferential direction of toroidal shell;
Above-mentioned water-soluble treating apparatus comprises the cylindrical outer cover of airtight hollow and is arranged on wind-guiding axle and the guide vane in cylindrical outer cover inner chamber; Wherein wind-guiding axle is hollow columnar, and is fixed on the middle and upper part in cylindrical outer cover inner chamber; The lower openings of wind-guiding axle communicates with cylindrical outer cover inner chamber, and the upper opening of wind-guiding axle is in the exterior of cylindrical outer cover and form the total gas outlet of system; Guide vane is spiral to be looped around on the lateral wall of wind-guiding axle; The bottom of cylindrical outer cover offers water-soluble discharge outlet, and the top of cylindrical outer cover offers water-soluble air inlet;
The air intake vent of above-mentioned blower fan is connected with the turbulent flow gas outlet of turbulent tower, and the air outlet of blower fan is connected with the cleaning air intake of annular cleaning device; The annular cleaning gas outlet of cleaning device and the water-soluble air inlet of water-soluble treating apparatus are connected.
As improvement, in turbulent tower, between every 2 layers of turbulent flow baffle, be provided with certain interval.
As improvement, in turbulent tower, between turbosphere and guide layer, be provided with a spilling water baffle ring; Now on the cylindrical shell of the turbulent tower relative with every layer of guide layer, offer at least one Overflow drainage mouth, above-mentioned all Overflow drainage mouths all communicate with outside oral siphon.
As improvement, in turbulent tower, the number that is positioned at the Overflow drainage mouth of lower floor will be more than the number that is positioned at upper strata Overflow drainage mouth.
As improvement, in turbulent tower, spraying ring pipe is directly communicated with outside oral siphon; The spray straight tube of the turbulent pipe of turbosphere and guide layer is communicated with outside oral siphon by water valve.
As improvement, in annular cleaning device, in the inner chamber of toroidal shell, be also provided with an interlayer, this interlayer is the annular slab that is covered with hole.
As improvement, in annular cleaning device, on toroidal shell, be also provided with rotating wash bowl dispensing port.
As improvement, in water-soluble treating apparatus, the axis of its wind-guiding axle overlaps with the axis of its cylindrical outer cover.
As improvement, in water-soluble treating apparatus, the initiating terminal of guide vane is positioned at water-soluble air inlet one side.
As improvement, in turbulent tower, the number of turbulent flow baffle is 2～100, and the number of the turbulent pipe in turbosphere is 10～50, and the number of the mozzle in guide layer is 6～30.
Compared with prior art, the present invention has following features:
1, equipment can be in operation and produce voluntarily water smoke, overcome tradition with nozzle water spray water smoke under wind-force effect, can change into water or the globule and be difficult to waste gas in the fused difficulty of particulate contaminant;
2, rotating wash bowl, at annular cleaning device persistent movement, can not stop up in annular cleaning device inside impurity;
2, product structure is reasonable, and floor space is little;
3, equipment is in operation does not need to clean for a long time;
4, simple to operate, maintenance, repair convenience;
5, cycling use of water, energy consumption is low, operating cost is few.
6, dedusting, desulfuration efficiency are high.
7, be not afraid of high temperature, humidity and oil gas.
Accompanying drawing explanation
Fig. 1 is a kind of schematic perspective view of turbulence type dusting and desulfuring system;
Fig. 2 is the schematic perspective view of turbulent tower in Fig. 1;
Fig. 3 is the cutaway view of turbulent tower in Fig. 1;
Fig. 4 is the schematic perspective view of annular cleaning device in Fig. 1;
Fig. 5 is the schematic perspective view of Fig. 4 internal washing ball;
Fig. 6 is the schematic perspective view of water-soluble treating apparatus in Fig. 1;
Fig. 7 is the cutaway view of water-soluble treating apparatus in Fig. 1.
Number in the figure:
1, turbulent tower; 11, cylindrical shell; 111, the total air inlet of system; 112, turbulent flow discharge outlet; 113, turbulent flow gas outlet; 114, Overflow drainage mouth; 12, spraying ring pipe; 13, turbulent flow baffle; 131, turbosphere; 132, spilling water baffle ring; 133, guide layer;
2, blower fan; 21, air intake vent; 22, air outlet;
3, annular cleaning device; 31, toroidal shell; 311, clean air intake; 312, clean discharge outlet; 313, clean gas outlet; 314, rotating wash bowl dispensing port; 32, interlayer; 33, rotating wash bowl;
4, water-soluble treating apparatus; 41 cylindrical outer covers; 411, the total gas outlet of system; 412 water-soluble discharge outlet; 413, water-soluble air inlet; 42, wind-guiding axle; 43, guide vane.
The specific embodiment
A turbulence type dusting and desulfuring system, as shown in Figure 1, it is mainly comprised of turbulent tower 1, blower fan 2, annular cleaning device 3 and water-soluble treating apparatus 4.
As shown in Figures 2 and 3, above-mentioned turbulent tower 1 comprises the cylindrical shell 11 of airtight hollow and is fixed on spraying ring pipe 12 in cylindrical shell 11 inner chambers and multilayer turbulent flow baffle 13 independently above-mentioned turbulent tower 1.Spraying ring pipe 12 is positioned at the top of cylindrical shell 11 inner chambers, and multilayer turbulent flow baffle 13 stacks the below that is arranged at spraying ring pipe 12.Spraying ring pipe 12 is connected with outside oral siphon.Each turbulent flow baffle 13 all comprises a turbosphere 131 and a guide layer 133, and turbosphere 131 is positioned at the top of guide layer 133.Turbosphere 131 is formed by the horizontal ordered arrangement of several turbulent pipe, on the tube wall of the above-mentioned turbulent pipe that is positioned at intermediate layer, offers aperture, and these are opened foraminate turbulent pipe and are all communicated with outside oral siphon.133 of guide layers are formed by the vertical ordered arrangement of several spray straight tubes, on the tube wall of each spray straight tube, all offer aperture, and all spray straight tubes are all communicated with outside oral siphon.The bottom of cylindrical shell 11 offers the total air inlet 111 of system and turbulent flow discharge outlet 112, and wherein turbulent flow discharge outlet 112 is positioned at the below of the total air inlet 111 of system, and the top of cylindrical shell 11 offers turbulent flow gas outlet 113.In order to allow waste gas carry out conversion direction between the multilayer turbulent flow baffle 13 of turbulent tower 1, and then make the fume in waste gas to carry out combination with water smoke better, between every 2 layers of turbulent flow baffle 13, be provided with certain interval.In the present invention, by spraying ring pipe 12, turbulent pipe and spray straight tube, entering into the water of turbulent tower 1 can be all be discharged by the turbulent flow discharge outlet 112 of turbulent tower 1 bottom, if but consider moisture can produce certain resistance to pending waste gas when being flowed to turbulent tower 1 bottom and make waste gas be difficult to upwards flow, therefore need between turbosphere 131 and guide layer 133, be provided with a spilling water baffle ring 132, and on the lateral wall of every one deck turbulent flow baffle 13, all offer some Overflow drainage mouths 114, and Overflow drainage mouth 114 communicates with outside oral siphon.Overflow drainage mouth 114 can be spilled over to moisture too much in the turbulent tower entering 1 in outside oral siphon, and allows these moisture can offer spraying ring pipe 12, turbulent pipe and mozzle.And in the present embodiment, 114, the Overflow drainage mouth of corresponding every layer of turbulent flow baffle 13 is opened on the cylindrical shell 11 of the turbulent tower 1 that every layer of guide layer 133 is relative.Quantity corresponding to the Overflow drainage mouth 114 of every layer of turbulent flow baffle 13 can be as many, but the water yield of considering turbulent tower 1 below can be greater than the water yield of top, the number that is therefore positioned at the Overflow drainage mouth 114 of lower floor will be more than the number that is positioned at upper strata Overflow drainage mouth 114.In addition, spraying ring pipe 12 is directly communicated with outside oral siphon, and spraying ring pipe 12 can be sprayed all the time in the inner chamber of turbulent tower 1.For the turbulent pipe of turbosphere 131 and the spray straight tube of guide layer 133, can be communicated with outside oral siphon by water valve, like this can be according to concrete user demand to turbulent pipe and the water flowing of spray straight tube, with using water wisely.
As shown in Figure 4, it comprises the toroidal shell 31 of airtight hollow and is movably arranged on several rotating wash bowls 33 in toroidal shell 31 inner chambers above-mentioned annular cleaning device 3.The bottom of toroidal shell 31 offers to be cleaned air intake 311 and cleans discharge outlet 312, and the top of toroidal shell 31 offers cleans gas outlet 313.Above-mentioned cleaning air intake 311 directions and cleaning gas outlet 313 directions are all tangent with the circumferential direction of toroidal shell 31.In order to improve effect, in the inner chamber of described toroidal shell 31, be also provided with an interlayer 32, this interlayer 32 is for being covered with the annular slab in hole.In addition,, in order can rotating wash bowl 33 supply volumes to be increased and to be reduced, simultaneously also in order can regularly rotating wash bowl 33 to be changed from the interior taking-up of toroidal shell 31, on described toroidal shell 31, be also provided with rotating wash bowl 33 dispensing ports 314.Wherein the structure of rotating wash bowl 33 as shown in Figure 5.In annular cleaning device 3, rotating wash bowl 33 can run up around the inner chamber circular passage of toroidal shell 31, the effect that turbulization is cleaned.
As shown in Figures 6 and 7, it comprises the cylindrical outer cover 41 of airtight hollow and is arranged on wind-guiding axle 42 and the guide vane 43 in cylindrical outer cover 41 inner chambers above-mentioned water-soluble treating apparatus 4.Wherein wind-guiding axle 42 is hollow columnar, and is fixed on the middle and upper part in cylindrical outer cover 41 inner chambers.The lower openings of wind-guiding axle 42 communicates with cylindrical outer cover 41 inner chambers, and the upper opening of wind-guiding axle 42 is in the exterior of cylindrical outer cover 41 and form the total gas outlet 411 of system.Guide vane 43 is spiral to be looped around on the lateral wall of wind-guiding axle 42.The bottom of cylindrical outer cover 41 offers water-soluble discharge outlet 412, and the top of cylindrical outer cover 41 offers water-soluble air inlet 413.In order can better to guide wind, the axis of described wind-guiding axle 42 overlaps with the axis of its cylindrical outer cover 41.Meanwhile, the initiating terminal of guide vane 43 is positioned at water-soluble air inlet 413 1 sides.
The air intake vent 21 of above-mentioned blower fan 2 is connected with the turbulent flow gas outlet 113 of turbulent tower 1, and the air outlet 22 of blower fan 2 is connected with the cleaning air intake 311 of annular cleaning device 3.The annular cleaning gas outlet 313 of cleaning device 3 and the water-soluble air inlet 413 of water-soluble treating apparatus 4 are connected.
The present invention arranges a turbulent tower 1 being comprised of multilayer turbulent flow baffle 13, and in running, under the wind-force effect of blower fan 2, turbulent tower 1 can change into water smoke automatically the water spraying into.Utilize the negative pressure of blower fan 2 by the pernicious gas suction turbulent tower 1 that contains flue dust or sulfide, waste gas constantly changes flow direction in tower in company with water smoke, make fume and water smoke multiple impacts in waste gas, fully water suction becomes heavy and follows water adhesion, and most of pollutant is discharged from the pipeline of turbulent tower 1 bottom in water by molten.An annular cleaning device 3 is set again, in device, drop into a certain amount of wear-resisting rotating wash bowl 33, utilize the positive pressure handle of blower fan 2 to absorb water to become the pollutant that escheat is not discharged by water adhesion to send in annular cleaning device 3, and add certain water, under wind-force effect, rotating wash bowl 33 can run up around circular passage, the effect that turbulization is cleaned, and the pollutant of the overwhelming majority can be taken out of annular cleaning device 3 by water in this link.Again the gas that contains a small amount of pollutant is sent in water dissolving type treating apparatus, new shape, revolved under wind action, the pollutant not eliminated and water smoke can be removed in the lump, totally without the gas of steam, from pipeline, discharge qualified discharge.
The present invention applicable to burn away the refuse and smoke abatement that coal-burning boiler produces and burn in the stink that produces due to high temperature process; Also can be widely used in the large processing of intractability such as flue gas that in industrial processes, available water is processed, dust, oil gas, steam, especially the best equipment of removal sulfur dioxide.
Claims (10)
1. turbulence type dusting and desulfuring system, is characterized in that: it is mainly comprised of turbulent tower (1), blower fan (2), annular cleaning device (3) and water-soluble treating apparatus (4);
Above-mentioned turbulent tower (1) comprises the cylindrical shell (11) of airtight hollow and is fixed on spraying ring pipe (12) in cylindrical shell (11) inner chamber and multilayer turbulent flow baffle (13) independently; Spraying ring pipe (12) is positioned at the top of cylindrical shell (11) inner chamber, and multilayer turbulent flow baffle (13) stacks the below that is arranged at spraying ring pipe (12); Spraying ring pipe (12) is connected with outside oral siphon; Each turbulent flow baffle (13) all comprises a turbosphere (131) and a guide layer (133), and turbosphere (131) is positioned at the top of guide layer (133); Turbosphere (131) is formed by the horizontal ordered arrangement of several turbulent pipe, on the tube wall of the above-mentioned turbulent pipe that is positioned at intermediate layer, offers aperture, and these are opened foraminate turbulent pipe and are all communicated with outside oral siphon; Guide layer (133) is formed by the vertical ordered arrangement of several spray straight tubes, on the tube wall of each spray straight tube, all offers aperture, and all spray straight tubes are all communicated with outside oral siphon; The bottom of cylindrical shell (11) offers the total air inlet of system (111) and turbulent flow discharge outlet (112), and the top of cylindrical shell (11) offers turbulent flow gas outlet (113);
Above-mentioned annular cleaning device (3) comprises the toroidal shell (31) of airtight hollow and is movably arranged on several rotating wash bowls (33) in toroidal shell (31) inner chamber; The bottom of toroidal shell (31) offers to be cleaned air intake (311) and cleans discharge outlet (312), and the top of toroidal shell (31) offers cleans gas outlet (313); Above-mentioned cleaning air intake (311) direction and cleaning gas outlet (313) direction are all tangent with the circumferential direction of toroidal shell (31);
Above-mentioned water-soluble treating apparatus (4) comprises the cylindrical outer cover (41) of airtight hollow and is arranged on wind-guiding axle (42) and the guide vane (43) in cylindrical outer cover (41) inner chamber; Wherein wind-guiding axle (42) is hollow columnar, and is fixed on the middle and upper part in cylindrical outer cover (41) inner chamber; The lower openings of wind-guiding axle (42) communicates with cylindrical outer cover (41) inner chamber, and the upper opening of wind-guiding axle (42) is in the exterior of cylindrical outer cover (41) and form the total gas outlet of system (411); Guide vane (43) is spiral to be looped around on the lateral wall of wind-guiding axle (42); The bottom of cylindrical outer cover (41) offers water-soluble discharge outlet (412), and the top of cylindrical outer cover (41) offers water-soluble air inlet (413);
The air intake vent (21) of above-mentioned blower fan (2) is connected with the turbulent flow gas outlet (113) of turbulent tower (1), and the air outlet (22) of blower fan (2) is connected with the cleaning air intake (311) of annular cleaning device (3); The cleaning gas outlet (313) of annular cleaning device (3) is connected with the water-soluble air inlet (413) of water-soluble treating apparatus (4).
2. turbulence type dusting and desulfuring system according to claim 1, is characterized in that: in turbulent tower (1), between every 2 layers of turbulent flow baffle (13), be provided with certain interval.
3. turbulence type dusting and desulfuring system according to claim 1 and 2, is characterized in that: in turbulent tower, be provided with a spilling water baffle ring (132) between turbosphere (131) and guide layer (133); Now on the cylindrical shell (11) of the turbulent tower (1) relative with every layer of guide layer (133), offer at least one Overflow drainage mouth (114); Above-mentioned all Overflow drainage mouths (114) all communicate with outside oral siphon.
4. turbulence type dusting and desulfuring system according to claim 3, is characterized in that: in turbulent tower, the number that is positioned at the Overflow drainage mouth (114) of lower floor will be more than the number that is positioned at upper strata Overflow drainage mouth (114).
5. turbulence type dusting and desulfuring system according to claim 1, is characterized in that: in turbulent tower (1), spraying ring pipe (12) is directly communicated with outside oral siphon; The spray straight tube of the turbulent pipe of turbosphere (131) and guide layer (133) is communicated with outside oral siphon by water valve.
6. turbulence type dusting and desulfuring system according to claim 1, is characterized in that: in annular cleaning device (3), be also provided with an interlayer (32) in the inner chamber of toroidal shell (31), this interlayer (32) is for being covered with the annular slab in hole.
7. turbulence type dusting and desulfuring system according to claim 1, is characterized in that: in annular cleaning device (3), be also provided with rotating wash bowl (33) dispensing port (314) on toroidal shell (31).
8. turbulence type dusting and desulfuring system according to claim 1, is characterized in that: in water-soluble treating apparatus (4), the axis of its wind-guiding axle (42) overlaps with the axis of its cylindrical outer cover (41).
9. turbulence type dusting and desulfuring system according to claim 1, is characterized in that: in water-soluble treating apparatus (4), the initiating terminal of guide vane (43) is positioned at water-soluble air inlet (413) one sides.
10. turbulence type dusting and desulfuring system according to claim 1, it is characterized in that: the number of the interior turbulent flow baffle of turbulent tower (1) (13) is 2～100, the number of the turbulent pipe in turbosphere (131) is 10～50, and the number of the mozzle in guide layer (133) is 6～30.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310073590.6A CN103143216B (en) | 2013-03-08 | 2013-03-08 | Turbulent-flow type dust-removing desulfurization system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310073590.6A CN103143216B (en) | 2013-03-08 | 2013-03-08 | Turbulent-flow type dust-removing desulfurization system |
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| CN103143216A CN103143216A (en) | 2013-06-12 |
| CN103143216B true CN103143216B (en) | 2014-08-27 |
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| CN201310073590.6A Expired - Fee Related CN103143216B (en) | 2013-03-08 | 2013-03-08 | Turbulent-flow type dust-removing desulfurization system |
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| CN109675414A (en) * | 2019-02-27 | 2019-04-26 | 广西贝仕特环保科技有限公司 | A kind of dehumidification structure for air purifier |
| CN117683572B (en) * | 2024-01-31 | 2024-04-05 | 国家能源集团煤焦化有限责任公司 | Coke oven gas water washing spray dust collecting equipment |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1091053A (en) * | 1993-12-29 | 1994-08-24 | 张爱清 | Combined smoke-removing dust-removing desulfurization device |
| CN201108801Y (en) * | 2007-08-31 | 2008-09-03 | 莫显坤 | Water dissolving separating exhaust gas treating apparatus |
| CN201120236Y (en) * | 2007-11-13 | 2008-09-24 | 闫会元 | Hydrosphere mixing, separating multilevel air purification device |
| CN201684540U (en) * | 2010-06-08 | 2010-12-29 | 成都每日环保科技有限责任公司 | Cleaning tower for smoke generated from aerodynamic turbulence |
| CN203139844U (en) * | 2013-03-08 | 2013-08-21 | 桂林市世环废气处理设备有限公司 | Turbulence type dust removal and desulfurization system |
| JP5768121B2 (en) * | 2013-12-24 | 2015-08-26 | 株式会社カプコン | Game machine |
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