CN101502733A - Spraying and dust-removing system - Google Patents
Spraying and dust-removing system Download PDFInfo
- Publication number
- CN101502733A CN101502733A CNA2009100247639A CN200910024763A CN101502733A CN 101502733 A CN101502733 A CN 101502733A CN A2009100247639 A CNA2009100247639 A CN A2009100247639A CN 200910024763 A CN200910024763 A CN 200910024763A CN 101502733 A CN101502733 A CN 101502733A
- Authority
- CN
- China
- Prior art keywords
- dust
- water
- wash tower
- gas wash
- containing water
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Images
Landscapes
- Separation Of Particles Using Liquids (AREA)
Abstract
The invention relates to a spray dedusting system, a dedusting tower is erected on a circulating deposition tank, an opening is opened at the top of the dedusting tower, the dedusting tower is connected with a smoke pipe, the inner wall of the dedusting tower corresponding to the upper part of the exit end of the smoke pipe is provided with a water baffle, the dedusting tower above the water baffle is internally provided with a plurality of spray heads, the bottom end of the dedusting tower corresponding to the lower of the exit end of the smoke pipe is provided with a water sealing device inserted in the circulating deposition tank, the spray heads are connected with the water outlets of a spray pump by pipelines, the water inlets of the spray pump are arranged in the circulating deposition tank, a quality regulating water storage tank is arranged beside the circulating deposition tank, a quality regulating mild base block layer is paved on the bottom of the quality regulating water storage tank, a non-water tight gland layer is paved on the quality regulating mild base block layer, a water supply device used for supplying water to the quality regulating water storage tank from the circulating deposition tank is arranged between the circulating deposition tank and the quality regulating water storage tank, and a water supplementing device for supplementing water to the circulating deposition tank from the quality regulating water storage tank is arranged between the circulating deposition tank and the quality regulating water storage tank.
Description
Technical field
The present invention relates to a kind of spraying and dust-removing system.
Background technology
At present, general enterprise mainly uses dry dust removal equipments such as sack cleaner, cyclone dust collectors and electrostatic precipitator when dedusting.Wherein, sack cleaner is generally used for elementary dedusting, and its dust collection capacity is general, and energy consumption is especially big, and service life is but very short, continues 3~4 months dust settling pockets of dedusting and has just stopped up, and small dust is not easy to eliminate; The cyclone dust collectors cleaning shaft is longer, and small dust also is not easy to eliminate; Though the electrostatic precipitator better dust removal effect costs an arm and a leg, also there is easy blocking problem in its dust arrester.Therefore, be badly in need of better dust removal effect, long service life, low-cost spraying and dust-removing system.
Summary of the invention
The objective of the invention is to overcome the deficiencies in the prior art, a kind of better dust removal effect is provided, can stop up, long service life and low price spraying and dust-removing system.
According to technical scheme provided by the invention, described spraying and dust-removing system, be included in the gas wash tower that sets up on the circulating sedimentation tank, the gas wash tower top end opening, on gas wash tower, be connected with fume pipe, on gas wash tower inwall corresponding above the port of export of fume pipe, the water fender of width greater than the fume pipe port of export is set, described water fender is by downward-sloping to close gas wash tower axis one end away from gas wash tower axis one end, set up some spray heads in the gas wash tower above water fender, gas wash tower bottom below the fume pipe port of export is provided with the water seal arrangement that inserts in the circulating sedimentation tank, spray head joins by the water side of pipeline with the spray water pump, the water inlet end of spray water pump places in the circulating sedimentation tank, at the other hardening and tempering reservoir that is provided with of circulating sedimentation tank, be equipped with modified weak base piece layer at the hardening and tempering reservoir inner bottom surface, on modified weak base piece layer, be equipped with the permeable gland layer that it is compressed, between circulating sedimentation tank and hardening and tempering reservoir, be provided with by the water supply installation of circulating sedimentation tank, between circulating sedimentation tank and hardening and tempering reservoir, be provided with by the water replanishing device of hardening and tempering reservoir to the circulating sedimentation tank moisturizing to hardening and tempering reservoir water supply.
Some demarcation strips have been set up at the circulating sedimentation tank inwall, described demarcation strip is divided into dust-containing water reception tank and at least two dust-containing water sedimentation basins with circulating sedimentation tank, offer the water stream channel that is communicated with dust-containing water reception tank and dust-containing water sedimentation basin or two dust-containing water sedimentation basins in the demarcation strip top ends, the water stream channel of offering on adjacent two demarcation strips is and shifts to install, and is provided with the water pump interface on the dust-containing water sedimentation basin pool wall away from the dust-containing water reception tank.
Offer the drain outlet that is communicated with dust-containing water reception tank and dust-containing water sedimentation basin or two dust-containing water sedimentation basins in the demarcation strip bottom, on dust-containing water sedimentation basin pool wall, also be provided with spout hole, dewatering orifice and mudhole, and described spout hole, dewatering orifice and mudhole position reduce successively away from the dust-containing water reception tank.
Described water seal arrangement is the funnel that converges that the gas wash tower bottom connects, and the described bottom outlet part that converges funnel embeds 30~50cm under the water surface of dust-containing water reception tank.
Described spray head is included in and connects the spiral helicine atomizing piece that the bottom, termination connects, described atomizing piece is also dwindled to its lower end extension gradually by its upper end, form ejiction opening between the upper and lower two-layer atomizing piece of in the vertical direction, in connecting the termination, has water stream channel, described atomizing piece is wound in the water stream channel bottom, it is characterized in that: described water stream channel is the taper cavity that seamlessly transits.
Outer wall is processed with screw thread in described connection termination, has nut on the outer wall of connection bottom, termination, and the outline formation tapering of described atomizing piece is 20~30 ° a cone.
Be fixed with the some support underframe that are provided with at interval at the gas wash tower inwall, on the support underframe, be coated with the corrosion resistant stratum reticulare, on the corrosion resistant stratum reticulare, lay the dedusting carrier ball, gas wash tower internal frame above the dedusting carrier ball is provided with some spray heads, described dedusting carrier ball is included in the passage of offering on the installing plate, all be fixed with some blades in the installing plate upper and lower surface, and the root of blade of same installing plate upper and lower surface is and shifts to install, the axis of passage and blade have the intersection point on blade.
Installing plate and blade are laminar flat board, and installing plate and blade outer contour formation spheroid, and installing plate is along the weft direction setting of described spheroid, and blade is along the warp direction setting of described spheroid.
On the dedusting carrier ball of placing on the support underframe that is positioned at top layer, be coated with spongy filter course, gas wash tower inwall above spongy filter course has set up the air-flow whirligig, described air-flow whirligig comprises inner ring body and the outer ring body that connects together, be fixed with blade between the lateral wall of inner ring body and the madial wall of outer ring body, make adjacent two blades, inner ring body and outer ring body form gas channel, the axis of described gas channel length direction and inner ring body or outer ring body is antarafacial and intersects, and all gas channels are clockwise or counterclockwise arranges, and is provided with dividing plate with its endoporus shutoff at the madial wall of inner ring body.
Gas wash tower above described air-flow whirligig has the changeover portion that the aperture dwindles from bottom to top, connects the pure qi (oxygen) aiutage in the changeover portion upper end, offers pure qi (oxygen) and detect the hole on the pure qi (oxygen) aiutage.
Advantages such as the present invention has better dust removal effect, can not stop up, long service life and low price.
Description of drawings
Fig. 1 is an overall structure schematic diagram of the present invention.
Fig. 2 is A-A cutaway view of Fig. 1.
Fig. 3 is the expanded view of blade among Fig. 2.
Fig. 4 is B-B cutaway view of Fig. 1.
Fig. 5 is the structural representation of circulating sedimentation tank among the present invention.
Fig. 6 is C-C cutaway view of Fig. 5.
Fig. 7 is the structural representation of hardening and tempering reservoir among the present invention.
Fig. 8 is the structural representation of hardening and tempering reservoir among the present invention.
Fig. 9 is the structural representation of spray head among the present invention.
The specific embodiment
The invention will be further described below in conjunction with concrete drawings and Examples.
As shown in the figure: this spraying and dust-removing system, be included in the gas wash tower 1 that sets up on the circulating sedimentation tank 5, gas wash tower 1 top end opening, on gas wash tower 1, be connected with fume pipe 2, on gas wash tower 1 inwall corresponding above the port of export of fume pipe 2, the water fender 3 of width greater than fume pipe 2 ports of export is set, described water fender 3 is by downward-sloping to close gas wash tower 1 axis one end away from gas wash tower 1 axis one end, set up some spray heads 4 in the gas wash tower 1 above water fender 3, gas wash tower 1 bottom below fume pipe 2 ports of export is provided with the water seal arrangement that inserts in the circulating sedimentation tank 5, spray head 4 joins by the water side of pipeline with spray water pump 7, the water inlet end of spray water pump 7 places in the circulating sedimentation tank 5, at the circulating sedimentation tank 5 other hardening and tempering reservoirs 6 that are provided with, be equipped with modified weak base piece layer 61 at hardening and tempering reservoir 6 inner bottom surfaces, on modified weak base piece layer 61, be equipped with the permeable gland layer 62 that it is compressed, between circulating sedimentation tank 5 and hardening and tempering reservoir 6, be provided with the water supply installation that supplies water to hardening and tempering reservoir 6 by circulating sedimentation tank 5, be provided with between circulating sedimentation tank 5 and hardening and tempering reservoir 6 by the water replanishing device of hardening and tempering reservoir 6 to circulating sedimentation tank 5 moisturizings, the Chi Kou of hardening and tempering reservoir 6 is lower than or with concordant at the bottom of circulating sedimentation tank 5 ponds.
The port of export inside of fume pipe 2 is provided with guide pad 14, on gas wash tower 1 inwall corresponding above the port of export of fume pipe 2 water fender 3 of width greater than fume pipe 2 ports of export is set, described water fender 3 is by downward-sloping to close gas wash tower 1 axis one end away from gas wash tower 1 axis one end.
Described fume pipe 2 internal diameters are increased to its outlet side internal diameter gradually by its inlet end, and described guide pad 14 external diameters are increased to the end near gas wash tower 1 wall gradually by the end away from gas wash tower 1 wall.Described fume pipe 2 all is coniform with guide pad 14.Described fume pipe 2 is consistent with the tapering of guide pad 3, and distance equates between guide pad 14 outside wall surface and fume pipe 2 internal faces.
Some demarcation strips 51 have been set up at circulating sedimentation tank 5 inwalls, described demarcation strip 51 is divided into dust-containing water reception tank 52 and at least two dust-containing water sedimentation basins 53 with circulating sedimentation tank 5, offer the water stream channel 54 that is communicated with dust-containing water reception tank 52 and dust-containing water sedimentation basin 53 or two dust-containing water sedimentation basins 53 in demarcation strip 51 top ends, the water stream channel of offering on adjacent two demarcation strips 51 54 is and shifts to install, and is provided with water pump interface 55 on dust-containing water sedimentation basin 53 pool walls away from dust-containing water reception tank 52.
Offer the drain outlet 56 that is communicated with dust-containing water reception tank 52 and dust-containing water sedimentation basin 53 or two dust-containing water sedimentation basins 53 in demarcation strip 51 bottoms, on dust-containing water sedimentation basin 53 pool walls, also be provided with spout hole 57, dewatering orifice 58 and mudhole 59 away from dust-containing water reception tank 52, and described spout hole 57, dewatering orifice 58 reduce successively with mudhole 59 positions, the adjutage that connects on the dewatering orifice 58 stretches in the hardening and tempering reservoir 6, is formed the water supply installation that is supplied water to hardening and tempering reservoir 6 by circulating sedimentation tank 5 by the adjutage that connects on the dewatering orifice 58.Be provided with the backwater water pump outside hardening and tempering reservoir 6, backwater water pump water inlet end stretches in the hardening and tempering reservoir 6, and backwater water pump water outlet end stretches in the circulating sedimentation tank 5, is formed by the water replanishing device of hardening and tempering reservoir 6 to circulating sedimentation tank 5 moisturizings by the backwater water pump.
Described water seal arrangement be gas wash tower 1 bottom connect converge funnel 17, the described bottom outlet part that converges funnel 17 embeds 30~50cm under the water surface of dust-containing water reception tank 52.
Described spray head 4 is included in and connects the spiral helicine atomizing piece 42 that 41 bottoms, termination connect, described atomizing piece 42 is also dwindled to its lower end extension gradually by its upper end, form ejiction opening between the upper and lower two-layer atomizing piece 42 of in the vertical direction, in connecting termination 41, has water stream channel 43, described atomizing piece 42 is wound in water stream channel 43 bottoms, it is characterized in that: described water stream channel 43 is the taper cavity that seamlessly transits.
41 outer walls are processed with screw thread in described connection termination, have nut 44 on the 41 bottom outer walls of connection termination, and the outline formation tapering of described atomizing piece 42 is 20~30 ° a cone.
Be fixed with the some support underframe 15 that are provided with at interval at gas wash tower 1 inwall, on support underframe 15, be coated with corrosion resistant stratum reticulare 12, on corrosion resistant stratum reticulare 12, lay dedusting carrier ball 8, gas wash tower 1 internal frame above dedusting carrier ball 8 is provided with some spray heads 4, described dedusting carrier ball 83 is included in the passage of offering on the installing plate 81 82, all be fixed with some blades 83 in installing plate 81 upper and lower surfaces, and blade 83 roots of same installing plate 81 upper and lower surfaces are and shift to install, and the axis of passage 82 and blade 83 have the intersection point on blade 83.
Installing plate 81 is laminar flat board with blade 83, and installing plate 81 and blade 83 outer contours formation spheroid, and installing plate 81 is along the weft direction setting of described spheroid, and blade 83 is along the warp direction setting of described spheroid.
On the dedusting carrier ball of placing on the support underframe 15 that is positioned at top layer 8, be coated with spongy filter course 9, gas wash tower 1 inwall above spongy filter course 9 has set up air-flow whirligig 10, described air-flow whirligig 10 comprises the inner ring body 101 and outer ring body 102 that connects together, be fixed with blade 103 between the madial wall of the lateral wall of inner ring body 101 and outer ring body 102, make adjacent two blades 103, inner ring body 101 forms gas channel with outer ring body 102, the axis of described gas channel length direction and inner ring body 101 or outer ring body 102 is antarafacial and intersects, and all gas channels are clockwise or counterclockwise arranges, and is provided with dividing plate 104 with its endoporus shutoff at the madial wall of inner ring body 101.
Ash-laden gas enters in the gas wash tower 1 and rising from fume pipe 2, and the spray head 4 in the gas wash tower 1 sprays a large amount of water from top to bottom.Because fume pipe 2 internal diameters are increased to its outlet side internal diameter gradually by its inlet end, guide pad 14 external diameters are increased to the end near gas wash tower 1 wall gradually by the end away from gas wash tower 1 wall, so, the ash-laden gas that sprays from fume pipe 2 outlet sides is directed to and is divergent shape after piece 7 leads, by behind the water fender 3 lower surfaces retaining, produce static pressure again, the ash-laden gas air-flow will evenly slowly rise from lower to upper, can not produce bounce-back, avoid the port of export of fume pipe 2 to produce backwater phenomenon.And after the basipetal big flow spray droplet of ejection is kept off by water fender 3 upper surfaces in the spray head 4, also avoided the backwater phenomenon of the port of export of fume pipe 2.
And dedusting carrier ball 8 places the corrosion resistant stratum reticulare 12 on the support underframe 15 that laterally sets up in the gas wash tower 1, feeds ash-laden gas in the gas wash tower 1 of support underframe 15 belows, in the gas wash tower 1 of support underframe 15 tops the spray head 4 of lasting water spray downwards is set.Ash-laden gas rises by the passage 82 of dedusting carrier ball 8, dust contacts with the sidewall of blade 83 humidities, dust in the ash-laden gas promptly sticks on the sidewall of blade 83, and the moist dust that the downward water that continues spray head 4 ejections of water spray will stick to blade 83 sidewalls sweeps away, by 82 times rows of passage, realize self-cleaning function, make dedusting carrier ball 8 can not stop up.
Because the countless passages of offering on the installing plate 81 of dedusting carrier ball 8 82, can avoid the disturbance in the ash-laden gas uphill process, make and to beat more on the sidewall of blade 83, be adsorbed on the sidewall of blade 83 humidities through the dust in the ash-laden gas of passage 82.
The moistening dust that is not removed rises to air-flow whirligig 10, the flue gas that contains moistening dust enters from the inlet end of gas channel, because the axis of gas channel length direction and inner ring body 102 or outer ring body 103 is antarafacial and intersects, be provided with dividing plate 105 at the madial wall of inner ring body 102 with its endoporus shutoff, make sectional area reduce, the ash-laden gas wind speed increases, ash-laden gas produces centrifugal force through behind the gas channel, moistening dust is got rid of to gas wash tower 1 inwall, assemble the back and flow to the pond from top to bottom along gas wash tower 1 inwall, clean gas is arranged on the outlet side by gas channel.
During use, the connection termination 41 of spray head 4 is fixed on the end of shower, water stream channel 43 is the taper cavity that seamlessly transits, owing to there has not been the attachment point of plaster in the water stream channel 43, so water stream channel 43 can not accumulate plaster, thereby avoided the generation of water stream channel 43 blockage, atomize and will be punched in atomizing piece 42 from the water stream channel 43 interior water that spray, atomizing effect is better, atomized water is opened along being the directional divergence that is similar to 60 ° with water stream channel 43, it is pipe external spiral of the present invention that the present invention's realization has the pipe inside spin of technology, makes spout stop up never.
During use, on the pool wall of dirt water reception tank 52, gas wash tower is installed, 1 sprays a large amount of water from top to bottom in the gas wash tower, this shower water enters dust adhesion in the ash-laden gas and flushing in the dust-containing water reception tank 52, when the dust-containing water in the dust-containing water reception tank 52 gathers certain depth, dust-containing water enters in the dust-containing water sedimentation basin 53 by the water stream channel of offering on the dividing plate 51 between dust-containing water reception tank 52 and the dust-containing water sedimentation basin 53 54, when the dust-containing water in the dust-containing water sedimentation basin 53 gathered certain depth, dust-containing water entered in the next dust-containing water sedimentation basin 53 by the water stream channel of offering on the dividing plate 51 between the two dust-containing water sedimentation basins 53 54.Because being, the water stream channel of offering on adjacent two demarcation strips 51 54 shifts to install, each water stream channel 54 exit end face is to demarcation strip 51, do not allow water stream channel 51 be aligned with each other, make the water route of dust-containing water increase, water velocity reduces, when reducing the current disturbance settled dust is stirred once again, quicken the precipitation of the dust in the dust-containing water, make that the dust sedimentation effect in the dust-containing water is good.
On dust-containing water sedimentation basin 53 pool walls, be provided with water pump interface 55, make shower water to reuse like this away from dust-containing water reception tank 52, the conserve water resource, but in use, water pump interface 55 needs to install screen pack.
As everyone knows, the general industrial flue dust all is weakly acidic, so after shower water carries out the dedusting of industrial fumes in gas wash tower 1, recirculated water in circulating sedimentation tank 5 all is weakly acidic, weakly acidic recirculated water is fed in the hardening and tempering reservoir 6 of the present invention, see through permeable gland layer 62 back and modified weak base piece layer 61 reaction, reacted water is alkalescent water, this alkalescent water continued to extract out and backwater to circulating sedimentation tank 5, saved water resource, avoided secondary pollution, the alkalescent water after modified is to having better cleaning performance attached to the faintly acid dust on the Wet-way dust-collector.
Claims (10)
1, a kind of spraying and dust-removing system, be included in the gas wash tower (1) that sets up on the circulating sedimentation tank (5), gas wash tower (1) top end opening, on gas wash tower (1), be connected with fume pipe (2), on corresponding gas wash tower (1) inwall in the port of export top of fume pipe (2), the water fender (3) of width greater than fume pipe (2) port of export is set, described water fender (3) is by downward-sloping to close gas wash tower (1) axis one end away from gas wash tower (1) axis one end, in the gas wash tower (1) of water fender (3) top, set up some spray heads (4), gas wash tower (1) bottom in fume pipe (2) port of export below is provided with the water seal arrangement that inserts in the circulating sedimentation tank (5), spray head (4) joins by the water side of pipeline with spray water pump (7), the water inlet end of spray water pump (7) places in the circulating sedimentation tank (5), it is characterized in that: at the other hardening and tempering reservoir (6) that is provided with of circulating sedimentation tank (5), be equipped with modified weak base piece layer (61) at hardening and tempering reservoir (6) inner bottom surface, on modified weak base piece layer (61), be equipped with the permeable gland layer (62) that it is compressed, between circulating sedimentation tank (5) and hardening and tempering reservoir (6), be provided with by the water supply installation of circulating sedimentation tank (5), between circulating sedimentation tank (5) and hardening and tempering reservoir (6), be provided with by the water replanishing device of hardening and tempering reservoir (6) to circulating sedimentation tank (5) moisturizing to hardening and tempering reservoir (6) water supply.
2, spraying and dust-removing system as claimed in claim 1, it is characterized in that: set up some demarcation strips (51) at circulating sedimentation tank (5) inwall, described demarcation strip (51) is divided into dust-containing water reception tank (52) and at least two dust-containing water sedimentation basins (53) with circulating sedimentation tank (5), offer the water stream channel (54) that is communicated with dust-containing water reception tank (52) and dust-containing water sedimentation basin (53) or two dust-containing water sedimentation basins (53) in demarcation strip (51) top ends, the water stream channel of offering on adjacent two demarcation strips (51) (54) is and shifts to install, and is provided with water pump interface (55) on dust-containing water sedimentation basin (53) pool wall away from dust-containing water reception tank (52).
3, spraying and dust-removing system as claimed in claim 2, it is characterized in that: offer the drain outlet (56) that is communicated with dust-containing water reception tank (52) and dust-containing water sedimentation basin (53) or two dust-containing water sedimentation basins (53) in demarcation strip (51) bottom, on dust-containing water sedimentation basin (53) pool wall, also be provided with spout hole (57), dewatering orifice (58) and mudhole (59), and described spout hole (57), dewatering orifice (58) and mudhole (59) position reduce successively away from dust-containing water reception tank (52).
4, spraying and dust-removing system as claimed in claim 1, it is characterized in that: described water seal arrangement be gas wash tower (1) bottom connect converge funnel (17), the described bottom outlet part that converges funnel (17) embeds 30~50cm under the water surface of dust-containing water reception tank (52).
5, spraying and dust-removing system as claimed in claim 1, it is characterized in that: described spray head (4) is included in and connects the spiral helicine atomizing piece (42) that bottom, termination (41) connects, described atomizing piece (42) is also dwindled to its lower end extension gradually by its upper end, form ejiction opening between the upper and lower two-layer atomizing piece (42) of in the vertical direction, in connecting termination (41), has water stream channel (43), described atomizing piece (42) is wound in water stream channel (43) bottom, it is characterized in that: described water stream channel (43) is the taper cavity that seamlessly transits.
6, spraying and dust-removing system as claimed in claim 5, it is characterized in that: outer wall is processed with screw thread in described connection termination (41), have nut (44) on the outer wall of connection bottom, termination (41), the outline formation tapering of described atomizing piece (42) is 20~30 ° a cone.
7, spraying and dust-removing system as claimed in claim 1, it is characterized in that: be fixed with the some support underframe (15) that are provided with at interval at gas wash tower (1) inwall, on support underframe (15), be coated with corrosion resistant stratum reticulare (12), go up laying dedusting carrier ball (8) at corrosion resistant stratum reticulare (12), gas wash tower (1) internal frame in dedusting carrier ball (8) top is provided with some spray heads (4), described dedusting carrier ball (83) is included in the passage of offering on the installing plate (81) (82), all be fixed with some blades (83) in installing plate (81) upper and lower surface, and blade (83) root of same installing plate (81) upper and lower surface is and shifts to install, and the axis of passage (82) and blade (83) have the intersection point on blade (83).
8, spraying and dust-removing system as claimed in claim 7, it is characterized in that: installing plate (81) is laminar flat board with blade (83), and installing plate (81) forms spheroid with blade (83) outer contour, installing plate (81) is along the weft direction setting of described spheroid, and blade (83) is along the warp direction setting of described spheroid.
9, spraying and dust-removing system as claimed in claim 7, it is characterized in that: go up on the dedusting carrier ball of placing (8) at the support underframe (15) that is positioned at top layer and be coated with spongy filter course (9), gas wash tower (1) inwall in spongy filter course (9) top has set up air-flow whirligig (10), described air-flow whirligig (10) comprises the inner ring body (101) and outer ring body (102) that connects together, be fixed with blade (103) between the madial wall of the lateral wall of inner ring body (101) and outer ring body (102), make adjacent two blades (103), inner ring body (101) forms gas channel with outer ring body (102), the axis of described gas channel length direction and inner ring body (101) or outer ring body (102) is antarafacial and intersects, and all gas channels are clockwise or counterclockwise arranges, and is provided with dividing plate (104) with its endoporus shutoff at the madial wall of inner ring body (101).
10, spraying and dust-removing system as claimed in claim 9, it is characterized in that: the gas wash tower (1) in described air-flow whirligig (10) top has the changeover portion (11) that the aperture dwindles from bottom to top, connect pure qi (oxygen) aiutage (16) in changeover portion (11) upper end, on pure qi (oxygen) aiutage (16), offer pure qi (oxygen) and detect hole (13).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNA2009100247639A CN101502733A (en) | 2009-02-13 | 2009-02-13 | Spraying and dust-removing system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNA2009100247639A CN101502733A (en) | 2009-02-13 | 2009-02-13 | Spraying and dust-removing system |
Publications (1)
Publication Number | Publication Date |
---|---|
CN101502733A true CN101502733A (en) | 2009-08-12 |
Family
ID=40975188
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CNA2009100247639A Pending CN101502733A (en) | 2009-02-13 | 2009-02-13 | Spraying and dust-removing system |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN101502733A (en) |
Cited By (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102397735A (en) * | 2011-12-02 | 2012-04-04 | 苏州硒谷科技有限公司 | Selenium fertilizer producing and dedusting device |
CN102441307A (en) * | 2011-11-09 | 2012-05-09 | 铜陵康达铝合金制品有限责任公司 | Smelting furnace exhaust gas filtering system |
CN102755797A (en) * | 2012-08-07 | 2012-10-31 | 四川德胜集团钢铁有限公司 | Wet dust collector |
CN102755798A (en) * | 2012-08-07 | 2012-10-31 | 四川德胜集团钢铁有限公司 | Overflow mechanism and wet dust collector and wet dust collection system |
CN102961938A (en) * | 2012-08-14 | 2013-03-13 | 江苏三环实业股份有限公司 | Wet-type paste mixing deduster |
CN104353318A (en) * | 2014-11-17 | 2015-02-18 | 浙江九川竹木有限公司 | Dust purification device and method |
CN104524901A (en) * | 2014-12-11 | 2015-04-22 | 中国瑞林工程技术有限公司 | Auto-induction atomizing dust collector for crushing station |
CN105056664A (en) * | 2015-08-08 | 2015-11-18 | 广西农垦糖业集团防城精制糖有限公司 | Waste brine reuse system |
CN105056678A (en) * | 2015-08-11 | 2015-11-18 | 孙立刚 | Flue gas cleaner with integration of desulfurization, denitrification, mercury removal and dust removal |
CN105148703A (en) * | 2015-09-30 | 2015-12-16 | 宜兴合一环保科技有限公司 | Device for harmless treatment of pollutants discharged from various hydrolytic treatment device |
CN105688548A (en) * | 2016-01-29 | 2016-06-22 | 河南农业大学 | Purifier for smoke of biomass stove |
CN106180113A (en) * | 2016-07-04 | 2016-12-07 | 李丹 | Ventilated chamber smoke absorption cleaning system |
CN106474850A (en) * | 2015-11-23 | 2017-03-08 | 湖南衡阳新澧化工有限公司 | A kind of wet scrubber |
CN106563326A (en) * | 2016-11-07 | 2017-04-19 | 班明华 | Water curtain dust remover |
CN106731399A (en) * | 2016-12-30 | 2017-05-31 | 天津大学 | A kind of multistage combined high efficient heat exchanging dust arrester and its application method |
CN107376601A (en) * | 2017-09-11 | 2017-11-24 | 天津市鑫天元机械设备有限公司 | A kind of novel spray type gas absorbs body of heater |
CN108579278A (en) * | 2018-07-10 | 2018-09-28 | 陈美青 | Wet-type spray deduster |
CN110102127A (en) * | 2019-05-07 | 2019-08-09 | 武汉世纪友源能源设备有限公司 | A kind of quenching tower flue gas takes off white dust pelletizing system |
CN110152886A (en) * | 2019-06-26 | 2019-08-23 | 广西贵港市雄达环保科技有限公司 | Wet type high-pressure electrostatic automatic dust removal equipment |
CN111604112A (en) * | 2020-05-19 | 2020-09-01 | 北京康禾建筑工程有限公司 | Gravel and sand grinding and screening device that building engineering used |
-
2009
- 2009-02-13 CN CNA2009100247639A patent/CN101502733A/en active Pending
Cited By (24)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102441307A (en) * | 2011-11-09 | 2012-05-09 | 铜陵康达铝合金制品有限责任公司 | Smelting furnace exhaust gas filtering system |
CN102397735A (en) * | 2011-12-02 | 2012-04-04 | 苏州硒谷科技有限公司 | Selenium fertilizer producing and dedusting device |
CN102755797B (en) * | 2012-08-07 | 2015-01-21 | 四川德胜集团钒钛有限公司 | Wet dust collector |
CN102755798A (en) * | 2012-08-07 | 2012-10-31 | 四川德胜集团钢铁有限公司 | Overflow mechanism and wet dust collector and wet dust collection system |
CN102755798B (en) * | 2012-08-07 | 2015-01-21 | 四川德胜集团钒钛有限公司 | Overflow mechanism and wet dust collector and wet dust collection system |
CN102755797A (en) * | 2012-08-07 | 2012-10-31 | 四川德胜集团钢铁有限公司 | Wet dust collector |
CN102961938A (en) * | 2012-08-14 | 2013-03-13 | 江苏三环实业股份有限公司 | Wet-type paste mixing deduster |
CN104353318A (en) * | 2014-11-17 | 2015-02-18 | 浙江九川竹木有限公司 | Dust purification device and method |
CN104524901A (en) * | 2014-12-11 | 2015-04-22 | 中国瑞林工程技术有限公司 | Auto-induction atomizing dust collector for crushing station |
CN105056664A (en) * | 2015-08-08 | 2015-11-18 | 广西农垦糖业集团防城精制糖有限公司 | Waste brine reuse system |
CN105056664B (en) * | 2015-08-08 | 2017-03-08 | 广西农垦糖业集团防城精制糖有限公司 | Useless bittern reutilization system |
CN105056678A (en) * | 2015-08-11 | 2015-11-18 | 孙立刚 | Flue gas cleaner with integration of desulfurization, denitrification, mercury removal and dust removal |
CN105148703A (en) * | 2015-09-30 | 2015-12-16 | 宜兴合一环保科技有限公司 | Device for harmless treatment of pollutants discharged from various hydrolytic treatment device |
CN106474850A (en) * | 2015-11-23 | 2017-03-08 | 湖南衡阳新澧化工有限公司 | A kind of wet scrubber |
CN105688548A (en) * | 2016-01-29 | 2016-06-22 | 河南农业大学 | Purifier for smoke of biomass stove |
CN106180113A (en) * | 2016-07-04 | 2016-12-07 | 李丹 | Ventilated chamber smoke absorption cleaning system |
CN106180113B (en) * | 2016-07-04 | 2018-03-23 | 李丹 | Vent cabinet smoke absorption cleaning system |
CN106563326A (en) * | 2016-11-07 | 2017-04-19 | 班明华 | Water curtain dust remover |
CN106731399A (en) * | 2016-12-30 | 2017-05-31 | 天津大学 | A kind of multistage combined high efficient heat exchanging dust arrester and its application method |
CN107376601A (en) * | 2017-09-11 | 2017-11-24 | 天津市鑫天元机械设备有限公司 | A kind of novel spray type gas absorbs body of heater |
CN108579278A (en) * | 2018-07-10 | 2018-09-28 | 陈美青 | Wet-type spray deduster |
CN110102127A (en) * | 2019-05-07 | 2019-08-09 | 武汉世纪友源能源设备有限公司 | A kind of quenching tower flue gas takes off white dust pelletizing system |
CN110152886A (en) * | 2019-06-26 | 2019-08-23 | 广西贵港市雄达环保科技有限公司 | Wet type high-pressure electrostatic automatic dust removal equipment |
CN111604112A (en) * | 2020-05-19 | 2020-09-01 | 北京康禾建筑工程有限公司 | Gravel and sand grinding and screening device that building engineering used |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101502733A (en) | Spraying and dust-removing system | |
CN104645768B (en) | A kind of Wet type cyclone dust arrester | |
CN105950226B (en) | Coal gas vertical spray cooling and dewatering integral system | |
CN101486505A (en) | Non-secondary pollution water circulating system for spraying dust removing | |
CN101537290A (en) | Spraying duster set with protecting device | |
CN201711068U (en) | Dual-tower water dust collector | |
CN103056045B (en) | For the primary cyclone of gas purification, gas cleaning system, gas purifying method and application thereof | |
CN201551961U (en) | Ammonia flue gas desulfurization tower | |
CN103060018A (en) | Gas distributor for coal gas high-efficiency washing and cleaning technique, secondary coal gas washing tower, coal gas cleaning device and application thereof | |
CN202322761U (en) | Gas distributor, secondary coal gas scrubber and coal gas purifying device for efficient washing and purifying process of coal gas | |
CN101537288A (en) | Three-stage combined dust removal chamber structure of spraying dust removal tower | |
CN101502734A (en) | Spray tower structure for spraying and dedusting | |
CN206700988U (en) | A kind of New type wet cleaner | |
CN103060017B (en) | Combined spiral tower tray for gas washing tower, gas cleaning device and application thereof | |
CN205676432U (en) | Coal gas Horizental showering cooling and dewatering integral system | |
CN202569874U (en) | Water mist dust removal device | |
CN202343047U (en) | Glass fiber reinforced plastic foam dust collector | |
CN103566691A (en) | Secondary water-bath dust collector | |
CN105861076B (en) | Coal gas Horizental showering cooling and dewatering integral system | |
CN202315599U (en) | Water bath dust removing system | |
CN205236185U (en) | Supplementary water of wet -type electrostatic precipitator sprays and washs integrated device | |
CN2345851Y (en) | Wet-type high-efficiency desulfurizing dust-removing device | |
CN201216920Y (en) | Desulfurating dust removing device for flue gas | |
CN210993349U (en) | Honeycomb tube bundle set rotational flow water washing tower | |
CN101549236A (en) | Three-stage dust chamber structure of spray-type dust collection tower |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20090812 |