CN105457796A - Smoke deacidification atomizer - Google Patents
Smoke deacidification atomizer Download PDFInfo
- Publication number
- CN105457796A CN105457796A CN201610012217.3A CN201610012217A CN105457796A CN 105457796 A CN105457796 A CN 105457796A CN 201610012217 A CN201610012217 A CN 201610012217A CN 105457796 A CN105457796 A CN 105457796A
- Authority
- CN
- China
- Prior art keywords
- atomization
- cylindrical shell
- nozzle cover
- nozzle
- flue gas
- 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
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B13/00—Machines or plants for applying liquids or other fluent materials to surfaces of objects or other work by spraying, not covered by groups B05B1/00 - B05B11/00
- B05B13/02—Means for supporting work; Arrangement or mounting of spray heads; Adaptation or arrangement of means for feeding work
- B05B13/0278—Arrangement or mounting of spray heads
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/38—Removing components of undefined structure
- B01D53/40—Acidic components
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/48—Sulfur compounds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/77—Liquid phase processes
- B01D53/78—Liquid phase processes with gas-liquid contact
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B1/00—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means
- B05B1/26—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means with means for mechanically breaking-up or deflecting the jet after discharge, e.g. with fixed deflectors; Breaking-up the discharged liquid or other fluent material by impinging jets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B15/00—Details of spraying plant or spraying apparatus not otherwise provided for; Accessories
- B05B15/50—Arrangements for cleaning; Arrangements for preventing deposits, drying-out or blockage; Arrangements for detecting improper discharge caused by the presence of foreign matter
- B05B15/52—Arrangements for cleaning; Arrangements for preventing deposits, drying-out or blockage; Arrangements for detecting improper discharge caused by the presence of foreign matter for removal of clogging particles
- B05B15/525—Arrangements for cleaning; Arrangements for preventing deposits, drying-out or blockage; Arrangements for detecting improper discharge caused by the presence of foreign matter for removal of clogging particles by increasing the cross section of the discharge openings
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B7/00—Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas
- B05B7/02—Spray pistols; Apparatus for discharge
- B05B7/04—Spray pistols; Apparatus for discharge with arrangements for mixing liquids or other fluent materials before discharge
- B05B7/0416—Spray pistols; Apparatus for discharge with arrangements for mixing liquids or other fluent materials before discharge with arrangements for mixing one gas and one liquid
- B05B7/0441—Spray pistols; Apparatus for discharge with arrangements for mixing liquids or other fluent materials before discharge with arrangements for mixing one gas and one liquid with one inner conduit of liquid surrounded by an external conduit of gas upstream the mixing chamber
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B7/00—Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas
- B05B7/02—Spray pistols; Apparatus for discharge
- B05B7/12—Spray pistols; Apparatus for discharge designed to control volume of flow, e.g. with adjustable passages
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0283—Flue gases
- B01D2258/0291—Flue gases from waste incineration plants
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Nozzles (AREA)
Abstract
A smoke deacidification atomizer comprises a twin-flow pipe body, a converging device and an atomization cylinder. The twin-flow pipe body is provided with a gas channel used for delivering compressed air and a liquid channel used for delivering calcium hydroxide slurry. The twin-flow pipe body and a mixing chamber above the atomization cylinder are communicated through the converging device. The smoke deacidification atomizer is characterized in that the smoke deacidification atomizer further comprises a nozzle cover which is arranged below the atomization cylinder; a horn-shaped flared opening is formed in the inner side wall of the bottom of the atomization cylinder; a gap is formed between the top of the nozzle cover and the bottom of the atomization cylinder and used for forming a nozzle together with the horn-shaped flared opening; the nozzle is communicated with the mixing chamber. The nozzle of the smoke deacidification atomizer is simple in structure and not prone to being blocked.
Description
Technical field
The present invention relates to technical field of waste incineration, be specifically related to a kind ofly be applicable to deacidify to flue gas in reaction tower or the atomizer of desulfurization.
Background technology
At present, the atomizer that the process of industrial flue gas deacidification desulfurizing and purifying uses, ubiquity nozzle holds susceptible to plugging problem, and normally affect very greatly on what produce, especially during employing calcium hydroxide neutralization reaction, problem is particularly outstanding.
Summary of the invention
The technical problem to be solved in the present invention is: provide a kind of nozzle arrangements simply and not susceptible to plugging flue gas deacidification atomizer.
Technical solution of the present invention is: a kind of flue gas deacidification atomizer, comprise double-current body, converging device and atomization cylindrical shell, described double-current body is provided with for carrying compressed-air actuated gas passage and for carrying the fluid passage of calcium hydroxide slurry, described converging device is communicated with the mixing chamber on double-current body and atomization cylindrical shell top, it is characterized in that: also comprise the nozzle cover be arranged on below atomization cylindrical shell, the madial wall of described atomization cylinder body bottom arranges trumpet flare, an intersegmental gap is provided with for cooperatively forming nozzle with trumpet flare between the top of described nozzle cover and the bottom of atomization cylindrical shell, described nozzle is communicated with mixing chamber.
After adopting said structure, the present invention has the following advantages:
Flue gas deacidification atomizer of the present invention forms nozzle between the bottom and the top of nozzle cover of atomization cylindrical shell, structure is simple, design cost is low, the madial wall of atomization cylinder body bottom is set to trumpet flare, the particle in mixing chamber aerosolized mixture out can be made not easily to retain at nozzle place, can effectively avoid particle to block the phenomenon of atomizer nozzle.
As preferably, the gap between the top of described nozzle cover and the bottom of atomization cylindrical shell is first annular gap of 360 °.This setting can make 360 °, the nozzle injection of atomizer, and jeting effect is good.
As preferably, also comprise spiro column, the upper end of described spiro column is positioned at atomization cylindrical shell and is connected with the madial wall of atomization cylindrical shell, it is external and be connected for nozzle cover being fixed on the below being atomized cylindrical shell with nozzle cover that lower end is exposed at atomizing cup, and described spiro column is provided with the drainage channel for being communicated with the mixing chamber on atomization cylindrical shell top.Adopt spiro column nozzle cover to be fixed on the below of atomization cylindrical shell, structure is simple, design cost is low.
As preferably, the upper end of described spiro column is stub end, lower end is cylinder, described drainage channel comprises at least one first through hole be arranged on stub end, and second annular gap of 360 ° be arranged between the lateral wall of cylinder and the madial wall of atomization cylindrical shell, described first through hole communicates with the second annular gap.This setting makes that the structure of drainage channel is simple, design cost is low.
As preferably, one end that described cylinder is exposed at atomizing cup external is provided with external thread section, the top being positioned at external thread section of described cylinder is provided with the spacing preiection be connected with external thread section, described nozzle cover is centrally axially arranged with axis hole, described cylinder is provided with the axis hole of one end through nozzle cover of external thread section, also be provided with between described spacing preiection and nozzle cover and regulate pad for regulating the openings of sizes of nozzle, nozzle cover and adjustment pad are pressed on spacing preiection in the below of nozzle cover by a nut.This setting had both made nozzle cover become dismountable structure, again by changing the size regulating the thickness of pad to change the first annular gap between the top of nozzle cover and the bottom of atomization cylindrical shell, coordinate the design of trumpet flare again, the adjustment of the spray angle to nozzle, height and flow can be reached.
As preferably, described double-current body comprises fluid connection, gas connection and the coaxial inner and outer tubes arranged, and described fluid connection communicates with interior pipe formation fluid passage, and the space between gas connection with inner and outer tubes communicates formation gas passage.
As preferably, described converging device comprises pedestal, described inner and outer tubes are all connected with pedestal, and described pedestal and the junction of interior pipe arrange the second through hole for communicating with fluid passage, described pedestal are at least arranged between inner and outer tubes a third through-hole for communicating with gas passage.This converging device structure is simple, design cost is low.
As preferably, cylindrical shell is mutually vertical arranges for described double-current body and atomization.This setting can make that entire length reduces, structure is compacter.
As preferably, the junction of described interior pipe and converging device is by arc section transition, and arc section transition is also passed through in the junction of described outer tube and converging device.This setting can make fluid pass through smoothly, reduces friction, thus reduces the damage to device.
As preferably, described double-current body, converging device, atomization cylindrical shell, spiro column and nozzle cover all adopt stainless steel acid-resistant steel material to make.Select resistant material, the acidproof corrosion resistance of device can be improved.
Accompanying drawing illustrates:
Fig. 1 is the structural representation of flue gas of the present invention deacidification atomizer;
Fig. 2 is the structural representation of converging device of the present invention, atomization cylindrical shell, nozzle cover;
In figure: 1-double fluid body, 2-converging device, 3-is atomized cylindrical shell, 4-mixing chamber, 5-nozzle cover, 6-first annular gap, 7-trumpet flare, 8-stub end, 9-cylinder, 10-first through hole, 11-second annular gap, 12-external thread section, 13-spacing preiection, 14-regulates pad, 15-nut, 16-fluid connection, 17-gas connection, pipe in 18-, 19-outer tube, 20-pedestal, 21-second through hole, 22-third through-hole, 23-spiro column.
Detailed description of the invention
Below in conjunction with accompanying drawing, and the present invention is described further in conjunction with the embodiments.
Embodiment:
As Fig. 1, shown in Fig. 2, a kind of flue gas deacidification atomizer, comprise double-current body 1, converging device 2 and atomization cylindrical shell 3, described double-current body 1 is provided with for carrying compressed-air actuated gas passage and for carrying the fluid passage of calcium hydroxide slurry, described converging device 2 is communicated with the mixing chamber 4 on double-current body 1 and atomization cylindrical shell 3 top, also comprise the nozzle cover 5 be arranged on below atomization cylindrical shell 3, madial wall bottom described atomization cylindrical shell 3 arranges trumpet flare 7, an intersegmental gap is provided with for cooperatively forming nozzle with trumpet flare 7 between the top of described nozzle cover 5 and the bottom of atomization cylindrical shell 3, described nozzle is communicated with mixing chamber 4.
Flue gas deacidification atomizer of the present invention forms nozzle between the bottom and the top of nozzle cover 5 of atomization cylindrical shell 3, structure is simple, design cost is low, madial wall bottom atomization cylindrical shell 3 is set to trumpet flare 7, the particle in mixing chamber 4 aerosolized mixture out can be made not easily to retain at nozzle place, can effectively avoid particle to block the phenomenon of atomizer nozzle.
As preferably, the gap between the top of described nozzle cover 5 and the bottom of atomization cylindrical shell 3 is first annular gap 6 of 360 °.This setting can make 360 °, the nozzle injection of atomizer, and jeting effect is good.
As preferably, also comprise spiro column 23, the upper end of described spiro column 23 is positioned at atomization cylindrical shell 3 and is connected with the madial wall of atomization cylindrical shell 3, lower end is exposed at and is atomized outside cylindrical shell 3 and is connected with nozzle cover 5 for nozzle cover 5 being fixed on the below being atomized cylindrical shell 3, and described spiro column 23 is provided with the drainage channel for being communicated with the mixing chamber 4 on atomization cylindrical shell 3 top.Adopt spiro column 23 nozzle cover 5 to be fixed on the below of atomization cylindrical shell 3, structure is simple, design cost is low.
As preferably, the upper end of described spiro column 23 is stub end 8, lower end is cylinder 9, described drainage channel comprises at least one first through hole 10 be arranged on stub end 8, and being arranged on second annular gap 11 of between the lateral wall of cylinder 9 and the madial wall of atomization cylindrical shell 3 360 °, described first through hole 10 communicates with the second annular gap 11.This setting makes that the structure of drainage channel is simple, design cost is low.
As preferably, one end that described cylinder 9 is exposed at outside atomization cylindrical shell 3 is provided with external thread section 12, the top being positioned at external thread section 12 of described cylinder 9 is provided with the spacing preiection 13 be connected with external thread section 12, described nozzle cover 5 is centrally axially arranged with axis hole, described cylinder 9 is provided with the axis hole of one end through nozzle cover 5 of external thread section 12, also be provided with between described spacing preiection 13 and nozzle cover 5 and regulate pad 14 for regulating the openings of sizes of nozzle, nozzle cover 5 and adjustment pad 14 are pressed on spacing preiection 13 by the below that one nut 15 is tightened on nozzle cover 5, nut 15 can be cover type nut.This setting had both made nozzle cover 5 become dismountable structure, again by changing the size regulating the thickness of pad 14 to change the first annular gap 6 between the top of nozzle cover 5 and the bottom of atomization cylindrical shell 3, coordinate the design of trumpet flare 7 again, the adjustment of the spray angle to nozzle, height and flow can be reached.
As preferably, described double-current body 1 comprises fluid connection 16, gas connection 17 and the interior pipe 18 coaxially arranged and outer tube 19, described fluid connection 16 communicates with interior pipe 18 formation fluid passage, and gas connection 17 communicates with the space between interior pipe 18 and outer tube 19 formation gas passage.
As preferably, described converging device 2 comprises pedestal 20, described interior pipe 18 is all connected with pedestal 20 with outer tube 19, described pedestal 20 and the junction of interior pipe 18 arrange the second through hole 21 for communicating with fluid passage, described pedestal 20 are at least arranged between interior pipe 18 and outer tube 19 third through-hole 22 for communicating with gas passage.This converging device 2 structure is simple, design cost is low.
As preferably, described double-current body 1 is arranged with atomization cylindrical shell 3 is mutually vertical.This setting can make that entire length reduces, structure is compacter.
As preferably, the junction of described interior pipe 18 and converging device 2 is by arc section transition, and the junction of described outer tube 19 and converging device 2 is also by arc section transition.This setting can make fluid pass through smoothly, reduces friction, thus reduces the damage to device.
As preferably, described double-current body 1, converging device 2, atomization cylindrical shell 3, spiro column 23 and nozzle cover 5 all adopt stainless steel acid-resistant steel material to make.Select resistant material, the acidproof corrosion resistance of device can be improved.
Claims (10)
1. a flue gas deacidification atomizer, comprise double-current body (1), converging device (2) and atomization cylindrical shell (3), described double-current body (1) is provided with for carrying compressed-air actuated gas passage and for carrying the fluid passage of calcium hydroxide slurry, described converging device (2) is communicated with the mixing chamber (4) on double-current body (1) and atomization cylindrical shell (3) top, it is characterized in that: also comprise the nozzle cover (5) being arranged on atomization cylindrical shell (3) below, the madial wall of described atomization cylindrical shell (3) bottom arranges trumpet flare (7), an intersegmental gap is provided with for cooperatively forming nozzle with trumpet flare (7) between the top of described nozzle cover (5) and the bottom of atomization cylindrical shell (3), described nozzle is communicated with mixing chamber (4).
2. a kind of flue gas deacidification atomizer according to claim 1, is characterized in that: the gap between the top of described nozzle cover (5) and the bottom of atomization cylindrical shell (3) is first annular gap (6) of 360 °.
3. a kind of flue gas deacidification atomizer according to claim 1, it is characterized in that: also comprise spiro column (23), the upper end of described spiro column (23) is positioned at atomization cylindrical shell (3) and is connected with the madial wall of atomization cylindrical shell (3), lower end is exposed at atomization cylindrical shell (3) and is connected for nozzle cover (5) is fixed on the below being atomized cylindrical shell (3) outward and with nozzle cover (5), and described spiro column (23) is provided with the drainage channel for being communicated with the mixing chamber (4) on atomization cylindrical shell (3) top.
4. a kind of flue gas deacidification atomizer according to claim 3, it is characterized in that: the upper end of described spiro column (23) is stub end (8), lower end is cylinder (9), described drainage channel comprises at least one first through hole (10) be arranged on stub end (8), and second annular gap (11) of 360 ° be arranged between the lateral wall of cylinder (9) and the madial wall of atomization cylindrical shell (3), described first through hole (10) communicates with the second annular gap (11).
5. a kind of flue gas deacidification atomizer according to claim 4, it is characterized in that: described cylinder (9) is exposed at atomization cylindrical shell (3) one end outward and is provided with external thread section (12), the top being positioned at external thread section (12) of described cylinder (9) is provided with the spacing preiection (13) be connected with external thread section (12), described nozzle cover (5) is centrally axially arranged with axis hole, described cylinder (9) is provided with the axis hole of one end through nozzle cover (5) of external thread section (12), also be provided with between described spacing preiection (13) and nozzle cover (5) and regulate pad (14) for regulating the openings of sizes of nozzle, nozzle cover (5) and adjustment pad (14) are pressed on spacing preiection (13) by the below that one nut (15) is tightened on nozzle cover (5).
6. a kind of flue gas deacidification atomizer according to claim 1, it is characterized in that: described double-current body (1) comprises fluid connection (16), gas connection (17) and the interior pipe (18) coaxially arranged and outer tube (19), described fluid connection (16) communicates with interior pipe (18) formation fluid passage, and gas connection (17) communicates with the space between interior pipe (18) and outer tube (19) formation gas passage.
7. a kind of flue gas deacidification atomizer according to claim 6, it is characterized in that: described converging device (2) comprises pedestal (20), described interior pipe (18) is all connected with pedestal (20) with outer tube (19), described pedestal (20) and the junction of interior pipe (18) arrange the second through hole (21) for communicating with fluid passage, described pedestal (20) are positioned between pipe (18) and outer tube (19) and at least arrange a third through-hole (22) for communicating with gas passage.
8. a kind of flue gas deacidification atomizer according to claim 7, is characterized in that: described double-current body (1) is arranged with atomization cylindrical shell (3) is mutually vertical.
9. a kind of flue gas deacidification atomizer according to claim 8, it is characterized in that: described interior pipe (18) passes through arc section transition with the junction of converging device (2), described outer tube (19) also passes through arc section transition with the junction of converging device (2).
10. a kind of flue gas deacidification atomizer according to claim 1, is characterized in that: described double-current body (1), converging device (2), atomization cylindrical shell (3), spiro column (23) and nozzle cover (5) all adopt stainless steel acid-resistant steel material to make.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610012217.3A CN105457796A (en) | 2016-01-07 | 2016-01-07 | Smoke deacidification atomizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610012217.3A CN105457796A (en) | 2016-01-07 | 2016-01-07 | Smoke deacidification atomizer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105457796A true CN105457796A (en) | 2016-04-06 |
Family
ID=55596209
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610012217.3A Pending CN105457796A (en) | 2016-01-07 | 2016-01-07 | Smoke deacidification atomizer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105457796A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109611888A (en) * | 2018-12-14 | 2019-04-12 | 中国航发沈阳发动机研究所 | A kind of emple hole |
| CN112827689A (en) * | 2021-02-03 | 2021-05-25 | 苏州恒洁润洁具科技有限公司 | Atomizing water tap |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SE447704B (en) * | 1985-04-16 | 1986-12-08 | Flaekt Ab | CONTACT REACTOR DEVICE INCLUDING MEASURES TO PREVENT RECYCLING OF ABSORPTION MATERIALS TO THE SIZE SURFACE |
| CN2043895U (en) * | 1988-12-29 | 1989-09-06 | 李保民 | Adjustable dished spray head |
| CN2344091Y (en) * | 1998-09-22 | 1999-10-20 | 马锦明 | Adjustable sprayer |
| CN1652876A (en) * | 2002-05-07 | 2005-08-10 | 喷洒系统公司 | Internal mix air atomizing spray nozzle assembly |
| CN2724848Y (en) * | 2004-06-30 | 2005-09-14 | 宝山钢铁股份有限公司 | Spray-nozzle for removing dust |
| CN2741666Y (en) * | 2004-06-21 | 2005-11-23 | 杨风起 | Anti-scale shower nozzle |
| CN101287555A (en) * | 2005-10-07 | 2008-10-15 | 迪特尔·沃尔兹 | Atomizing nozzle for two substances |
| CN201944826U (en) * | 2011-01-24 | 2011-08-24 | 杭州杭辅电站辅机有限公司 | Steam attemperator with spring-adjustable umbrella-shaped atomizing nozzle |
| CN102989298A (en) * | 2012-11-30 | 2013-03-27 | 浙江泰来环保科技有限公司 | Acid-removing and desulfurizing device |
| CN204148020U (en) * | 2014-09-22 | 2015-02-11 | 浙江江山化工股份有限公司 | A kind of anti-clogging atomizer |
| CN204208691U (en) * | 2014-10-17 | 2015-03-18 | 杭州杭真真空工程技术有限公司 | The adjustable washer jet of a kind of lobe pump |
| CN204933816U (en) * | 2015-07-29 | 2016-01-06 | 杭州余杭獐山钢瓶有限公司 | For the inner spray coating device of reducing steel cylinder |
| CN205269988U (en) * | 2016-01-07 | 2016-06-01 | 浙江泰来环保科技有限公司 | Flue gas deacidification atomizer |
-
2016
- 2016-01-07 CN CN201610012217.3A patent/CN105457796A/en active Pending
Patent Citations (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SE447704B (en) * | 1985-04-16 | 1986-12-08 | Flaekt Ab | CONTACT REACTOR DEVICE INCLUDING MEASURES TO PREVENT RECYCLING OF ABSORPTION MATERIALS TO THE SIZE SURFACE |
| CN2043895U (en) * | 1988-12-29 | 1989-09-06 | 李保民 | Adjustable dished spray head |
| CN2344091Y (en) * | 1998-09-22 | 1999-10-20 | 马锦明 | Adjustable sprayer |
| CN1652876A (en) * | 2002-05-07 | 2005-08-10 | 喷洒系统公司 | Internal mix air atomizing spray nozzle assembly |
| CN2741666Y (en) * | 2004-06-21 | 2005-11-23 | 杨风起 | Anti-scale shower nozzle |
| CN2724848Y (en) * | 2004-06-30 | 2005-09-14 | 宝山钢铁股份有限公司 | Spray-nozzle for removing dust |
| CN101287555A (en) * | 2005-10-07 | 2008-10-15 | 迪特尔·沃尔兹 | Atomizing nozzle for two substances |
| CN201944826U (en) * | 2011-01-24 | 2011-08-24 | 杭州杭辅电站辅机有限公司 | Steam attemperator with spring-adjustable umbrella-shaped atomizing nozzle |
| CN102989298A (en) * | 2012-11-30 | 2013-03-27 | 浙江泰来环保科技有限公司 | Acid-removing and desulfurizing device |
| CN204148020U (en) * | 2014-09-22 | 2015-02-11 | 浙江江山化工股份有限公司 | A kind of anti-clogging atomizer |
| CN204208691U (en) * | 2014-10-17 | 2015-03-18 | 杭州杭真真空工程技术有限公司 | The adjustable washer jet of a kind of lobe pump |
| CN204933816U (en) * | 2015-07-29 | 2016-01-06 | 杭州余杭獐山钢瓶有限公司 | For the inner spray coating device of reducing steel cylinder |
| CN205269988U (en) * | 2016-01-07 | 2016-06-01 | 浙江泰来环保科技有限公司 | Flue gas deacidification atomizer |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109611888A (en) * | 2018-12-14 | 2019-04-12 | 中国航发沈阳发动机研究所 | A kind of emple hole |
| CN112827689A (en) * | 2021-02-03 | 2021-05-25 | 苏州恒洁润洁具科技有限公司 | Atomizing water tap |
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Effective date of registration: 20181119 Address after: 315176 No. 149 Ketai Road, Wangchun Industrial Park, Haishu District, Ningbo City, Zhejiang Province Applicant after: Ningbo Tailai environmental protection equipment Co., Ltd. Address before: 315176 No. 149 Ketai Road, Wangchun Industrial Park, Yinzhou District, Ningbo City, Zhejiang Province Applicant before: Zhejiang Eco-Waste Technology Co., Ltd. |
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Application publication date: 20160406 |