CN101332387A - Flue type mist water separator - Google Patents
Flue type mist water separator Download PDFInfo
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- CN101332387A CN101332387A CNA2008100212762A CN200810021276A CN101332387A CN 101332387 A CN101332387 A CN 101332387A CN A2008100212762 A CNA2008100212762 A CN A2008100212762A CN 200810021276 A CN200810021276 A CN 200810021276A CN 101332387 A CN101332387 A CN 101332387A
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Abstract
The invention discloses a stove-pipe type mist-water separator, and more particularly relates to the stove-pipe type mist-water separator used for carrying out mist-water separation on the flue gases with water discharged by wet dust separators such as a scrubbing tower. The mist-water separator is applicable to the wet dust separators such as the scrubbing tower and a tower absorption system in the industries such as the chemical plant, the fuel electric plant and the mine, etc. The mist-water separator is characterized by containing a cylinder which is internally provided with a prerotation vane. The prerotation vane takes a spiral shape and is arranged along the inner wall of the cylinder from top to bottom, and the outer edge of the prerotation vane is fixedly connected with the inner wall of the cylinder. A ring-shaped sink is arranged at the lower end of the cylinder and is distributed along the circumferential direction of the inner wall of the cylinder. A water outlet is arranged on the wall of the cylinder which is corresponding to the ring-shaped sink. The stove-pipe type mist-water separator has the advantages of using fewer equipment, needing less investment and being low in cost.
Description
Technical field
The present invention relates to the wet scrubber corollary equipment.Specifically, be used for to the band shredded tobacco for water pipes gas that wet scrubber such as scrubbing tower are discharged carry out mist, moisture from flue type mist water separator.Be applicable on the wet scrubbers such as the scrubber system of industries such as chemical plant, thermal power plant and mine and absorption tower system.
Background technology
As everyone knows, for the pollution that the band shredded tobacco for water pipes gas of eliminating industry chimneys discharges such as chemical plant, thermal power plant and mine brings atmosphere, mostly adopt wet scrubber such as scrubbing tower that flue gas is carried out spray washing, to remove the dust in the flue gas.Though removed the dust in the flue gas by scrubbing tower, still be entrained with contaminant particle and a large amount of water smoke in the gas after the scrubbing tower washing, this water smoke enters atmosphere with contaminant particle as not separating, and still can cause certain pollution to atmosphere.In addition, band aqueous vapor body is totally unfavorable to the work of exhaust blower.Therefore, the scrubbing tower rear portion all is furnished with the fog separator, so that a large amount of water smoke and contaminant particle are separated from gas.
Traditional fog separator is made up of Venturi tube and cyclone type mist water separator.Though adopt this fog separator a large amount of water smoke and contaminant particle can be separated from gas, need devices such as Venturi tube, cyclone type mist water separator and multistage flue, the equipment of use is more, investment is many, cost is higher.
Summary of the invention
The problem to be solved in the present invention is to overcome disadvantages of background technology, a kind of flue type mist water separator is provided.This flue type mist water separator, device therefor is few, small investment, cost are low.
For addressing the above problem, take following technical scheme:
Flue type mist water separator characteristics of the present invention are to contain cylinder, and flow deflector is arranged in the cylinder.Described flow deflector is a helical form, and its inwall along cylinder is arranged from top to bottom and its outer edge is connected mutually with the inwall of cylinder.
In the cylinder lower end annular water tank is arranged, this annular water tank is along the inwall circumferential arrangement of cylinder.With on the corresponding cylindrical wall of annular water tank delivery port is arranged.
Described annular water tank is to weld ring plate earlier on cylinder inner wall, and makes the inside edge of ring plate upwards turn up and form.
Take such scheme, have the following advantages:
Because flue type mist water separator of the present invention constitutes by cylinder with along the helical form flow deflector that the inwall of cylinder is arranged from top to bottom, the flue type mist water separator that is made of the helical form flow deflector in a cylinder and the cylinder has replaced traditional mist water separator of being made up of Venturi tube, cyclone type mist water separator and multistage flue, thereby reduced use equipment, reduced investment and processing cost.
Description of drawings
Fig. 1 is a flue type mist water separator structural representation of the present invention;
Fig. 2 is the A-A cross-sectional schematic of Fig. 1.
The specific embodiment
As depicted in figs. 1 and 2, flue type mist water separator of the present invention contains cylinder 1, is provided with flow deflector 2 in the cylinder 1.Described flow deflector 2 is a helical form, and the inwall that its inwall along cylinder 1 is shape screw arrangement from top to bottom and its outer edge and cylinder 1 is fixed together.
The lower end of cylinder 1 inner chamber is provided with annular water tank 3, and this annular water tank is along the inwall circumferential arrangement of cylinder 1.Be processed with delivery port 4 on annular water tank 3 corresponding cylinder 1 walls.
Described annular water tank 3 is to weld ring plate earlier on cylinder 1 inwall, and makes the inside edge of ring plate upwards turn up and form.
During work, after the flue gas that has a large amount of water smokes enters cylinder 1 from cylinder 1 upper end, flue gas is changed to be flowed to and speed, formation is than the vortex of wide-angle, so that the little water droplet in the flue gas is being thrown under the effect of centrifugal acceleration power on cylinder 1 inwall, and merge with the moisture film that sticks on cylinder 1 inwall, form weep and wash cylinder 1 inwall equably.At last, in the annular water tank 3 of cylinder 1 bottom, accumulate current, and discharge by delivery port 4.
Claims (3)
1. flue type mist water separator is characterized in that containing cylinder (1), and flow deflector (2) is arranged in the cylinder; This flow deflector is a helical form, and its inwall along cylinder (1) is arranged from top to bottom and its outer edge is connected mutually with the inwall of cylinder (1).
2. flue type mist water separator according to claim 1 is characterized in that there is annular water tank (3) cylinder (1) lower end, and this annular water tank is along the inwall circumferential arrangement of cylinder (1); On cylinder (1) wall delivery port (4) is arranged accordingly with annular water tank (3).
3. flue type mist water separator according to claim 1 is characterized in that described annular water tank (3) is to weld ring plate earlier on cylinder (1) inwall, and makes the inside edge of ring plate upwards turn up and form.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2008100212762A CN101332387A (en) | 2008-07-23 | 2008-07-23 | Flue type mist water separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2008100212762A CN101332387A (en) | 2008-07-23 | 2008-07-23 | Flue type mist water separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN101332387A true CN101332387A (en) | 2008-12-31 |
Family
ID=40195427
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNA2008100212762A Pending CN101332387A (en) | 2008-07-23 | 2008-07-23 | Flue type mist water separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101332387A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102059042A (en) * | 2010-10-30 | 2011-05-18 | 陈群 | Combination unit for multilevel heat exchange and gas liquid separation |
| CN103657388A (en) * | 2013-12-06 | 2014-03-26 | 无锡雪浪环境科技股份有限公司 | COCone type semidry process reaction tower |
| CN103706190A (en) * | 2013-12-24 | 2014-04-09 | 江苏江成冶金设备制造有限公司 | Three-phase separator for purifying sintering flue gas |
| CN106268200A (en) * | 2016-08-15 | 2017-01-04 | 宁波德泰化学有限公司 | A kind of classification dehydrating unit |
| CN109420385A (en) * | 2017-09-03 | 2019-03-05 | 郝占宁 | A kind of whirlpool formula air purifier and the air purification method based on the clarifier |
-
2008
- 2008-07-23 CN CNA2008100212762A patent/CN101332387A/en active Pending
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102059042A (en) * | 2010-10-30 | 2011-05-18 | 陈群 | Combination unit for multilevel heat exchange and gas liquid separation |
| CN103657388A (en) * | 2013-12-06 | 2014-03-26 | 无锡雪浪环境科技股份有限公司 | COCone type semidry process reaction tower |
| CN103657388B (en) * | 2013-12-06 | 2015-11-04 | 无锡雪浪环境科技股份有限公司 | A kind of taper semidry method reaction tower |
| CN103706190A (en) * | 2013-12-24 | 2014-04-09 | 江苏江成冶金设备制造有限公司 | Three-phase separator for purifying sintering flue gas |
| CN103706190B (en) * | 2013-12-24 | 2015-10-28 | 江苏江成冶金设备制造有限公司 | For the three phase separator of sintering gas purifying |
| CN106268200A (en) * | 2016-08-15 | 2017-01-04 | 宁波德泰化学有限公司 | A kind of classification dehydrating unit |
| CN106268200B (en) * | 2016-08-15 | 2019-08-13 | 宁波德泰化学有限公司 | A kind of classification dehumidification device |
| CN109420385A (en) * | 2017-09-03 | 2019-03-05 | 郝占宁 | A kind of whirlpool formula air purifier and the air purification method based on the clarifier |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| ASS | Succession or assignment of patent right |
Owner name: JIANGSU QUANNENG ENVIRONMENT ENGINEERING CO., LTD. Free format text: FORMER OWNER: CHEN MINDONG Effective date: 20090403 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20090403 Address after: Jiangsu province Yixing city dingshuzhen Tang Lu post encoding: 214221 Applicant after: Jiangsu Quanneng Environment Engineering Co., Ltd. Address before: 402, room 112, Cang Bang new village, Yicheng street, Yixing, Jiangsu, China Post Code: 214221 Applicant before: Chen Min Dong Co-applicant before: Zhou Tinghua |
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| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Open date: 20081231 |