CN101468274A - Wet dust separator - Google Patents

Wet dust separator Download PDF

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Publication number
CN101468274A
CN101468274A CNA2007103045979A CN200710304597A CN101468274A CN 101468274 A CN101468274 A CN 101468274A CN A2007103045979 A CNA2007103045979 A CN A2007103045979A CN 200710304597 A CN200710304597 A CN 200710304597A CN 101468274 A CN101468274 A CN 101468274A
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CN
China
Prior art keywords
section
venturi tube
wet scrubber
air inlet
larynx section
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
Application number
CNA2007103045979A
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Chinese (zh)
Inventor
陈光亮
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Haisibote (Beijing) Technology Co Ltd
Original Assignee
Haisibote (Beijing) Technology Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Haisibote (Beijing) Technology Co Ltd filed Critical Haisibote (Beijing) Technology Co Ltd
Priority to CNA2007103045979A priority Critical patent/CN101468274A/en
Priority to US12/119,745 priority patent/US20090165685A1/en
Publication of CN101468274A publication Critical patent/CN101468274A/en
Pending legal-status Critical Current

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D47/00Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/10Venturi scrubbers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D47/00Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/06Spray cleaning

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Separation Of Particles Using Liquids (AREA)

Abstract

The invention relates to a wet dust collector, which comprises a venturi tube and a cylindrical washer, wherein an air outlet of the venturi tube is connected with an air inlet of the cylindrical washer; the venturi tube consists of a contraction section, a throat section and a diffusion section; the side wall of the throat section is provided with a plurality of through holes, and the outer sides of the through holes are connected with a pressure water supply pipe; a port of the diffusion section forms the air outlet of the venturi tube; a port of the contraction section forms an air inlet of the venturi tube; and the inside of the cylindrical washer is provided with a plurality of spray nozzles distributed on the cross section respectively, and a plurality of layers of dewatering wire meshes. The cylindrical washer is U-shaped, an air inlet pipe of the cylindrical washer adopts a structure of horizontal and tangential air intake, and the bottom of the air intake pipe is cambered. The wet dust collector has the advantages of small investment, high dust removing efficiency, comparatively longer service life, small water consumption and low running cost, and can be mainly applied to the dust removal of high density flue gas and industrial dust in various industrial furnaces.

Description

Wet scrubber
Technical field
The present invention relates to a kind of wet scrubber, mainly can be used for the high concentration flue gas ash removal of various industrial furnaces and the dedusting of industrial dust.
Background technology
Industrial dedusting mainly contains dry dust removal and wet dust removal two big classes, wherein dry dust removal mainly comprises dust settling pocket technique and electrostatic precipitation technology, wet dust removal mainly is spray woods tower, foaming tower, Venturi tube, impact or self-excitation dedusting technology or the like, various technology all have many advantages separately, but its deficiency is still more outstanding, wherein the major defect of dry dust removal is that investment is big, operating cost is high, floor space is big, and wet dust removal is subjected to the restriction of dust characteristic, under the dust condition that adapts to, then should pay attention to problems such as efficiency of dust collection, service life and water consumption.
Summary of the invention
For overcoming the defective of prior art, the invention provides a kind of wet scrubber, this wet scrubber is longer relatively required small investment, efficiency of dust collection height, service life, and water consumption is less, and operating cost is low.
The present invention realizes that the technical scheme of above-mentioned purpose is: a kind of wet scrubber, comprise Venturi tube and cylindric washer, the gas outlet of described Venturi tube connects the air inlet of described cylindric washer, described Venturi tube is by contraction section, larynx section and diffuser constitute, described larynx section sidewall is provided with some through holes, the outside of described through hole connects the pressure water supply pipe, the port of described diffuser constitutes the gas outlet of described Venturi tube, the port of described contraction section constitutes the air inlet of described Venturi tube, be provided with the plurality of nozzles that distributes on some cross sections respectively in the described cylindric washer, and be provided with several layers dehydration silk screen.
Operation principle of the present invention and beneficial effect are: processed gas such as flue gas enters Venturi tube by pipeline from the contraction section port of Venturi tube, dwindle because of caliber during through the larynx section, it is big that flow velocity becomes, form certain suction static pressure, described high service pipe connects cleaning solution, cooperate suction function cleaning solution to be squeezed into the larynx section of Venturi tube by pump, gas is involved in cleaning solution in the air-flow, fully mix with gas, make the dust in the gas enter cleaning solution, air-flow comes out to enter cylindric washer from diffuser, the cleaning solution water smoke of shower nozzle ejection continues same airflow collision, play further dedusting effect, simultaneously since in cylindric washer speed descend, the water smoke in the air-flow collides with silk screen during through silk screen, on silk screen, realized gas-liquid separation thus, the air-flow after the separation is substantially free of dust and other impurity, has realized the dedusting purpose thus.Venturi tube is combined with the cylindric washer that is beneficial to gas-liquid separation efficiently because the present invention has adopted, and has guaranteed efficiency of dust collection and gas-liquid separation effect, the efficiency of dust collection height; Owing to adopt the mode of high service in the larynx section of Venturi tube; overcome the little defective of amount of liquor that following negative pressure that forms by high velocity air of prior art absorbs; enough liquid-gas ratios have been guaranteed; improved efficiency of dust collection thus; simultaneously owing to the water yield that enters the larynx section under the high pressure is big; on larynx section sidewall, form water membrane, the larynx section sidewall of serious wear has been played good protective action, help improving service life.
Description of drawings
Fig. 1 is a structural representation of the present invention.
The specific embodiment
Referring to Fig. 1, a kind of wet scrubber, comprise Venturi tube and cylindric washer, the gas outlet of described Venturi tube connects the air inlet of described cylindric washer, described Venturi tube is made of contraction section 11, larynx section 12 and diffuser 13, described larynx section sidewall is provided with some through holes 14, the outside of described through hole connects pressure water supply pipe 15, the port of described diffuser constitutes the gas outlet of described Venturi tube, the port of described contraction section constitutes the air inlet of described Venturi tube, be provided with distribution plurality of nozzles 25 on some cross sections respectively in the described cylindric washer, and be provided with several layers dehydration silk screen 26.
The contraction section of described Venturi tube, larynx section and diffuser are one, mutual connection can be welding, also can be that flange connects, can also be one-body molded, described larynx section adopts the rectangular tube of sizing usually, and described through hole is opened on two relative in larynx section wall sidewalls usually, also can open on four sidewalls, its position should be distributed in whole larynx section or be distributed in more than half larynx section, so that form moisture film on whole larynx section sidewall from the position that larynx section and contraction section join.
The outside that described larynx section is distributed with through hole can be provided with the closure casing that the through hole on this sidewall is surrounded, described housing is connected with inlet channel, this inlet channel is provided with water pump, so that supply water to the housing internal pressure, by such housing is set, not only make to through hole water supply to become easily, but also can form certain static pressure, guarantee that the pressure of supply water of each through hole is equal substantially.
In the practice, described larynx section can have two relative sidewalls and relative two rectangular tank of being clipped between these two sidewalls constitute, and the sidewall of described rectangular tank inboard has constituted the sidewall of described larynx section, has described through hole on this sidewall.
Described cylindric washer takes the shape of the letter U, its air inlet pipe 21 adopts the structure of horizontal tangential air inlet, be installed on the barrel of a side 22 of U-shaped structure, its escape pipe 23 is installed in the top of barrel of the opposite side 24 of U-shaped structure, extend upward, the air-flow that enters cylindric washer from Venturi tube can form eddy flow in the air inlet pipe side neck chamber of cylindric washer thus, with further raising gas-liquid mixed ability, this eddy flow fades away through a segment distance and through behind the described dehydration silk screen, form stable air-flow in another side neck chamber of cylindric washer, so that gas-liquid separation.The bottom camber of described cylindric washer, air-flow be at cylindric washer bottom conversion direction, helps thus coming out water droplet is centrifugal.
The number of plies of described dehydration silk screen can be 1 one 3 layers usually, the silk screen space can be 1.5 1 2.5 millimeters, determine that according to dust characteristic, concentration and air velocity described nozzle is evenly distributed on the whole cross section, the particle diameter of water droplets can be 0.5mm-1.5mm, in the collision of water smoke and grit, adsorb grit, and the cohesion water fog particle, big water droplet formed, so that dehydration can be provided with inspection manhole on the described cylindrical shell.

Claims (10)

1. wet scrubber, it is characterized in that comprising Venturi tube and cylindric washer, the gas outlet of described Venturi tube connects the air inlet of described cylindric washer, described Venturi tube is made of contraction section, larynx section and diffuser, described larynx section sidewall is provided with some through holes, the outside of described through hole connects the pressure water supply pipe, the port of described diffuser constitutes the gas outlet of described Venturi tube, the port of described contraction section constitutes the air inlet of described Venturi tube, be provided with the plurality of nozzles that distributes on some cross sections respectively in the described cylindric washer, and be provided with several layers dehydration silk screen.
2. wet scrubber as claimed in claim 1 is characterized in that described larynx section adopts the rectangular tube of sizing.
3. wet scrubber as claimed in claim 2 is characterized in that described through hole is opened on two relative in larynx section wall sidewalls, perhaps opens on four sidewalls.
4. wet scrubber as claimed in claim 3 is characterized in that the through hole on the described trunnion sidewall begins to be distributed in whole larynx section or is distributed in more than half larynx section from the position that larynx section and contraction section join.
5. wet scrubber as claimed in claim 4 is characterized in that the through hole outside on the described larynx section sidewall is provided with the closure casing that these through holes are surrounded, and described closure casing is connected with inlet channel, and this inlet channel is provided with water pump.
6. wet scrubber as claimed in claim 5 is characterized in that described larynx section is made of two relative sidewalls and two relative rectangular tank of being clipped between these two sidewalls, and the sidewall of described rectangular tank inboard has constituted the sidewall of described larynx section.
7. as claim 1,2,3,4,5 or 6 described wet scrubbers, it is characterized in that described cylindric washer takes the shape of the letter U, its air inlet pipe adopts the structure of horizontal tangential air inlet, is installed on the side tube-wall of U-shaped structure, its escape pipe is installed in the top of the opposite side barrel of U-shaped structure, extends upward.
8. wet scrubber as claimed in claim 7 is characterized in that the bottom of described cylindric washer is curved.
9. wet scrubber as claimed in claim 8, the number of plies that it is characterized in that described dehydration silk screen is 1-3 layers, the space of dehydration silk screen is 1.5-2.5 millimeters.
10. wet scrubber as claimed in claim 9 is characterized in that described nozzle is evenly distributed on the whole cross section, and the particle diameter of the water droplets of its ejection is 0.5mm-1.5mm.
CNA2007103045979A 2007-12-28 2007-12-28 Wet dust separator Pending CN101468274A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
CNA2007103045979A CN101468274A (en) 2007-12-28 2007-12-28 Wet dust separator
US12/119,745 US20090165685A1 (en) 2007-12-28 2008-05-13 wet dust remover

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNA2007103045979A CN101468274A (en) 2007-12-28 2007-12-28 Wet dust separator

Publications (1)

Publication Number Publication Date
CN101468274A true CN101468274A (en) 2009-07-01

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ID=40796563

Family Applications (1)

Application Number Title Priority Date Filing Date
CNA2007103045979A Pending CN101468274A (en) 2007-12-28 2007-12-28 Wet dust separator

Country Status (2)

Country Link
US (1) US20090165685A1 (en)
CN (1) CN101468274A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103845981A (en) * 2012-11-28 2014-06-11 沈阳铝镁设计研究院有限公司 Filtering apparatus of reduction jar and filtering method
CN104028068A (en) * 2014-03-10 2014-09-10 江苏宝丽环保科技有限公司 A multistage deduster
CN104500286A (en) * 2014-12-25 2015-04-08 雷同飞 Efficient air filter
CN107638770A (en) * 2017-10-27 2018-01-30 广西贝仕特环保科技有限公司 A kind of water circulation Waste gas purifying machine
CN109579016A (en) * 2018-12-07 2019-04-05 朱海斌 A kind of small rural consumer waste incineration purifying and dedusting device

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107817826B (en) * 2017-11-21 2020-07-14 重庆凯西驿电子科技有限公司 Control device based on sensitive trigger silicon controlled rectifier
CN114251926B (en) * 2021-12-30 2023-03-14 宜春万申制药机械有限公司 Boiling dryer

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4095737B2 (en) * 1999-03-29 2008-06-04 日本エア・リキード株式会社 Cleaning dust collector and exhaust gas treatment facility
US6251168B1 (en) * 1999-07-23 2001-06-26 Hudson Products Corporation High efficiency gas scrubber using combined coalescing media and centrifugal cyclone
US6241809B1 (en) * 1999-09-20 2001-06-05 Dan Hopkins Apparatus and method for liquid scrubbing contaminants from a gas flow
FR2832936B1 (en) * 2001-12-05 2004-02-20 Snecma Moteurs PROCESS AND PLANT FOR THE TREATMENT OF EFFLUENT GASES CONTAINING HYDROCARBONS
US6953495B2 (en) * 2003-07-31 2005-10-11 Envirocare International, Inc. Low-energy venturi pre-scrubber for an air pollution control system and method

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103845981A (en) * 2012-11-28 2014-06-11 沈阳铝镁设计研究院有限公司 Filtering apparatus of reduction jar and filtering method
CN103845981B (en) * 2012-11-28 2015-08-19 沈阳铝镁设计研究院有限公司 A kind of reductive jar filter and filter method
CN104028068A (en) * 2014-03-10 2014-09-10 江苏宝丽环保科技有限公司 A multistage deduster
CN104500286A (en) * 2014-12-25 2015-04-08 雷同飞 Efficient air filter
CN104500286B (en) * 2014-12-25 2017-10-10 西京学院 A kind of efficient air cleaner
CN107638770A (en) * 2017-10-27 2018-01-30 广西贝仕特环保科技有限公司 A kind of water circulation Waste gas purifying machine
CN109579016A (en) * 2018-12-07 2019-04-05 朱海斌 A kind of small rural consumer waste incineration purifying and dedusting device

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Open date: 20090701