CN1302682A - Flow-guiding condensing duster and its technique - Google Patents

Flow-guiding condensing duster and its technique Download PDF

Info

Publication number
CN1302682A
CN1302682A CN 01103982 CN01103982A CN1302682A CN 1302682 A CN1302682 A CN 1302682A CN 01103982 CN01103982 CN 01103982 CN 01103982 A CN01103982 A CN 01103982A CN 1302682 A CN1302682 A CN 1302682A
Authority
CN
China
Prior art keywords
flow
guiding
type
condensing
buffler
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
CN 01103982
Other languages
Chinese (zh)
Inventor
李启山
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CN 01103982 priority Critical patent/CN1302682A/en
Publication of CN1302682A publication Critical patent/CN1302682A/en
Pending legal-status Critical Current

Links

Images

Landscapes

  • Cyclones (AREA)
  • Separating Particles In Gases By Inertia (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)

Abstract

A flow-guiding condensing deduster features that a guide tube type mixed flow-device composed of flue partition, flow-guiding tube and inner surface through the main body is arranged at lower part of main body so as to omit circulating water pump and sprayer, and a cyclon suction type condensing cleaner composed of settling chamber and cyclon sucker is arranged at upper part of main body to condense the water vapour containing dust into liquid drops which are then centrifugally separated out. Its advantages are high desulfurizing and dedusting effect and low cost.

Description

A kind of flow-guiding condensing duster and technology thereof
The invention belongs to a kind of deduster and technology thereof that the environmental protection aspect is used, particularly a kind of flow-guiding condensing duster and technology thereof belong to processing technique field.
In the prior art purified treatment is carried out in the stove atmosphere pollution, wet type desulfurizing dust collector that is adopted and technology thereof, as products such as granite dusters, owing to aspect mixed flow, can not accomplish even mixed flow and can not accomplish again aspect separating that steam is separated fast with air, so, in the water yield hour, tend to occur dragging the discharging that exceeds standard of floating part sulfur dioxide and oxynitrides, then when the water yield is big, air-introduced machine band water appears again easily, its operation and instability, efficient is low, maintenance cost is high, can not satisfy the use needs.
The purpose of this invention is to provide a kind of flow-guiding condensing duster and technology thereof, mainly below the deduster body, be combined into a catheter type flow mixing device by body by buffler and mozzle and inwall, thereby can realize the mixed flow effect of deduster without water circulating pump and shower nozzle, in addition, above the deduster body, be provided with the whirlwind suction-type condensation purifier of forming by expansion chamber and cyclone type inhalator, therefrom a large amount of cold airs is sucked in the expansion chamber and mix with flue gas by the cyclone type inhalator, making the steam that is inclusive with flue dust obtain forming drop after the condensation separates rapidly with air in centrifugal motion, promptly realize the purpose that it purifies air by condensation cleverly, thereby remedy the deficiencies in the prior art, effectively improve the desulfurization dust-removing efficiency of deduster, reduce operating cost.
A kind of flow-guiding condensing duster provided by the invention and technology thereof, implement by the following technical programs: above the deduster body, be provided with whirlwind suction-type condensation purifier, wherein, on the aperture plate of clarifier bottom near several centrifuge blades that is fixed with of the edge-perpendicular of mesopore, on centrifuge blade, be fixed with flow distribution plate, and near the outward flange of aperture plate vertical be fixed with several louvre blades, on louvre blade, be fixed with intercepter plate, on intercepter plate, face down drain tube is installed, for the purpose that is able to suck surrounding air makes the guiding of centrifuge blade opposite with the guiding of louvre blade, for a side that is gone in aperture plate in separator and emission shunting is shaped on hole draining downwards, promptly by aperture plate, centrifuge blade, louvre blade, intercepter plate, flow distribution plate constitute a cyclone type inhalator mutually.Above inhalator, be combined into an expansion chamber by discharge duct, anticorrosion liner plate, metal angle bead, expansion chamber and inhalator are combined and constitute whirlwind suction-type condensation purifier.Below clarifier, utilize the deduster body of Bolt Connection by flange, flue tube place in its bottom utilizes outer wall to be provided with flue shrouding and buffler, with several in the horizontal direction the mozzle of both-side opening connect with buffler by the waters that exceedes stream pond or control of dust water tank, the inlet end that wherein makes mozzle is by bolt or welding or build by laying bricks or stones and be fixed on the inwall that exceedes stream pond or control of dust water tank, the other end is blocked by shrouding, promptly form a catheter type flow mixing device mutually by buffler and mozzle and inwall by body.In addition, the osculum on the corresponding clarifier is provided with drain tube in body.
In use, the flue tube of deduster body is connected with the supplied flue gases pipeline, an amount of water of input in exceeding stream pond or control of dust water tank.When operation, when decline constitutes the space with buffler after flue gas is walked around buffler upwards to erupt the water surface pressurized that makes its contact by flue impact downwards, mozzle will exceed the water in stream pond or the control of dust water tank, at any time introduce in the body and carry out comparatively fine and smooth mixed flow, thereby do not need to use water circulating pump and shower nozzle just can realize the mixed flow effect of flue gas and current from both-side opening outflow and flue gas; Through the mixed flow water-dust mixture of eruption upwards, be subjected to the effect of flow distribution plate to be subjected to the guide effect of centrifuge blade crack to form centrifugal motion again by aperture plate, and rotation is risen between centrifuge blade and louvre blade, therefrom make separated object and air carry out initial gross separation, because it is opposite with it that the guiding of louvre blade crack is set in the centrifuge blade periphery, the flue gas between rotates the impulsive force that forms that rises at a high speed can't flee from flue gas itself from the crack of louvre blade, opposite because the flue gas that rotation is risen by the louvre blade crack to around the jet action that produces of cold air it is sucked in expansion chamber, being inhaled into a large amount of cold airs mixes with the steam that is inclusive with flue dust, make it to drop on the intercepter plate very soon with the centrifugal motion that rotates ascending air after drop is formed in condensation with air separation, flow on the aperture plate to return through drain tube again and exceed stream pond or control of dust water tank by the body drain tube, and the air behind the process isolation of purified is subjected to the interior pressure effect of deduster body, continues to rise in expansion chamber and is discharged by discharge duct.
Promptly, can fundamentally remedy the deficiencies in the prior art, effectively improve the desulfurization dust-removing efficiency of deduster, reduce operating cost by the said goods structure provided by the invention and technical method.
Below in conjunction with accompanying drawing the present invention is described in further details
Accompanying drawing 1 is looked cutaway view for the master of product structure provided by the invention and its technical method embodiment
Accompanying drawing 2 is the A-A cutaway view of accompanying drawing 1
Accompanying drawing 3 is the B-B cutaway view of accompanying drawing 1
See Fig. 1 and Fig. 2 and Fig. 3, be provided with whirlwind suction-type condensation purifier (I) in deduster body (III) top, wherein, be fixed with several centrifuge blades (7) near the edge-perpendicular of mesopore (D) on clarifier (I) bottom aperture plate (13), on centrifuge blade (7), be fixed with flow distribution plate (4), and near the outward flange of aperture plate (13) vertical be fixed with several louvre blades (6), on louvre blade (6), be fixed with intercepter plate (5), on intercepter plate (5), face down drain tube (19) is installed, for the purpose that is able to suck ambient cold air makes the guiding of centrifuge blade (7) opposite with the guiding of louvre blade (6), for a side that is gone in aperture plate (13) in separator and emission shunting is shaped on hole (C) draining downwards, promptly by aperture plate (13), centrifuge blade (7), louvre blade (6), intercepter plate (5), flow distribution plate (4) constitute a cyclone type inhalator (II) mutually.In the top of inhalator (II), be combined into an expansion chamber (V) by discharge duct (1), anticorrosion liner plate (2), metal angle bead (3), expansion chamber (V) and inhalator (II) are combined and constitute whirlwind suction-type condensation purifier (I).Below in clarifier (I), utilize the deduster body (III) of bolt (14) connection by flange (8), flue tube (10) in its bottom locates to utilize outer wall to be provided with flue shrouding (9) and buffler (11), with several in the horizontal direction the mozzle (16) of both-side opening (W) connect with buffler (11) by the waters that exceedes stream pond or control of dust water tank (VI), water inlet (K) end that wherein makes mozzle (16) is by bolt (17) or welding or build by laying bricks or stones to be fixed on and exceed on the inwall (18) that flows pond or control of dust water tank (VI), the other end is blocked by shrouding (12), promptly form a catheter type flow mixing device (IV) by buffler (11) and mozzle (16) and inwall (18) by body (III).In addition, the osculum (C) on the corresponding clarifier (I) is provided with drain tube (15) in body (III).
In use, the flue tube (10) of deduster body (III) is connected with the supplied flue gases pipeline, an amount of water of input in exceeding stream pond or control of dust water tank (VI).When operation, when decline is with buffler (11) formation space after flue gas is walked around buffler (11) upwards to erupt the water surface pressurized that makes its contact by flue (F) impact downwards, mozzle (16) will exceed the water in stream pond or the control of dust water tank (VI), at any time introduce in the body (III) and carry out comparatively fine and smooth mixed flow, thereby do not need to use water circulating pump and shower nozzle just can realize the mixed flow effect of flue gas and current from both-side opening (W) outflow and flue gas; Through the mixed flow water-dust mixture of eruption upwards, be subjected to the effect of flow distribution plate (4) to be subjected to the guide effect of centrifuge blade (7) crack (T) to form centrifugal motion again by aperture plate (13), and (B) rotation is risen between centrifuge blade (7) and louvre blade (6), therefrom make separated object and air carry out initial gross separation, because it is opposite with it that the guiding of louvre blade (6) crack (U) is set in centrifuge blade (7) periphery, flue gas between (B) impulsive force of rotation rising formation at a high speed can't be fled from flue gas itself from the crack (U) of louvre blade (6), opposite because the flue gas that rotation is risen by louvre blade (6) crack (U) to around the jet action that produces of cold air it is sucked in expansion chamber (A), being inhaled into a large amount of cold airs mixes with the steam that is inclusive with flue dust, make it to drop on the intercepter plate (5) very soon with the centrifugal motion that rotates ascending air after drop is formed in condensation with air separation, pass through last the returning of drain tube (19) inflow aperture plate (13) again and exceed stream pond or control of dust water tank (VI) by body (III) drain tube (15), and the air behind the process isolation of purified is subjected to the interior pressure effect of deduster body (III), and (A) continuation rising is discharged by discharge duct (1) in expansion chamber.
Promptly, can fundamentally remedy the deficiencies in the prior art, effectively improve the desulfurization dust-removing efficiency of deduster, reduce operating cost by the said goods structure provided by the invention and technical method.

Claims (4)

1, the invention provides a kind of flow-guiding condensing duster and technology thereof, it is characterized in that: below the deduster body, by body by buffler and mozzle and exceed stream pond or control of dust tank inner wall and be combined into a catheter type flow mixing device, when the water surface below the buffler is descended, mozzle by the catheter type flow mixing device, in the deduster body, import current from the waters that exceedes stream pond or control of dust water tank and realize the mixed flow effect of itself and flue dust, in addition, above the deduster body, be provided with the whirlwind suction-type condensation purifier of forming by expansion chamber and cyclone type inhalator, therefrom the guiding by cyclone type inhalator centrifuge blade is opposite with louvre blade, utilize the rotation of flue gas between to rise surrounding air is produced jet action, to mix with flue gas in a large amount of cold air suction expansion chambers, separate rapidly with air in centrifugal motion and make the steam that is inclusive with flue dust obtain forming drop after the condensation, promptly realize the purpose that it purifies air by condensation cleverly.
2, according to described a kind of flow-guiding condensing duster of claim 1 and technology thereof, involved catheter type flow mixing device (IV), be by body (III), combine by buffler (11) and mozzle (16) and inwall (18), mainly be with several in the horizontal direction the mozzle (16) of both-side opening (W) connect with buffler (11) by the waters that exceedes stream pond or control of dust water tank (VI), water inlet (K) end that wherein makes mozzle (16) is by bolt (17) or welding or build by laying bricks or stones to be fixed on and exceed on the inwall (18) that flows pond or control of dust water tank (VI), the other end is blocked by shrouding (12), to this, can be used for above the various forms of dedusters.
3, according to described a kind of flow-guiding condensing duster of claim 1 and technology thereof, involved whirlwind suction-type condensation purifier (I), be to combine by expansion chamber (V) and cyclone type inhalator (II), cyclone type inhalator (II) wherein, be by aperture plate (13) and be fixed with several centrifuge blades (7) near the edge-perpendicular of mesopore (D) in the above, on centrifuge blade (7), be fixed with flow distribution plate (4), and near the outward flange of aperture plate (13) vertical be fixed with several louvre blades (6), on louvre blade (6), be fixed with intercepter plate (5), on intercepter plate (5), face down drain tube (19) is installed, for the purpose that is able to suck surrounding air makes the guiding of centrifuge blade (7) opposite with the guiding of louvre blade (6), go for making separator and emission shunting, side in aperture plate (13) is shaped on hole (C) draining downwards, to this, not only can with expansion chamber (V) use that combines, also can be matched with chimney, flue, be that the cylindrical shell thing uses, in use, also inhalator can be together in series.
4, according to claim 1 and 2 and 3 described a kind of flow-guiding condensing duster and technology thereof, the anticorrosion liner plate (2) that uses in involved expansion chamber (I) and cyclone type inhalator (II) and the deduster body (III), aperture plate (13), centrifuge blade (7), louvre blade (6), intercepter plate (5), flow distribution plate (4), buffler (11), the i.e. material that contacts with smoke mixture, available safety glass or stone material or fiberglass or plastics or stainless steel material manufacturing, when making, can make deduster body (III) and whirlwind suction-type condensation purifier (I) and corresponding component change system into round with stainless steel material; During with safety glass or stone material or fiberglass or plastic material manufacturing, can make deduster body (III) and whirlwind suction-type condensation purifier (I) make many ribs type.
CN 01103982 2001-02-19 2001-02-19 Flow-guiding condensing duster and its technique Pending CN1302682A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 01103982 CN1302682A (en) 2001-02-19 2001-02-19 Flow-guiding condensing duster and its technique

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 01103982 CN1302682A (en) 2001-02-19 2001-02-19 Flow-guiding condensing duster and its technique

Publications (1)

Publication Number Publication Date
CN1302682A true CN1302682A (en) 2001-07-11

Family

ID=4653595

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 01103982 Pending CN1302682A (en) 2001-02-19 2001-02-19 Flow-guiding condensing duster and its technique

Country Status (1)

Country Link
CN (1) CN1302682A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101406804B (en) * 2008-09-09 2011-08-17 刘启杰 Purification treatment device for flue tail gas of fuel oil cremator
CN102614726A (en) * 2012-04-25 2012-08-01 李晓亮 Pressurized air dust collector
CN102012035B (en) * 2009-09-08 2014-11-26 上海超惠通风环保设备有限公司 method for producing ultrahigh large-caliber acid-resistant fiber glass reinforced plastic chimney
CN104162350A (en) * 2014-01-29 2014-11-26 樊后鹏 Haze origin greenhouse gas zero-discharge machine
CN104275082A (en) * 2014-01-29 2015-01-14 樊后鹏 Haze source greenhouse gas zero-emission machine
CN106823683A (en) * 2017-03-26 2017-06-13 从江县胜达活性炭有限公司 Exhaust treatment system in a kind of Activated Carbon Production
CN107051156A (en) * 2017-03-26 2017-08-18 从江县胜达活性炭有限公司 Exhaust gas processing device in a kind of Activated Carbon Production
CN116966679A (en) * 2023-08-29 2023-10-31 凯盛君恒(蚌埠)有限公司 Equipment and method for cooling and dedusting medium borosilicate glass production flue

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101406804B (en) * 2008-09-09 2011-08-17 刘启杰 Purification treatment device for flue tail gas of fuel oil cremator
CN102012035B (en) * 2009-09-08 2014-11-26 上海超惠通风环保设备有限公司 method for producing ultrahigh large-caliber acid-resistant fiber glass reinforced plastic chimney
CN102614726A (en) * 2012-04-25 2012-08-01 李晓亮 Pressurized air dust collector
CN104162350A (en) * 2014-01-29 2014-11-26 樊后鹏 Haze origin greenhouse gas zero-discharge machine
CN104275082A (en) * 2014-01-29 2015-01-14 樊后鹏 Haze source greenhouse gas zero-emission machine
CN104162350B (en) * 2014-01-29 2019-05-17 樊后鹏 Haze source greenhouse gases zero-emission machine
CN106823683A (en) * 2017-03-26 2017-06-13 从江县胜达活性炭有限公司 Exhaust treatment system in a kind of Activated Carbon Production
CN107051156A (en) * 2017-03-26 2017-08-18 从江县胜达活性炭有限公司 Exhaust gas processing device in a kind of Activated Carbon Production
CN116966679A (en) * 2023-08-29 2023-10-31 凯盛君恒(蚌埠)有限公司 Equipment and method for cooling and dedusting medium borosilicate glass production flue
CN116966679B (en) * 2023-08-29 2024-03-19 凯盛君恒(蚌埠)有限公司 Equipment and method for cooling and dedusting medium borosilicate glass production flue

Similar Documents

Publication Publication Date Title
CN106145228A (en) The two-part vaporising device of desulfurization wastewater and processing method thereof
CN100464824C (en) Oil fume secondary purifier
KR101140251B1 (en) Immersion Scrubber
CN1302682A (en) Flow-guiding condensing duster and its technique
CN109663449A (en) A kind of wet type inertial dust separator
CN106422600B (en) Condensing water dust scrubber
CN201684533U (en) Wet dust removal desulfurizing unit
CN104028068A (en) A multistage deduster
CN2383576Y (en) Venturi desulfurizing duster
CN2394703Y (en) Water spray and cyclone separating waste gas purifier
CN201055750Y (en) Secondary purifier fir oil smoke
CN201692760U (en) Gas-liquid swirling-flow desulfuration dust cleaner of efficient desulfuration dust-cleaning device
CN211328715U (en) Wet dust removal equipment
CN207153283U (en) Auto-excitation type device for eliminating smoke and dust based on venturi effect
CN203764062U (en) Multi-stage dust remover
US4880357A (en) Method and apparatus for producing high vacuum
CN101069799B (en) Frame-structure ripple ceramic wet-type cleaner
CN2273616Y (en) Wet type desulfurizing and dust removing equipment
CN201899957U (en) Variable-speed combined high-pressure spray type dust remover
CN2124057U (en) Coal burning flue gas purifier
CN2573896Y (en) Adjustable rotary jet cooling fume exhauster
CN218485545U (en) A high-efficient compound cyclone dust collector that sprays for fertilizer field of making
CN211612067U (en) Multi-stage humidifying tower
CN2464427Y (en) High-energy wet type dust remover
CN2159825Y (en) Auto exciting venturi tube duster

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