CN1544128A - Dual cycle pocked stone pagoda stack gas desulfurizing and dedusting apparatus - Google Patents
Dual cycle pocked stone pagoda stack gas desulfurizing and dedusting apparatus Download PDFInfo
- Publication number
- CN1544128A CN1544128A CNA2003101069608A CN200310106960A CN1544128A CN 1544128 A CN1544128 A CN 1544128A CN A2003101069608 A CNA2003101069608 A CN A2003101069608A CN 200310106960 A CN200310106960 A CN 200310106960A CN 1544128 A CN1544128 A CN 1544128A
- Authority
- CN
- China
- Prior art keywords
- dust
- alkali
- liquid distributor
- desulfurizing
- tower
- 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.)
- Granted
Links
Images
Landscapes
- Treating Waste Gases (AREA)
- Separation Of Particles Using Liquids (AREA)
Abstract
The invention is a double-circulating granite tower fume -desulfurizing and -dust cleaning device, including granite tower main body, solution distributor, dust-water circulating system and sedimentation tank. Its character: there is an annular wetting sprayer in the inlet channel of the granite tower; the solution distributor is composed of many pipes extending into the granite tower and uniformly distributed along the circumference on the granite tower main body and near the top; the top of the granite tower main body is also installed with a two-stage desulfurizing and dust-cleaning device. Its beneficial effect: adopting a double-circulating system, i.e. the dust-water and alkali liquor independently circulate, respectively, thus enhancing the alkali utilization ratio and making the desulfurizing and dust-cleaning course stable and the desulfurizing and dust-cleaning efficiency high. The two-stage desulfurizing circulation has high desulfurizing efficiency and plays a role in primary dehydrating, and the low-resistance demister on the top of the desulfurizing tower can thoroughly eliminate fine water drops in the fume, ensuring that the fume carries no water. Adopting solution distributing pipes to replace solution distributing tanks can use samller water quantity to form a uniform falling liquid film on the inner wall of the dust-cleaning tower, ensuring dust-cleaning efficiency and avoiding dust accumulating.
Description
Technical field
The present invention relates to the boiler desulfurization dedusting technology, particularly a kind of pair of circulation pocked stone pagoda desulfurating dust removing device for flue gas.
Background technology
Middle-size and small-size power plant and big-and-middle-sized Industrial Boiler flue gas desulfurization and dedusting are related to air quality and environmental protection in the zone, are closely related with the people's health.Often use a kind of gallet water curtain dust collector in this field prior art, it is made up of pocked stone pagoda main body, Venturi tube, cloth liquid bath, grey water circulation system and settling tank etc.This deduster has effect preferably to the removing of soot dust granule thing, but not good to desulfurized effect, and its some shortcoming of also existing has also influenced normal use and dust removing effects simultaneously.The first is when desulfurization and dedusting are carried out simultaneously, if liquid distributor can not continuous water feeding, or calcium ion concentration supersaturation crystallization causes and adheres at the equipment inwall that to produce ash stifled in the alkali lye; It two is scale formations, when adding the alkali operation, because device interior filler and device space are less, and resistive connection dirt ability, sweetening liq produces calcium sulfate and calcium carbonate crystal occluding device under the high-temperature flue gas effect, cause equipment normally not move.It three is because flue gas demister poor structure, makes fan belt water, can not effectively remove the drop in the flue gas.It four is owing to during pocked stone pagoda deduster generation immerge, also be easy to cause the cloth liquid bath to tilt, and causes cloth liquid to lose efficacy, and dust stratification and efficiency of dust collection decline problem occur.
Summary of the invention
The objective of the invention is in order to overcome the deficiencies in the prior art, and provide a kind of pair of circulation pocked stone pagoda desulfurating dust removing device for flue gas, this dust arrester is taked at gas approach place increase ring-type humidification atomizer, increase the secondary desulfation dust-extraction device in the exit, and improvement liquid distribution system and modes such as buck and alkali lye independent loops, improve efficiency of dust collection, increase the desulfurization defrosting function, and convenient the use keeped in repair.
The present invention be address the above problem the scheme that is adopted be the design a kind of pair of circulation pocked stone pagoda desulfurating dust removing device for flue gas.It comprises pocked stone pagoda main body, liquid distributor, grey water circulation system and settling tank.It is characterized in that said pocked stone pagoda main body near in the intake channel of bottom, is equipped with a ring-type humidification atomizer.Said liquid distributor be the pocked stone pagoda main body near the top be uniformly distributed with along the circumference a plurality of, stretch to the liquid distributor in the tower.Also be equipped with by the deflection plate demister of a plurality of shower nozzles, Venturi tube, bump plate washer, annular array and the secondary desulfation dust-extraction device that alkali liquor circulating system is formed at the top of said pocked stone pagoda main body.
The invention has the beneficial effects as follows: it is the difference independent loops of buck and alkali lye that (1) two circulation pocked stone pagoda desulfurating dust removing device for flue gas adopts binary cycle system, has improved the utilization rate of alkali, desulfurization and dedusting process stabilization, desulfurization dust-removing efficiency height.In the buck circulation, flue dust does not have the deposition blending of alkaline residue and alkali in settling tank, and flue dust is recycling.Because flue dust is being removed more than 95% in the tower down, so product purity height in the alkali cyclic process provides advantage for further recycling in alkali circulation.(2) allow to exist excessive alkali in the alkali cyclic process, the system buffer capacity is big, and desulfuration efficiency improves, and not with SO
2The variation of load and fluctuating, because pH value is stable, fouling and the obstruction of having avoided calcium sulfate supersaturation and fluctuation to cause.(3) because halide concentrates in the buck circulation, make that therefore the selection of material of alkali lye recycle column is more economical, thereby make the cost reduction.(4) in the secondary desulphurization circulating that increases, adopt low speed venturi+impingement baffles structure, make flue gas resistance low, the desulfuration efficiency height, and played the effect that one-level is dewatered, and the low-resistance demister on desulfurizing tower top can thoroughly be removed fine liquid particles in the flue gas, the assurance flue gas is not with water.(5) establish ring-type side jet mould blocking humidification materialization device on horizontal flue, fully add wet flue gas and make the flue dust granulation, side spray structure makes flue gas directly not wash away nozzle, and flue gas resistance is low, and nozzle does not does not wear and tear.And jet head sets employing modular construction, make easy to maintenance.(6) adopt liquid distributor to replace the cloth liquid bath, can utilize the less water yield to make the gas wash tower inwall form the liquid film of even decline, also overcome the pocked stone pagoda deduster because the cloth liquid bath failure phenomenon that immerge causes has guaranteed efficiency of dust collection and avoided fouling phenomenon.Liquid distributor is installed for the punching of tower wall, can install in system's running, dismantle, keeps in repair, and makes the operation maintenance convenient simple.The present invention can be used for the corollary equipment of newly constructed boiler room flue gas desulfurization and dedusting, and also can be used for old gallet water curtain dust collector increases the improvement project that desulfurizing function improves efficiency of dust collection.Particularly on old gallet water curtain dust collector desulfurization improvement project, adopt more economical and effective of this technology.
Be described in detail with reference to accompanying drawing below with reference to embodiments of the invention.
Description of drawings
The two circulation pocked stone pagoda desulfurating dust removing device for flue gas system schematic of Fig. 1;
Fig. 2 ring-type humidification atomizer schematic diagram;
Fig. 3 liquid distributor schematic diagram;
Fig. 4 Venturi tube and bump plate washer schematic diagram;
Fig. 5 demister schematic diagram.
The specific embodiment
Of the present invention pair of circulation pocked stone pagoda desulfurating dust removing device for flue gas includes: pocked stone pagoda main body, liquid distributor, grey water circulation system 12 and settling tank 11.Wherein: as shown in Figure 1, 2, the pocked stone pagoda main body is equipped with a ring-type humidification atomizer 1 near in the intake channel of bottom, and the shower nozzle 15 of this ring-type humidification atomizer is divided into two or more sets, every group relatively level be loaded on the sidewall of intake channel, the shower nozzle water outlet is vertical with flue gas flow direction.
Shown in Fig. 1,3, liquid distributor be the pocked stone pagoda main body near the top be uniformly distributed with along the circumference a plurality of, stretch to the liquid distributor 2 in the tower.Each liquid distributor all is loaded on Ta Bishang by the rubber ring sealing, and the liquid distributor center line faces toward the pocked stone pagoda center line, and downward-sloping.At the port of export of liquid distributor, also be connected with a fan-shaped prolate spout towards the tower wall.And the entrance point of each liquid distributor all is connected with grading ring pipe 3.Stifled for ease of fouling in the cleaning liquid distributor and ash, the liquid distributor center is inserted with a cleaning rod 16 that back-moving spring is arranged.
Shown in Fig. 1,4,5, also be equipped with by a plurality of shower nozzles 7, Venturi tube 4, bump plate washer 5, the deflection plate demister 6 of annular array and the secondary desulfation dust-extraction device that alkali liquor circulating system 9 is formed at the top of pocked stone pagoda main body.This device has one upper and lowerly to be the tank body 8 of open type.Be fixed with a supporting clapboard 13 by the bottom in the tank body, plate is provided with a plurality of circular holes, and correspondence is fixed the low speed Venturi tube that a flow velocity is a per second 15-20 rice on each hole, and above each Venturi tube, fixes a water conservancy diversion bump plate washer.Under the supporting clapboard corresponding Venturi tube position be provided with the resistance drop that communicates with alkali liquor pipe at 2 meter water columns with interior low-resistance shower nozzle.Also be coated with the coating that one deck is made up of waterglass and glass-cermic powder on the supporting clapboard surface.Also be fixed with an installing plate 17 by top in the tank body, also be provided with a plurality of circular holes on the plate, correspondence is fixed a top deflection plate 18 for the annular array of sealing demister on each hole.In the alkali liquor circulating system of this secondary desulfation dust-extraction device, alkali lye pumps into the low-resistance shower nozzle by alkali case 10 through alkali liquor pipe and alkali pump, sprays into the low speed Venturi tube, and the mixture of flue gas and alkali lye drop behind the bump plate washer is removed down, and liquid flows back to the alkali case by leakage fluid dram 14.According to the pH value that returns liquid, alkali, moisturizing can be mended to the alkali pond by mending the alkali mouth and the mouth of a river by system.The flue dust in the alkali case and the sediment of product enter settling tank 11 by scum pipe.
The present invention in use, flue gas at first enters ring-type humidification atomizer from import, as shown in Figure 2, adopts the spray of shower nozzle side to install, flue gas does not directly wash away shower nozzle, so shower nozzle do not wear and tear, and does not produce the stifled phenomenon of ash.6-8 jet head sets is contained in outside installation the on the template, easy accessibility, be both sides during work to spray, water smoke covers whole flue cross section, can be according to dust concentration and flue gas load, opening one group or several groups works simultaneously, flue gas flow rate is controlled at about 15m/s, liquid-gas ratio 0.5-0.8, and the flue gas humidification is long, the humidification effect is better than venturi, but flue gas resistance is well below the venturi flue resistance.In this process, flue gas is with after the water smoke of ejection mixes, and water droplet is quickened by flue gas, be cooled at the accelerator flue gas, in the flue gas flue dust and drop bump, cohesion, granulation.
The flue gas that is cooled off by humidification carries water smoke and tangentially enters king-tower, and rotation is upwards flowed, and under action of centrifugal force, flue dust in the flue gas and drop rush at inwall and be captured, and forms evenly continuous liquid falling film for guaranteeing inner wall of tower, this device employing liquid distributor structure.As shown in Figure 3, recirculated water is distributed to liquid distributor after entering the grading ring pipe, and the liquid distributor front end is that a fan-shaped prolate spout sprays to inwall, and the liquid of a plurality of liquid distributor combination ejections forms continuous liquid film and can cover inwall, forms continuous liquid falling film.Liquid distributor is installed for punching, and liquid distributor and tower cinclides seal with rubber ring, mount and dismount very convenient.The effective lucite pipe of liquid distributor and grading ring connects, and it is convenient to observe, can be manually or automatic block clearing.Liquid distributor cloth liquid measure can increase and reduce the liquid distributor outlet pressure according to variation, use occasion, the change overflow pipe height of dust concentration, thereby changes thickness of liquid film, is suitable for different dust concentrations.
Flue gas after the dedusting enters low speed Venturi tube 4 and mixes upwards mobile with the alkali lye of low-resistance shower nozzle 7 ejections, under the effect of bump plate washer 5, turn to mobile, flue gas fully contacts with alkali lye in this process, sulfur dioxide is absorbed by alkali lye, micronic dust in the flue gas is further purified and has been strengthened the desulfurization and dedusting effect, plays the effect of primary dewatering.Flue gas is up behind impingement baffles, and the drop in the flue gas converges on the dividing plate, flows back to the alkali pond by leakage fluid dram.Because dustiness is few in the flue gas, so product purity height is convenient to recycle.Supporting clapboard is then separated dedusting circulation and desulphurization circulating.
Flue gas after the desulfurization upwards flows into the low-resistance demister.As shown in Figure 5, flue gas changes the flow direction after entering demister, flows out from horizontal direction, and the drop in the flue gas is captured by deflection plate, along compiling under the flap vertical current.This structural change the mode of traditional demister horizontal layout, change cellular structure into, on unit are, increase the girth of dehydration flap, be convenient to install, overhaul more convenient, because it is more thorough that deflection plate is vertically installed dehydration, avoided the flue gas reentrainment, than Plane Installation permissible velocity of flow height, saved the space, facility compact.
In the water circulation, the buck that flows out from the king-tower bottom enters settling tank 11, the flue dust precipitation, and supernatant pumps into liquid distributor by water circulating pump and ring-type humidification atomizer recycles.In the alkali lye circulation, alkali lye pumps into the low-resistance shower nozzle by NaOH solution circulating pump and sprays into the low speed Venturi tube, and the liquid under the bump plate washer removes flows back to the alkali case by leakage fluid dram, and the flue dust in the alkali case and the sediment of product also enter settling tank by scum pipe.
Claims (8)
1 one kinds of two circulation pocked stone pagoda desulfurating dust removing device for flue gas comprise pocked stone pagoda main body, liquid distributor, grey water circulation system and settling tank, it is characterized in that said pocked stone pagoda main body near in the intake channel of bottom, is equipped with a ring-type humidification atomizer; Said liquid distributor be the pocked stone pagoda main body near the top be uniformly distributed with along the circumference a plurality of, stretch to the liquid distributor in the tower; Also be equipped with by the deflection plate demister of a plurality of shower nozzles, Venturi tube, bump plate washer, annular array and the secondary desulfation dust-extraction device that alkali liquor circulating system is formed at the top of said pocked stone pagoda main body.
2 according to the described dust arrester of claim 1, it is characterized in that the shower nozzle of said ring-type humidification atomizer is divided into two or more sets, and level is loaded on the sidewall of intake channel relatively, and is vertical with flue gas flow direction.
3 according to the described dust arrester of claim 1, it is characterized in that said liquid distributor is loaded on Ta Bishang by the rubber ring sealing, and the liquid distributor center line faces toward the pocked stone pagoda center line, and downward-sloping; At the port of export of liquid distributor, also be connected with a fan-shaped prolate spout towards the tower wall; And the entrance point of each liquid distributor all is connected with the grading ring pipe.
4 according to claim 1 or 3 described dust arresters, it is characterized in that said liquid distributor center is inserted with a cleaning rod that back-moving spring is arranged.
5 according to the described dust arrester of claim 1, it is characterized in that said secondary desulfation dust-extraction device has one upper and lowerly to be the tank body of open type; Be fixed with a supporting clapboard by the bottom in the said tank body, plate is provided with a plurality of circular holes, and correspondence is fixed a Venturi tube on each hole, and above each Venturi tube, fixes a water conservancy diversion bump plate washer; Corresponding Venturi tube position is provided with the shower nozzle that communicates with alkali liquor pipe under the said supporting clapboard; Also be fixed with an installing plate by top in the said tank body, also be provided with a plurality of circular holes on the plate, correspondence is fixed a top deflection plate for the annular array of sealing demister on each hole.
6 according to the described dust arrester of claim 5, it is characterized in that said Venturi tube is that flow velocity is the low speed Venturi tube of per second 15-20 rice.
7 according to the described dust arrester of claim 5, it is characterized in that said shower nozzle be resistance drop at 2 meter water columns with interior low-resistance shower nozzle.
8 according to claim 1 or 6,7 described dust arresters, it is characterized in that in the alkali liquor circulating system of said secondary desulfation dust-extraction device, alkali lye pumps into the low-resistance shower nozzle by the alkali case through alkali liquor pipe and alkali pump, spray into the low speed Venturi tube, flue gas is removed down with the mixture of seeing liquid drop behind the bump plate washer, liquid flows back to the alkali case via leakage fluid dram, and the flue dust in the alkali case and the sediment of product enter settling tank by scum pipe; Also be respectively equipped with on the said alkali case and mend alkali mouth and water supplement port.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200310106960 CN1242840C (en) | 2003-11-10 | 2003-11-10 | Dual cycle pocked stone pagoda stack gas desulfurizing and dedusting apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200310106960 CN1242840C (en) | 2003-11-10 | 2003-11-10 | Dual cycle pocked stone pagoda stack gas desulfurizing and dedusting apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1544128A true CN1544128A (en) | 2004-11-10 |
| CN1242840C CN1242840C (en) | 2006-02-22 |
Family
ID=34334300
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200310106960 Expired - Fee Related CN1242840C (en) | 2003-11-10 | 2003-11-10 | Dual cycle pocked stone pagoda stack gas desulfurizing and dedusting apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1242840C (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101732972B (en) * | 2010-01-27 | 2012-05-23 | 天津理工大学 | Dual-liquid level jet bubbling pipe |
| CN105879653A (en) * | 2014-12-12 | 2016-08-24 | 安徽盛运环保工程有限公司 | Impact material-returning type flue reactor |
| CN109731443A (en) * | 2019-03-18 | 2019-05-10 | 上海超高环保科技股份有限公司 | Administer the used oil spray equipment and preparation method thereof of volatile organic matter |
| CN109876575A (en) * | 2019-02-11 | 2019-06-14 | 深圳国技仪器有限公司 | Smoke filter and smoke flue gas sampling equipment |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101254398B (en) * | 2007-12-14 | 2010-06-09 | 天津理工大学 | Double circulation desulfurating dust removing device for flue gas |
| CN101716463B (en) * | 2010-01-05 | 2012-07-04 | 浙江大学 | Simultaneous removing device and method of various pollutants by electrocatalytical oxidation combining lime-gypsum method |
-
2003
- 2003-11-10 CN CN 200310106960 patent/CN1242840C/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101732972B (en) * | 2010-01-27 | 2012-05-23 | 天津理工大学 | Dual-liquid level jet bubbling pipe |
| CN105879653A (en) * | 2014-12-12 | 2016-08-24 | 安徽盛运环保工程有限公司 | Impact material-returning type flue reactor |
| CN109876575A (en) * | 2019-02-11 | 2019-06-14 | 深圳国技仪器有限公司 | Smoke filter and smoke flue gas sampling equipment |
| CN109876575B (en) * | 2019-02-11 | 2024-08-09 | 深圳国技仪器有限公司 | Smoke filter and smoke and dust sampling equipment |
| CN109731443A (en) * | 2019-03-18 | 2019-05-10 | 上海超高环保科技股份有限公司 | Administer the used oil spray equipment and preparation method thereof of volatile organic matter |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1242840C (en) | 2006-02-22 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101254398B (en) | Double circulation desulfurating dust removing device for flue gas | |
| CN208008493U (en) | A kind of equipment that flue residue heat is used for Waste Water From Fire Power Plant zero discharge treatment | |
| CN1242840C (en) | Dual cycle pocked stone pagoda stack gas desulfurizing and dedusting apparatus | |
| CN2843595Y (en) | Multi-stage spiral-plate leaf desulfurizing dust collector | |
| CN1259119C (en) | Doublestage desulfurizing and dedusting apparatus | |
| CN2838732Y (en) | Enhanced water bathing desulfurization dust cleaner | |
| CN103056045A (en) | Primary cyclone separator for gas purification, gas purification system, gas purification method and application thereof | |
| CN206435035U (en) | Desulfurizer | |
| CN202620874U (en) | Gypsum slurry discharge device utilizing open type filter and pit | |
| CN108310951A (en) | The micro- ultra-clean exhaust system of mist desulfurization and dedusting of integrated fume | |
| CN1158752A (en) | Multifunctional smoke purifier | |
| CN205007846U (en) | S -shaped bar bubble cap desulfurization gas wash tower structure of twining | |
| CN204447739U (en) | A kind of high-efficiency wet-desulfurizing and electric demist integrated apparatus | |
| CN208465601U (en) | A kind of desulfurizing tower | |
| CN209501311U (en) | A kind of desulfurizing tower for capableing of circulation flushing demister | |
| CN209188491U (en) | A kind of structure of fume desulfurating absorption tower | |
| CN2616280Y (en) | Efficient wet desulfurizing dust-removing apparatus | |
| CN2573053Y (en) | Cyclone spray plate flue gas purifying tower | |
| CN220715405U (en) | Desulfurizing device of flue gas acid making system | |
| CN2796810Y (en) | Compound wet type desulfur dust eliminating equipment | |
| CN2345851Y (en) | Wet-type high-efficiency desulfurizing dust-removing device | |
| CN108067089B (en) | A kind of method and apparatus producing NaHS | |
| CN205517205U (en) | Novel high -efficient desulfurization dust removal purification device | |
| CN110614017A (en) | Desulfurizing tower for flue gas desulfurization | |
| CN216125451U (en) | Washing tower for purifying flue gas |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20060222 Termination date: 20101110 |