CN204182256U - A kind of washing degree of depth dust arrester - Google Patents

A kind of washing degree of depth dust arrester Download PDF

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Publication number
CN204182256U
CN204182256U CN201420589259.XU CN201420589259U CN204182256U CN 204182256 U CN204182256 U CN 204182256U CN 201420589259 U CN201420589259 U CN 201420589259U CN 204182256 U CN204182256 U CN 204182256U
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CN
China
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washing
water
flue
dedust
flushing
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CN201420589259.XU
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Chinese (zh)
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陈鸥
陈建
陈振宇
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北京国电龙源环保工程有限公司
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Abstract

The utility model discloses a kind of washing degree of depth dust arrester, mainly comprise washing section flue, circulating water pool, washing spraying layer, water washing dedust circulating pump, water washing dedust mist eliminator flushing water pump, absorption tower demisting device flush water pump, water washing dedust demister, the first Flushing nozzle and the second Flushing nozzle.Comprise packing layer, water washing dedust mist eliminator flushing water collecting device and process water in addition and supplement interface.Washing degree of depth dust arrester of the present utility model is arranged on the downstream of wet desulphurization absorption tower, can continue on the one hand to catch part dust, dust-laden drop can be made to be diluted on the other hand, last again by the droplet in water washing dedust demister seizure flue gas, the dust carrying amount in flue gas can be reduced, make flue gas obtain advanced treating.The utility model efficiently solves the technical barrier of exhaust gas dust even minimum discharge up to standard, can play certain desulfurized effect, considerably reduce cost of investment, save the area, and has higher layout Installation Flexibility.

Description

A kind of washing degree of depth dust arrester

Technical field

The utility model belongs to flue gas ash removal technical field, relates to a kind of dust arrester, is specifically related to a kind of washing degree of depth dust arrester being arranged on wet desulphurization device downstream.Washing degree of depth dust arrester of the present utility model can realize the object of flue gas being carried out to degree of depth washing.

Background technology

Along with the enhancing gradually of the day by day serious of problem of environmental pollution and people's environmental consciousness, countries in the world government, especially the Chinese government just progressively carries out strict coal-fired flue-gas discharge standard on fume emission.A large amount of flue gases that the enterprises such as thermal power plant produce, before eliminating air, need to carry out procedural flue gas desulfurization and dedusting process.The desulfuration processing method of flue gas often can be divided into dry method, semidry method, wet desulfurizing process.At present, most of thermal power plant adopts wet desulfurizing process to carry out the desulfurization process of flue gas.

Wet desulfurizing process, can be described as again lime/lime stone wet desulphurization (being called for short FGD) technique, after the supercharging of FGD blower fan, be cooled to about 100 DEG C by heat exchanger from the high-temperature flue gas of boiler of power plant air-introduced machine outlet to enter wet desulphurization absorption tower and carry out wet desulphurization, lime/lime stone slurries spray rising flue gas in wet desulphurization absorption tower, sulfur dioxide in flue gas is absorbed by slurries, at the bottom of the tower of wet desulphurization absorption tower, obtain by-produced gypsum, the flue gas being stripped of sulfur dioxide enters air after a large amount of steam that demister removes entrained with.

Flue gas, before entering air, except needs desulfurization process, generally also will carry out dedusting.Conventional dust collection method can be divided into electrostatic precipitation, bag-type dust, wet dedusting etc.At present, Coal-fired Power Plant in China smoke harnessing engineering great majority adopt electric cleaner and electric sack cleaner.

For reducing the dust content in fume emission, usually before air-introduced machine, be provided with deduster (electric precipitation or bag-type dust), but along with the raising day by day of discharge standard, and the wet desulphurization device after air-introduced machine can increase carrying of part gypsum and dissolving salt (lime/lime stone slurries), such that dust in final fume emission is up to standard certain difficulty.For solving final dust emission concentration problem, there is now following several solution:

(1) by increasing electric field quantity (or cloth bag progression), increase cryogenic technique (reduction flue-gas temperature, improve dust collection efficiency), the technology such as Mobile pole plate, make dust in the flue gas exported at deduster (electric precipitation or bag-type dust) reach very low concentration.

Utility model patent 201010228281.8 discloses the combined dust remover of a kind of electric precipitation and electric bag-type dust, comprise inlet gas flue, electric bag-type dust district and electric precipitation district, in electric bag-type dust district, be then furnished with 2 grades and 2 grades with overdraught guide valve and airflow-distribution board by front, described air-flow guide valves at different levels are arranged at an angle of 90 mutually.The utility model regulates the inlet air flow of deduster by air-flow guide valve and airflow-distribution board, thus make deduster not by the impact of dust granules, dust content, can in the electric field of high wind speed, all can Efficient Collection to all kinds of physicochemical property, fine solid particle particle.

Utility model patent 200910143945.8 discloses a kind of flue gas purification system and method thereof.Disclosed in this utility model, content comprises flue, chimney, and in described flue, order arranges nonaqueous dust cleaner, air-introduced machine, sparge pipe successively; It is described that chimney bottom is provided with liquid-jet device, top is provided with demister; Described nonaqueous dust cleaner is ceramic multicyclone dust collector.The method of gas cleaning is that flue gas is carried out dry method dust in flue, then carries out wet dedusting by the sparge pipe arranged in flue and to flue gas cool-down; Enter alkali droplet that chimney sprays by the liquid-jet device gas-liquid mixed that moved upward and realize desulfurization.Compared with prior art, the advantage of this utility model is, the idle space which utilizes flue realizes dedusting, desulfurization and fume exhaust integrated, for gas cleaning provide that a kind of structure is simple, acid-resistant anti-corrosion, the new technology that maintains easily.

Utility model patent 200510032204.4 discloses a kind of flue type dust removal and purification apparatus, comprise flue, at flue Inner Front End, shower is housed, shower there is nozzle, at the external water inlet pipe of shower, cleaning waste liquid outlet is had below flue Inner Front End, in flue, one group of ceramic honey comb adsorption tube is equipped with in rear end, at the front end of ceramic honey comb adsorption tube dress cleaning water pipe, wash water pipe is equipped with cleaning hose, cleaning hose opening is in the porch of ceramic honey comb adsorption tube, in flue, have absorption waste liquid outlet below rear end.Major advantage of the present utility model is the after-treatment achieving flue gas, can adsorb fine dusts after washing process in flue dust and not by the pernicious gas of alkali treatment.

Utility model patent 02114598.9 discloses a kind of equipment for dust-removing and sulfur-removing washed by atomized water in heat-engine plant, form primarily of speedup pump water scrubber, multipotency atomizing water scrubber and flue dust sewage water filtration tower three part, the dynamo-electric split of speedup washing pump of installing in speedup pump water scrubber, impeller meal side porous, multipotency atomizing water scrubber is provided with multiple helical duct and group's atomizer, and supportingly have resistance fast web plate group and multilayer tank, flue dust sewage water filtration tower middle and upper part is provided with double charcoal filtering layer, and row's coil is dried in supporting installation, bottom is provided with sewage water filtration storehouse.Major advantage of the present utility model is need not supporting tall and big chimney.

(2) increase wet electrical dust precipitator in wet desulphurization device downstream, this method also can make the final concentration of emission of dust in flue gas reach low-down level.

Utility model patent 201020537350.9 discloses a kind of water and covers formula dust-removing desulfurating apparatus.Disclosed in this utility model, content mainly comprises dedusting, blower fan and desulfurizer, described desulfurizer is flue gas and limewash reaction unit, flue gas or coal gas discharge system after water washing dedust and desulfurization, this water covers three kinds of structures that formula dust-removing desulfurating apparatus adopts malleation negative pressure coupling or negative pressure or malleation, and described malleation negative pressure coupling structure is dust arrester, connects successively with flange between blower fan and desulfurizer three; Described negative pressure structure is dust arrester, connect successively with flange between desulfurizer and blower fan three; Described positive laminated structure is blower fan, connects successively with flange between dust arrester and desulfurizer three.This utility model has the advantages such as structure is simple, making is easy, cost is low, floor space is little, flue-gas temperature effectively can be reduced in less than 50 degree, the pressure of final discharge flue gas is below one kPa, dust removing effects can reach more than 99 percent, lingemann blackness 0 grade, desulfuration efficiency reaches more than 95 percent.

For the method for above-mentioned two kinds of exhaust gas dust process, due to some odjective causes, adopt first method possibly cannot realize the low concentration standard of flue outlet dust, and wet desulphurization can increase a part of dust, and not all project adopts the method can qualified discharge.Although and adopt second method can play extraordinary dust removing effects, the method investment cost is high, and floor space is large.

Utility model content

The purpose of this utility model is the technical barrier solving exhaust gas dust even minimum discharge up to standard, provides a kind of washing degree of depth dust arrester.This device is arranged on the downstream of wet desulphurization device, can play certain desulfurized effect, can not cause the increase of secondary pollution and slurries carrying amount, can not cause negative effect, can work under any operating mode to the normal operation of wet desulphurization device; Significantly can reduce cost of investment, save the area.

For achieving the above object, the technical scheme that the utility model is taked is as follows:

A kind of washing degree of depth dust arrester, comprises the equipment such as washing section flue, circulating water pool, washing spraying layer, water washing dedust circulating pump, water washing dedust mist eliminator flushing water pump, absorption tower demisting device flush water pump, water washing dedust demister, the first Flushing nozzle and the second Flushing nozzle.Washing degree of depth dust arrester is arranged on the downstream of wet desulphurization absorption tower demister, flue gas enters washing section flue from wet desulphurization absorption tower outlet, flue gas is washed by shower water, solid content in adsorption of dust, dilution absorption wet desulphurization absorption tower outlet drop and salt content, eventually through clean emission flue gas after water washing dedust demister removal droplet.

The upstream of described washing section flue is connected with wet desulphurization absorption tower; Washing section flue is connected with circulating water pool, and circulating water pool is arranged in the bottom of washing section flue; Washing spraying layer and water washing dedust demister are arranged in the inside of washing section flue, and washing spraying layer is arranged on the top of circulating water pool, and water washing dedust demister is arranged on the downstream of washing section flue.

Described water washing dedust circulating pump, water washing dedust mist eliminator flushing water pump, absorption tower demisting device flush water pump are connected with circulating water pool respectively, wherein, water washing dedust circulating pump is connected with washing spraying layer by aqueduct, water washing dedust mist eliminator flushing water pump is connected with the first Flushing nozzle by aqueduct, and absorption tower demisting device flush water pump is connected with the second Flushing nozzle by aqueduct.

Described first Flushing nozzle is arranged in the inside of washing section flue, and adjacent with water washing dedust demister; Second Flushing nozzle is arranged in the inside of wet desulphurization absorption tower, and adjacent with wet desulphurization absorption tower demister.

As the further improvement of technical solutions of the utility model, described washing degree of depth dust arrester also comprises packing layer and water washing dedust mist eliminator flushing water collecting device; Wherein, described packing layer is arranged in the inside of washing section flue, and is positioned at the top of circulating water pool; Described water washing dedust mist eliminator flushing water collecting device comprises flushing water collection unit and flushing water pipe section, and flushing water collection unit is positioned at the below of water washing dedust demister, and flushing water collection unit is connected with circulating water pool by flushing water pipe section.

As the further improvement of technical solutions of the utility model, described washing degree of depth dust arrester also comprises process water and supplements interface, and process water supplements interface and is connected with circulating water pool, for supplementing process water to circulating water pool.

Preferred as technical solutions of the utility model, described washing section flue is a monoblock type flue, or be recycled pond and be spaced apart the first washing section flue and the second washing section flue, the first washing section flue is connected with the second washing section flue by the inner space of circulating water pool.

Preferred as technical solutions of the utility model, described washing section flue is a monoblock type flue, circulating water pool is connected with the middle part vertical section of washing section flue, and described packing layer is horizontally set on the inside of the middle part vertical section of the washing section flue between washing spraying layer and circulating water pool; Or circulating water pool is connected with the middle part horizontal segment of washing section flue, the washing section flue that described packing layer is vertically set on right oblique upper is inner, and packing layer is between washing spraying layer and the first Flushing nozzle.

Preferred as technical solutions of the utility model, described washing section flue is recycled pond and is spaced apart the first washing section flue and the second washing section flue, described packing layer and washing spraying layer are all arranged on the inside of the first washing section flue, and packing layer is horizontally set between washing spraying layer and circulating water pool; Or described packing layer is all arranged on the inside of the second washing section flue with washing spraying layer, packing layer is horizontally set between washing spraying layer and circulating water pool.

Preferred as technical solutions of the utility model, described water washing dedust demister level or be arranged vertically on the downstream of washing section flue.

Preferred as technical solutions of the utility model, the horizontally disposed downstream at washing section flue of described water washing dedust demister, the first Flushing nozzle is arranged in the below of water washing dedust demister.

Preferred as technical solutions of the utility model, described water washing dedust demister is arranged vertically on the downstream of washing section flue, and the first Flushing nozzle is arranged in the left side of water washing dedust demister.

Compared with prior art, the beneficial effect that the utility model produces is:

(1) in wet desulphurization absorption tower, flue gas is by slurry wash, and part dust can be removed, but simultaneously, because slurries are carried away by flue gas, therefore can increase part dust carrying amount.Washing degree of depth dust arrester of the present utility model is arranged on the downstream of wet desulphurization absorption tower, degree of depth dust removal process is carried out to the flue gas after wet desulphurization, can continue on the one hand to catch part dust, dust-laden drop can be made to be diluted on the other hand, last again by the droplet in water washing dedust demister seizure flue gas, the dust carrying amount in flue gas can be reduced, make flue gas obtain advanced treating.The utility model efficiently solves the technical barrier of exhaust gas dust even minimum discharge up to standard, achieves the clean emission of flue gas.

(2) washing section flue and circulating water pool have been carried out integrated design by the utility model, and the water washing dedust circulating pump, water washing dedust mist eliminator flushing water pump and the absorption tower demisting device flush water pump that are connected with circulating water pool are respectively set, the washing and spraying layer that can feed water respectively, water washing dedust demister and absorption tower demisting device circulation-supplied wash water.

(3) circulating water pool of the present utility model is also communicated with water washing dedust mist eliminator flushing water collecting device and process water supplements interface, wherein, supplements interface can supplement process water to circulating water pool by process water, and the water met in circulating water pool is sufficient; Water washing dedust mist eliminator flushing water collecting device rinses the water of water washing dedust demister for collecting, and is collected to circulating water pool, achieves recycling of process water.

(4) washing section Flue duct design pattern of the present utility model is various, and on the whole, can be monoblock type washing section flue, washing section flue be recycled pond and be spaced apart the first washing section flue and the second washing section flue.The utility model can select different washing section Flue duct design patterns according to specific circumstances, makes manufacture of the present utility model and assembling have more flexibility, goes for various working.

(5) washing degree of depth dust arrester of the present utility model, can determine whether to arrange packing layer according to actual dust removal requirement and spray flux size, packing layer can form moisture film, realizes water film dedusting function, improves dust removal effect.

(6) washing degree of depth dust arrester of the present utility model is arranged on the downstream of wet desulphurization absorption tower, can not impact the operation of wet desulfurization system, certain additional pollutant removal effect can be played, such as to sulfur dioxide, sulfur trioxide, there is certain removal effect.

(7) washing degree of depth dust arrester of the present utility model can be reduced investment outlay significantly, saves the area, and arranges to install to have higher flexibility.

Accompanying drawing explanation

Fig. 1 is the structural representation of the washing degree of depth dust arrester described by embodiment 1.

Fig. 2 is the structural representation of the washing degree of depth dust arrester described by embodiment 2.

Fig. 3 is the structural representation of the washing degree of depth dust arrester described by embodiment 3.

Fig. 4 is the structural representation of the washing degree of depth dust arrester described by embodiment 4.

Description of reference numerals: 1, washing section flue; 2, circulating water pool; 3, spraying layer is washed; 4, water washing dedust circulating pump; 5, water washing dedust mist eliminator flushing water pump; 6, absorption tower demisting device flush water pump; 7, water washing dedust demister; 8, the first Flushing nozzle; 9, the second Flushing nozzle; 10, packing layer; 11, water washing dedust mist eliminator flushing water collecting device; 12, flushing water collection unit; 13, flushing water pipe section; 14, the first washing section flue; 15, the second washing section flue; 16, absorption tower demisting device; 17, wet desulphurization absorption tower; 18, process water supplements interface.

Detailed description of the invention

For the ease of understanding the purpose of this utility model, technical scheme and beneficial effect thereof, now will be elaborated further the utility model in conjunction with the embodiments.

Embodiment 1:

The enterprises such as thermal power plant meet the standard limit of smog release day by day improved, need to reduce the dust content in flue gas, common way is, is provided with deduster (electric precipitation or bag-type dust) or installs Wet type electric dust-removing device in the downstream of wet desulphurization before air-introduced machine.The technological deficiency that prior art exists is the technical barrier being difficult to solve dust even minimum discharge up to standard, and the investment cost of existing apparatus or dust collecting process is high, and floor space is large.The present embodiment is for the problems referred to above, devise a novel washing degree of depth dust arrester, this device is arranged on the downstream of wet desulphurization absorption tower demister, flue gas enters washing section flue 1 from wet desulphurization absorption tower 17 entrance, flue gas is washed by shower water, adsorption of dust, dilution absorb wet desulphurization absorption tower 17 and export solid content in drop and salt content, after removing droplet eventually through water washing dedust demister 7, by the flue gas of cleaning through smoke stack emission to air.

The structure of the washing degree of depth dust arrester described in the present embodiment as shown in Figure 1, mainly comprises the equipment such as washing section flue 1, circulating water pool 2, washing spraying layer 3, water washing dedust circulating pump 4, water washing dedust mist eliminator flushing water pump 5, absorption tower demisting device flush water pump 6, water washing dedust demister 7, first Flushing nozzle 8 and the second Flushing nozzle 9.

Wherein, the upstream of described washing section flue 1 is connected with wet desulphurization absorption tower 17, specifically the communicated downstream of the upstream of washing section flue 1 and the absorption tower demisting device 16 of wet desulphurization absorption tower 17 inside.Washing section flue 1 is connected with circulating water pool 2, and circulating water pool 2 is arranged in the bottom of washing section flue 1.Washing spraying layer 3 and water washing dedust demister 7 are arranged in the inside of washing section flue 1, and washing spraying layer 3 is arranged on the top of circulating water pool 2, and water washing dedust demister 7 is arranged on the downstream of washing section flue 1.

Described water washing dedust circulating pump 4, water washing dedust mist eliminator flushing water pump 5, absorption tower demisting device flush water pump 6 are connected with circulating water pool 2 respectively.Wherein, water washing dedust circulating pump 4 is connected with washing spraying layer 3 by aqueduct, can carry out spray and provides and use water for water washing spray drenches layer 3 pairs of flue gas.Water washing dedust mist eliminator flushing water pump 5 is connected with the first Flushing nozzle 8 by aqueduct, and the first Flushing nozzle 8 is arranged in the inside of washing section flue, and the first Flushing nozzle 8 is for rinsing water washing dedust demister 7.Absorption tower demisting device flush water pump 6 is connected with the second Flushing nozzle 9 by aqueduct, second Flushing nozzle 9 is arranged in the inside of wet desulphurization absorption tower 17, second Flushing nozzle 9 is for rinsing absorption tower demisting device 16, specifically, the second Flushing nozzle 9 is arranged in the below of absorption tower demisting device 16.

As shown in Figure 1, the washing degree of depth dust arrester of the present embodiment, also comprises packing layer 10 and water washing dedust mist eliminator flushing water collecting device 11.It should be noted that, arranging of packing layer 10 is optional, and can determine whether to arrange packing layer 10 according to actual dust removal requirement and spray flux size, packing layer 10 can form moisture film, realizes water film dedusting function, improves dust removal effect.For the installation site of packing layer 10, packing layer 10 is arranged in the inside of washing section flue 1, and is positioned at the top of circulating water pool 2.

For realizing recycling of flushing water, the washing degree of depth dust arrester of the present embodiment is provided with water washing dedust mist eliminator flushing water collecting device 11.For convenience of description, water washing dedust mist eliminator flushing water collecting device 11 comprises the flushing water collection unit 12 and flushing water pipe section 13 that are connected, wherein, flushing water collection unit 12 is positioned at the below of water washing dedust demister, and the profile of flushing water collection unit 12 is funnel-form to collect flushing water as soon as possible; The bottom of flushing water collection unit 12 is communicated with flushing water pipe section 13, and flushing water pipe section 13 is connected with circulating water pool 2, and the flushing water that flushing water collection unit 12 is collected is collected to circulating water pool 2.

In order to supplement fresh process water to circulating water pool 2, ensure that circulating water pool 2 has enough process waters, the washing degree of depth dust arrester of the present embodiment also comprises process water and supplements interface 18.As shown in Figure 1, process water supplements interface 18 and is connected with circulating water pool 2, and is arranged on the side on circulating water pool 2 top.

It needs to be noted, the washing section flue 1 of the washing degree of depth dust arrester of the present embodiment is not designed to a monoblock type flue, but be recycled pond 2 and be partitioned into the first washing section flue 14 and the second washing section flue 15, first washing section flue 14 is connected with the second washing section flue 15 by the upper space of circulating water pool 2.

As shown in Figure 1, described packing layer 10 and washing spraying layer 3 are all arranged on the inside of the first washing section flue 14, and wherein, packing layer 10 is horizontally set on the inside of the first washing section flue 14 between washing spraying layer 3 and circulating water pool 2.Described first Flushing nozzle 8 and water washing dedust demister 7 are all arranged on the inside of the second washing section flue 15, and wherein, the first Flushing nozzle 8 is arranged on the left side of water washing dedust demister 7.

For farthest reducing the droplet concentration of exhanst gas outlet, water washing dedust demister 7 can according to actual conditions employing level or the inside being arranged vertically on the second washing section flue 15.As shown in Figure 1, described water washing dedust demister 7 is arranged vertically on the inside of the second washing section flue 15, and the first Flushing nozzle 8 is arranged in the left side of water washing dedust demister 7.

Washing degree of depth dust arrester described in the present embodiment is arranged on the downstream of the absorption tower demisting device 16 of wet desulphurization absorption tower 17 inside, and wherein, the second Flushing nozzle 9 is arranged in the below of absorption tower demisting device 16.Flue gas to be clean enters wet desulphurization absorption tower 17 by wet desulphurization absorption tower entrance, through wet desulphurization spraying layer washing flue gas, again after droplet removed by absorption tower demisting device 16, flue gas is entered the washing section flue 1 of the washing degree of depth dust arrester in downstream by wet desulphurization absorption tower 17.The first washing section flue 14 and the second washing section flue 15 is partitioned into because washing section flue 1 is recycled pond 2, flue gas first washs through the washing spraying layer 3 be arranged in the first washing section flue 14, water film dedusting is realized again through packing layer 10, water after washing flows in the circulating water pool 2 below the first washing section flue 14, the flue gas exported from packing layer 10 enters the second washing section flue 15 by the upper space of circulating water pool 2, droplet is removed eventually through water washing dedust demister 7, flue gas after desulfurization and dedusting flow to chimney, by the fume emission after cleaning in air.

Can draw from above-mentioned, the washing degree of depth dust arrester of the present embodiment is arranged on the downstream of wet desulphurization absorption tower 17, degree of depth dust removal process is carried out to the flue gas after wet desulphurization, can continue on the one hand to catch part dust, dust-laden drop can be made to be diluted on the other hand, the last droplet caught by water washing dedust demister 7 again in flue gas, can be reduced the dust carrying amount in flue gas, make flue gas obtain advanced treating.The present embodiment achieves recycling of process water, has certain removal effect, can reduce investment outlay significantly, save the area sulfur dioxide, sulfur trioxide.

Embodiment 2:

As shown in Figure 2, washing degree of depth dust arrester described in the present embodiment and embodiment 1 are substantially similar, and main composition equipment remains washing section flue 1, circulating water pool 2, washing spraying layer 3, water washing dedust circulating pump 4, water washing dedust mist eliminator flushing water pump 5, absorption tower demisting device flush water pump 6, water washing dedust demister 7, first Flushing nozzle 8 and the second Flushing nozzle 9 etc.In addition, Fig. 2 shows, and the washing degree of depth dust arrester described in the present embodiment also comprises process water and supplements interface 18, packing layer 10 and water washing dedust mist eliminator flushing water collecting device 11.

The difference part of the washing degree of depth dust arrester that the present embodiment and embodiment 1 describe is that described washing section flue 1 is a monoblock type flue.Circulating water pool 2 and washing section flue 1 are unitary design, and namely circulating water pool 2 is connected with the middle part vertical section of washing section flue 1.Described packing layer 10 is horizontally set on the inside of the middle part vertical section of the washing section flue 1 between washing spraying layer 3 and circulating water pool 2.

The washing degree of depth dust arrester of the present embodiment is still arranged on the downstream of wet desulphurization absorption tower 17, flue gas enters washing section flue 1 from wet desulphurization absorption tower 17, flue gas first washs through washing spraying layer 3, water film dedusting is realized again through packing layer 10, flue gas passes through at the superjacent air space of circulating water pool 2, the last droplet caught by water washing dedust demister 7 again in flue gas, the flue gas after desulfurization and dedusting flow to chimney, by the fume emission after cleaning in air.

The present embodiment can realize the beneficial effect described in embodiment 1, and the installation site relation of the component parts of the washing degree of depth dust arrester described in the present embodiment please refer to embodiment 1.

Embodiment 3:

Washing degree of depth dust arrester described in the present embodiment is another kind of preferred version of the present utility model, as shown in Figure 3, washing section flue 1, circulating water pool 2, washing spraying layer 3, water washing dedust circulating pump 4, water washing dedust mist eliminator flushing water pump 5, absorption tower demisting device flush water pump 6, water washing dedust demister 7, first Flushing nozzle 8 and the second Flushing nozzle 9 etc. are mainly comprised.In addition, Fig. 3 shows, and the washing degree of depth dust arrester described in the present embodiment also comprises process water and supplements interface 18, packing layer 10 and water washing dedust mist eliminator flushing water collecting device 11.

There is something in common in the design and implementation example 1 of the washing section flue 1 of the washing degree of depth dust arrester described in the present embodiment, namely washing section flue 1 is not a monoblock type flue, but be recycled pond 2 and be partitioned into the first washing section flue 14 and the second washing section flue 15, first washing section flue 14 is connected with the second washing section flue 15 by the upper space of circulating water pool 2.Be described packing layer 10 with the difference of embodiment 1 and wash the inside that spraying layer 3 is all arranged on the second washing section flue 15, wherein, packing layer 10 is horizontally set on the inside of the second washing section flue 15 washed between spraying layer 3 and circulating water pool 2.

The washing degree of depth dust arrester of the present embodiment is still arranged on the downstream of wet desulphurization absorption tower 17, flue gas enters washing section flue 1 from wet desulphurization absorption tower 17, the first washing section flue 14 and the second washing section flue 15 is partitioned into because washing section flue 1 is recycled pond 2, flue gas is introduced into the first washing section flue 14, superjacent air space through circulating water pool 2 inside enters the second washing section flue 15, first realize water film dedusting through packing layer 10, wash through washing spraying layer 3 again, the last droplet caught by water washing dedust demister 7 again in flue gas, flue gas after desulfurization and dedusting flow to chimney, by the fume emission after cleaning in air.

The present embodiment can realize the beneficial effect described in embodiment 1, and the installation site relation of the component parts of the washing degree of depth dust arrester described in the present embodiment please refer to embodiment 1.

Embodiment 4:

Washing degree of depth dust arrester described in the present embodiment is another kind of preferred version of the present utility model, as shown in Figure 4, washing section flue 1, circulating water pool 2, washing spraying layer 3, water washing dedust circulating pump 4, water washing dedust mist eliminator flushing water pump 5, absorption tower demisting device flush water pump 6, water washing dedust demister 7, first Flushing nozzle 8 and the second Flushing nozzle 9 etc. are mainly comprised.In addition, Fig. 4 shows, and the washing degree of depth dust arrester described in the present embodiment also comprises process water and supplements interface 18, packing layer 10 and water washing dedust mist eliminator flushing water collecting device 11.

The washing degree of depth dust arrester that the present embodiment and embodiment 2 describe also exists something in common, and namely described washing section flue 1 is a monoblock type flue.The middle part of washing section flue 1 and downstream part are one and are horizontal direction to arrange, and circulating water pool 2 is positioned at the middle part of washing section flue 1 and is in the below of washing section flue 1.The washing section flue 1 that described packing layer 10 is vertically set on right oblique upper is inner, and the washing section flue 1 that packing layer 10 is between washing spraying layer 3 and the first Flushing nozzle 8 is inner.Described washing spraying layer 3 is arranged on the superjacent air space of circulating water pool 2.

The washing degree of depth dust arrester of the present embodiment is still arranged on the downstream of wet desulphurization absorption tower 17, flue gas enters washing section flue 1 from wet desulphurization absorption tower 17, flue gas first washs through washing spraying layer 3, flue gas passes through at the superjacent air space of circulating water pool 2, water film dedusting is realized again through packing layer 10, the last droplet caught by water washing dedust demister 7 again in flue gas, the flue gas after desulfurization and dedusting flow to chimney, by the fume emission after cleaning in air.

The present embodiment can realize the beneficial effect described in embodiment 1, and the installation site relation of the component parts of the washing degree of depth dust arrester described in the present embodiment please refer to embodiment 1.

The utility model is done above in conjunction with the embodiments and further described, but the utility model is not limited to above-mentioned embodiment, in the ken that one skilled in the relevant art possesses, can also make a variety of changes under the prerequisite not departing from the utility model aim.

Claims (9)

1. a washing degree of depth dust arrester, it is characterized in that, comprise washing section flue, circulating water pool, washing spraying layer, water washing dedust circulating pump, water washing dedust mist eliminator flushing water pump, absorption tower demisting device flush water pump, water washing dedust demister, the first Flushing nozzle and the second Flushing nozzle;
The upstream of described washing section flue is connected with wet desulphurization absorption tower; Washing section flue is connected with circulating water pool, and circulating water pool is arranged in the bottom of washing section flue; Washing spraying layer and water washing dedust demister are arranged in the inside of washing section flue, and washing spraying layer is arranged on the top of circulating water pool, and water washing dedust demister is arranged on the downstream of washing section flue;
Described water washing dedust circulating pump, water washing dedust mist eliminator flushing water pump, absorption tower demisting device flush water pump are connected with circulating water pool respectively, wherein, water washing dedust circulating pump is connected with washing spraying layer by aqueduct, water washing dedust mist eliminator flushing water pump is connected with the first Flushing nozzle by aqueduct, and absorption tower demisting device flush water pump is connected with the second Flushing nozzle by aqueduct;
Described first Flushing nozzle is arranged in the inside of washing section flue, and adjacent with water washing dedust demister; Second Flushing nozzle is arranged in the inside of wet desulphurization absorption tower, and adjacent with wet desulphurization absorption tower demister.
2. washing degree of depth dust arrester according to claim 1, is characterized in that, also comprises packing layer and water washing dedust mist eliminator flushing water collecting device; Described packing layer is arranged in the inside of washing section flue, and is positioned at the top of circulating water pool; Described water washing dedust mist eliminator flushing water collecting device comprises flushing water collection unit and flushing water pipe section, and flushing water collection unit is positioned at the below of water washing dedust demister, and flushing water collection unit is connected with circulating water pool by flushing water pipe section.
3. washing degree of depth dust arrester according to claim 1 and 2, is characterized in that, also comprise process water and supplement interface, process water supplements interface and is connected with circulating water pool, for supplementing process water to circulating water pool.
4. washing degree of depth dust arrester according to claim 2, it is characterized in that, described washing section flue is a monoblock type flue, or be recycled pond and be spaced apart the first washing section flue and the second washing section flue, the first washing section flue is connected with the second washing section flue by the inner space of circulating water pool.
5. washing degree of depth dust arrester according to claim 4, it is characterized in that, described washing section flue is a monoblock type flue, circulating water pool is connected with the middle part vertical section of washing section flue, and described packing layer is horizontally set on the inside of the middle part vertical section of the washing section flue between washing spraying layer and circulating water pool; Or circulating water pool is connected with the middle part horizontal segment of washing section flue, the washing section flue that described packing layer is vertically set on right oblique upper is inner, and packing layer is between washing spraying layer and the first Flushing nozzle.
6. washing degree of depth dust arrester according to claim 4, it is characterized in that, described washing section flue is recycled pond and is spaced apart the first washing section flue and the second washing section flue, described packing layer and washing spraying layer are all arranged on the inside of the first washing section flue, and packing layer is horizontally set between washing spraying layer and circulating water pool; Or described packing layer is all arranged on the inside of the second washing section flue with washing spraying layer, packing layer is horizontally set between washing spraying layer and circulating water pool.
7. washing degree of depth dust arrester according to claim 3, is characterized in that, described water washing dedust demister level or be arranged vertically on the downstream of washing section flue.
8. washing degree of depth dust arrester according to claim 7, is characterized in that, the horizontally disposed downstream at washing section flue of described water washing dedust demister, the first Flushing nozzle is arranged in the below of water washing dedust demister.
9. washing degree of depth dust arrester according to claim 7, it is characterized in that, described water washing dedust demister is arranged vertically on the downstream of washing section flue, and the first Flushing nozzle is arranged in the left side of water washing dedust demister.
CN201420589259.XU 2014-10-13 2014-10-13 A kind of washing degree of depth dust arrester CN204182256U (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104258668A (en) * 2014-10-13 2015-01-07 北京国电龙源环保工程有限公司 Deep washing dust removal device
CN104722160A (en) * 2015-04-03 2015-06-24 永固工程技术(江苏)有限公司 Wet dust removal system and method
CN104984633A (en) * 2015-07-14 2015-10-21 北京国电龙源环保工程有限公司 Desulphurization and dust removal integrating flue gas purification device and method

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104258668A (en) * 2014-10-13 2015-01-07 北京国电龙源环保工程有限公司 Deep washing dust removal device
CN104258668B (en) * 2014-10-13 2016-04-06 北京国电龙源环保工程有限公司 A kind of washing degree of depth dust arrester
CN104722160A (en) * 2015-04-03 2015-06-24 永固工程技术(江苏)有限公司 Wet dust removal system and method
WO2016155196A1 (en) * 2015-04-03 2016-10-06 永固工程技术(江苏)有限公司 Wet dust removing system and dust removing method
CN104984633A (en) * 2015-07-14 2015-10-21 北京国电龙源环保工程有限公司 Desulphurization and dust removal integrating flue gas purification device and method

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