CN204485655U - Novel desulfurizing dust removing treatment system - Google Patents
Novel desulfurizing dust removing treatment system Download PDFInfo
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- CN204485655U CN204485655U CN201520146803.8U CN201520146803U CN204485655U CN 204485655 U CN204485655 U CN 204485655U CN 201520146803 U CN201520146803 U CN 201520146803U CN 204485655 U CN204485655 U CN 204485655U
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Abstract
The utility model discloses a kind of Novel desulfurizing dust removing treatment system, comprise granite duster, first stage precipitation tank, second-level settling pond, clear water reserviors and the secondary settlement barrel that is arranged in clear water reserviors and desulfuration recycle pump; Wherein, the delivery port of granite duster is communicated with first stage precipitation tank, second-level settling pond and clear water reserviors successively by connecting pipe; The water inlet of granite duster is communicated with the secondary settlement barrel in desulfuration recycle pump, clear water reserviors successively by connecting pipe; The connecting pipe of the suction inlet connection of desulfuration recycle pump stretches into the bottom of secondary settlement barrel, and the connecting pipe of the outlet of desulfuration recycle pump is communicated with the water inlet of granite duster; Secondary settlement barrel is positioned at the middle part of clear water reserviors, and the cylinder edge, top of secondary settlement barrel is positioned at below the horizontal plane of clear water reserviors.This Novel desulfurizing dust removing treatment system, scrubbing, removal of impurity more remarkable effect, can reduce the fault rate of desulfuration recycle pump effectively.
Description
Technical field
The utility model relates to desulfurization and dedusting treatment facility technical field, particularly relates to Novel desulfurizing dust removing treatment system.
Background technology
At present in heating industry field, the desulfurating dust-removing equipment utilizing granite duster to make coal-burning boiler is adopted widely.Granite duster of the prior art is the building block adopting lithotome fiber crops stone and be processed into, with the cylindrical shape cleaner of acidproof glue cement masonry.
Granite duster of the prior art, its operation principle is that the buck mist sprayed by spray system in granite duster mixes with flue gas, to reach the object of desulfurization.Spray system in granite duster of the prior art is after being pressurizeed by circulating pump, is sprayed and forms water smoke, make whole system be in recurrent state by nozzle.
But obviously, also there are some objective technological deficiencies in the granite duster of prior art and spray system really; In the granite duster and spray system structure of prior art, circulating water pool, after first stage precipitation tank, second-level settling pond precipitation, flows to clear water reserviors.Because sedimentation basin is natural sedimentation, have considerable tiny lime-ash in water and flow into clear water reserviors, make the water dregginess in clear water reserviors very high (namely dirt is very many), above-mentioned dirt normally will use desulfurization water pump (namely also known as desulfuration recycle pump) and have an impact, water pump is caused often to break down, cause the damage in impeller of desulfurization water pump serious, normally run to like this desulfurization water pump and bring a lot of unfavorable factor.Also add maintenance cost and operating cost to heating enterprise simultaneously.Because above-mentioned traditional granite duster and spray system widely use, so its economic loss brought can not be ignored, such as: one of each boiler room will be keeped in repair desulfurization water pump for several times for warm season, significantly add the operating cost of heating enterprise.
In sum, how to overcome the above-mentioned technological deficiency of granite duster of the prior art and spray system, reducing desulfuration recycle pump fault rate is those skilled in the art's technical problems urgently to be resolved hurrily.
Utility model content
The utility model provides a kind of Novel desulfurizing dust removing treatment system, in order to solve the problems of the technologies described above.
The utility model realizes by the following technical solutions:
The utility model provides a kind of Novel desulfurizing dust removing treatment system, comprises granite duster, first stage precipitation tank, second-level settling pond, clear water reserviors and the secondary settlement barrel that is arranged in described clear water reserviors and desulfuration recycle pump;
Wherein, the delivery port of described granite duster is communicated with described first stage precipitation tank, described second-level settling pond and described clear water reserviors successively by connecting pipe; The water inlet of described granite duster is communicated with the described secondary settlement barrel in described desulfuration recycle pump, described clear water reserviors successively by connecting pipe; The connecting pipe of the suction inlet connection of described desulfuration recycle pump stretches into the bottom of described secondary settlement barrel, and the connecting pipe of the outlet of described desulfuration recycle pump is communicated with the water inlet of described granite duster;
Described secondary settlement barrel is positioned at the middle part of described clear water reserviors, and the cylinder edge, top of described secondary settlement barrel is positioned at below the horizontal plane of described clear water reserviors.
Preferably, can embodiment as one, the top cylinder of described secondary settlement barrel is along 500mm position below the horizontal plane being positioned at described clear water reserviors all the time.
Preferably, can embodiment as one, in concrete structure, the delivery port of described granite duster is communicated with the water inlet of described first stage precipitation tank by first stage precipitation tank inlet channel; And the delivery port of described granite duster is positioned at the bottom of described granite duster, the water inlet of described first stage precipitation tank is positioned at the top of described first stage precipitation tank.
Preferably, can embodiment as one, the delivery port of described first stage precipitation tank is communicated with the water inlet of described second-level settling pond by second-level settling pond inlet channel; And the delivery port of described first stage precipitation tank is positioned at the bottom of described first stage precipitation tank, the water inlet of described second-level settling pond is positioned at the top of described second-level settling pond.
Preferably, can embodiment as one, the delivery port of described second-level settling pond is communicated with the water inlet of described clear water reserviors by three grades of sedimentation basin inlet channels; And the delivery port of described second-level settling pond is positioned at the bottom of described second-level settling pond, the water inlet of described clear water reserviors is positioned at the top of described clear water reserviors.
Preferably, can embodiment as one, the connecting pipe of the suction inlet connection of described desulfuration recycle pump stretches into the bottom of described secondary settlement barrel, and the connecting pipe of the outlet of described desulfuration recycle pump stretches into the water inlet of described granite duster as desulfuration spraying tube road;
Preferably, can embodiment as one, the delivery port place height of described granite duster is higher than the water inlet place height of described first stage precipitation tank; The delivery port place height of described first stage precipitation tank is higher than the water inlet place height of described second-level settling pond; And the delivery port place height of described second-level settling pond is higher than the water inlet place height of described clear water reserviors.
Preferably, can embodiment as one, the connecting pipe that the suction inlet of described desulfuration recycle pump is communicated with also is provided with check-valves.
Preferably, can embodiment as one, described clear water reserviors entirety is positioned at ground level with upper/lower positions.
Preferably, can embodiment as one, described Novel desulfurizing dust removing treatment system also comprises fluid level control device; Described fluid level control device is electrically connected with described desulfuration recycle pump; And the liquid-level switch on described fluid level control device is positioned at the fixing liquid level position of described clear water reserviors.
Compared with prior art, the advantage of the utility model embodiment is:
The utility model provides a kind of Novel desulfurizing dust removing treatment system, and the structure analyzing above-mentioned Novel desulfurizing dust removing treatment system is known: above-mentioned novel de-dust removing treatment system is primarily of granite duster, first stage precipitation tank, second-level settling pond, clear water reserviors, the composition such as secondary settlement barrel, desulfuration recycle pump be arranged in described clear water reserviors.Analyze the annexation of said system known with position relationship: the delivery port of granite duster is communicated with first stage precipitation tank, second-level settling pond and clear water reserviors (namely realizing said structure by three sections of connecting pipes to be connected) successively by connecting pipe, and the water inlet of granite duster is communicated with secondary settlement barrel with desulfuration recycle pump (it is interior that the connecting pipe that namely suction inlet of desulfuration recycle pump is communicated with stretches into secondary settlement barrel) successively by connecting pipe in addition; So, by granite duster, through spraying, the mixing water (delivery port namely through granite duster flows out) after desulfurization process still successively enters first stage precipitation tank, second-level settling pond carries out natural sedimentation, enters clear water reserviors subsequently; But the core modified node method of the relatively traditional desulfurization dust-removal system of Novel desulfurizing dust removing treatment system that the utility model provides is: the secondary settlement barrel that in clear water reserviors, water level place, middle part is arranged; The cylinder edge, top of this secondary settlement barrel is positioned at below the horizontal plane of clear water reserviors, higher than at the bottom of the pond of clear water reserviors at the bottom of the bottom cylinder of secondary settlement barrel; The clean water source that such secondary settlement barrel will be collected in the middle part of clear water reserviors.Namely the utility model mainly utilizes the density difference of impurity thing in water body to carry out sedimentation filtration in conjunction with the flow principles of its impurity thing, because the density of impurity thing various in water body is different, after the mixing water containing impurity enters clear water reserviors, the impurity thing that density ratio water is large sinks (bottom sinking to clear water reserviors after namely flowing downward) naturally, the impurity that density ratio water is little floats naturally (swimming on the clear water reserviors water surface after namely upwards flowing), but only have water source free from foreign meter just can flow into secondary settlement barrel, so desulfuration recycle pump can be allowed all the time to keep sucking pure clear water, thus reach the object reducing desulfuration recycle pump fault rate.
Accompanying drawing explanation
In order to be illustrated more clearly in the utility model detailed description of the invention or technical scheme of the prior art, be briefly described to the accompanying drawing used required in detailed description of the invention or description of the prior art below, apparently, accompanying drawing in the following describes is embodiments more of the present utility model, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
The structural representation of the Novel desulfurizing dust removing treatment system that Fig. 1 provides for the utility model embodiment;
The partial structurtes enlarged diagram of the Novel desulfurizing dust removing treatment system that Fig. 2 provides for the utility model embodiment in Fig. 1;
In figure:
First stage precipitation tank 1; Second-level settling pond 2; Clear water reserviors 3; Granite duster 4; Secondary settlement barrel 5; Desulfuration recycle pump 6; Fluid level control device 7; First stage precipitation tank inlet channel 8; Second-level settling pond inlet channel 9; Three grades of sedimentation basin inlet channels 10; Connecting pipe 11; Connecting pipe 12.
Detailed description of the invention
Be clearly and completely described the technical solution of the utility model below in conjunction with accompanying drawing, obviously, described embodiment is the utility model part embodiment, instead of whole embodiments.Based on the embodiment in the utility model, those of ordinary skill in the art are not making the every other embodiment obtained under creative work prerequisite, all belong to the scope of the utility model protection.
Also by reference to the accompanying drawings the utility model is described in further detail below by specific embodiment.
As shown in Figure 1, a kind of Novel desulfurizing dust removing treatment system that the utility model embodiment provides, comprises granite duster 4, first stage precipitation tank 1, second-level settling pond 2, clear water reserviors 3 and the secondary settlement barrel 5 be arranged in described clear water reserviors 3 and desulfuration recycle pump 6;
Wherein, the delivery port of described granite duster 4 is communicated with described first stage precipitation tank 1, described second-level settling pond 2 and described clear water reserviors 3 successively by connecting pipe; The water inlet of described granite duster 4 is communicated with the described secondary settlement barrel 5 in described desulfuration recycle pump 6, described clear water reserviors successively by connecting pipe; The connecting pipe of the suction inlet connection of described desulfuration recycle pump 6 stretches into the bottom of described secondary settlement barrel 5, and the connecting pipe of the outlet of described desulfuration recycle pump 6 is communicated with the water inlet of described granite duster 4;
Described secondary settlement barrel 5 is positioned at the middle part of described clear water reserviors 3, and the top cylinder of described secondary settlement barrel 5 is along (can see also partial enlargement structure illustrated in Figure 2) below the horizontal plane being positioned at described clear water reserviors 3.
It should be noted that, the top cylinder of secondary settlement barrel 5 can realize structural principle of the present utility model below the horizontal plane being positioned at clear water reserviors 3, but as a kind of scheme of optimum selecting, the top cylinder of secondary settlement barrel 5 is along 500mm position below the horizontal plane being positioned at clear water reserviors all the time; It should be noted that, show through large quantity research, when only having secondary settlement barrel and clear water reserviors to be in above-mentioned relative position, in the secondary settlement barrel sampled out, impurity is minimum, the purest, and therefore the position of above-mentioned secondary settlement barrel is a kind of preferred position.
The concrete framework analyzing above-mentioned novel de-dust removing treatment system is known: above-mentioned novel de-dust removing treatment system is primarily of granite duster 4 (namely main technique effect carries out the process of spray desulfurization and dedusting to coal combustion exhaust), first stage precipitation tank 1 (namely Main Function is natural sedimentation process), second-level settling pond 2 (namely acting as natural subsidence), clear water reserviors 3, be arranged on the secondary settlement barrel 5 in described clear water reserviors 3, desulfuration recycle pump 6 (namely infusion circulation power is provided), the compositions such as fluid level control device 7 (namely start and stop control being carried out to desulfuration recycle pump).Wherein, fluid level control device controls the start and stop of desulfuration recycle pump, remains that the liquid level liquid level of clear water reserviors is in a normal working water level.Analyze the annexation of said system known with position relationship: the delivery port of granite duster is communicated with first stage precipitation tank, second-level settling pond and clear water reserviors (namely realizing said structure by three sections of connecting pipes to be connected) successively by connecting pipe, the water inlet of granite duster is communicated with (i.e. the suction inlet of desulfuration recycle pump stretch into secondary settlement barrel interior) by connecting pipe with secondary settlement barrel with desulfuration recycle pump in addition; So, by granite duster, through spraying, the mixing water (delivery port namely through granite duster flows out) after desulfurization process still successively enters first stage precipitation tank, second-level settling pond carries out natural sedimentation, enters clear water reserviors subsequently; The core modified node method of the relatively traditional desulfurization dust-removal system of the Novel desulfurizing dust removing treatment system that the utility model provides is the secondary settlement barrel that in clear water reserviors, water level place, middle part is arranged; The top cylinder of this secondary settlement barrel is along (concrete secondary settlement barrel cylinder is along being located at below horizontal plane 500 millimeters of positions) below the horizontal plane being positioned at clear water reserviors; Secondary settlement barrel cylinder is along being located at horizontal plane with upper/lower positions, and desulphurization circulating mouth piece is arranged on a low inside and puts, to prevent from finding time.Suction inlet place is equipped with check-valves in addition, flows back in cylinder to avoid system water.
But the core modified node method of the relatively traditional desulfurization dust-removal system of Novel desulfurizing dust removing treatment system that the utility model provides is: the secondary settlement barrel that in clear water reserviors, water level place, middle part is arranged; The cylinder edge, top of this secondary settlement barrel is positioned at below the horizontal plane of clear water reserviors, higher than at the bottom of the pond of clear water reserviors at the bottom of the bottom cylinder of secondary settlement barrel; The clean water source that such secondary settlement barrel will be collected in the middle part of clear water reserviors.Namely the utility model mainly utilizes the density difference of impurity thing in water body to carry out sedimentation filtration in conjunction with the flow principles of its impurity thing, because the density of impurity thing various in water body is different, after the mixing water containing impurity enters clear water reserviors, the impurity thing that density ratio water is large sinks (bottom sinking to clear water reserviors after namely flowing downward) naturally, the impurity that density ratio water is little floats naturally (swimming on the clear water reserviors water surface after namely upwards flowing), but only have water source free from foreign meter just can flow into secondary settlement barrel, so desulfuration recycle pump can be allowed all the time to keep sucking pure clear water, thus reach the object reducing desulfuration recycle pump fault rate.
It should be noted that, the water source that above-mentioned desulfuration recycle pump sucks, by being neither less than the impurity thing of water containing density, is not also greater than the impurity thing of water containing density; But, why the Novel desulfurizing dust removing treatment system that the utility model embodiment provides adopts above-mentioned structural design, mainly find based on following research: after desulfurization process and one-level, secondary natural subsidence, the major impurity owner in mixing water will be exactly some particles or the organic matter that density is less than that some floating things of water and density is greater than water.Therefore, the Novel desulfurizing dust removing treatment system that the utility model embodiment provides, solid particle and floating impurity in water body are farthest separated, the scrubbing of above-mentioned Novel desulfurizing dust removing treatment system, removal of impurity more remarkable effect, modified node method is more outstanding, effectively can reduce the fault rate of desulfuration recycle pump.
Detailed description is once done to the concrete structure of the Novel desulfurizing dust removing treatment system that the utility model embodiment provides and its concrete technique effect below:
In concrete structure, three sections of connecting pipes that granite duster delivery port is communicated with successively are respectively: first stage precipitation tank inlet channel 8, second-level settling pond inlet channel 9, three grades of sedimentation basin inlet channels 10; The connecting pipe that granite duster water inlet is communicated with successively is: connecting pipe 11 and connecting pipe 12.
Concrete structure: the delivery port of described granite duster 4 is communicated with the water inlet of described first stage precipitation tank 1 by first stage precipitation tank inlet channel 8; And the delivery port of described granite duster 4 is positioned at the bottom of described granite duster 4, the water inlet of described first stage precipitation tank 1 is positioned at the top of described first stage precipitation tank 1.
The delivery port of described first stage precipitation tank 1 is communicated with the water inlet of described second-level settling pond 2 by second-level settling pond inlet channel 9; And the delivery port of described first stage precipitation tank 1 is positioned at the bottom of described first stage precipitation tank 1, the water inlet of described second-level settling pond 2 is positioned at the top of described second-level settling pond.
The delivery port of described second-level settling pond 2 is communicated with the water inlet of described clear water reserviors 3 by three grades of sedimentation basin inlet channels 10; And the delivery port of described second-level settling pond 2 is positioned at the bottom of described second-level settling pond 2, the water inlet of described clear water reserviors 3 is positioned at the top (namely the bottom of clear water reserviors water inlet is also provided with fluid level control device) of described clear water reserviors 3.
The connecting pipe 11 of the suction inlet connection of described desulfuration recycle pump 6 stretches into the bottom of described secondary settlement barrel 5, and the connecting pipe 12 of the outlet of described desulfuration recycle pump 6 stretches into the water inlet of described granite duster 4 as desulfuration spraying tube road; Described clear water reserviors 3 entirety is positioned at ground level B with upper/lower positions.
In addition, the delivery port place height of described granite duster 4 is higher than the water inlet place height of described first stage precipitation tank 1; The delivery port place height of described first stage precipitation tank 1 is higher than the water inlet place height of described second-level settling pond 2; And the delivery port place height of described second-level settling pond 2 is higher than the water inlet place height of described clear water reserviors 3.Wherein, it should be noted that, the horizontal plane in each sedimentation basin and clear water reserviors all illustrates its water surface site with numbering A in the accompanying drawings, and numbering B illustrates the height and position of ground level.So, the water exit position of the treatment pond of each upper level is all higher than the water inlet position of next stage, can ensure that mixing water enters in each pond naturally and carry out purification filtering process, finally the water source in secondary settlement barrel being transported in high-order granite duster by desulfuration recycle pump.
Preferably, can embodiment as one, the connecting pipe 11 that the suction inlet of described desulfuration recycle pump 6 is communicated with also is provided with check-valves (not shown).
It should be noted that, as the technology contents described in said structure, the suction inlet place of desulfuration recycle pump 6 is equipped with check-valves, secondary settlement barrel water source is caused to mix with the water source in other positions of clear water reserviors after avoiding water conservancy diversion, and then avoid water source in secondary settlement barrel muddy, and remain the clean of the water source of secondary settlement barrel.
Preferably, can embodiment as one, described Novel desulfurizing dust removing treatment system also comprises fluid level control device 7; Described fluid level control device 7 is electrically connected with described desulfuration recycle pump 6; And the liquid-level switch on described fluid level control device 7 is positioned at the fixing liquid level position of described clear water reserviors 3.
To sum up the concrete technology flow process of Novel desulfurizing dust removing treatment system that provides of the utility model embodiment is as follows: in granite duster structure, the water smoke of shower ejection mixes with flue gas, after completing desulfurization, naturally first stage precipitation tank is flow to, after first stage precipitation tank natural sedimentation, flow to second-level settling pond, then flow to clear water reserviors after secondary precipitation.When the water level of clear water reserviors rises to fixed horizontal plane, liquid-level switch floats, and controls desulphurization circulating pump startup.When desulphurization circulating pump startup draws water, the water of 500 millimeters of positions below clear water reserviors inner horizontal flows in secondary settlement barrel, then is pumped to granite duster shower atomization desulfurization by desulphurization circulating.So go round and begin again, the water that desulfuration recycle pump is taken out remains clean.
In sum, the Novel desulfurizing dust removing treatment system that the utility model embodiment provides, can pass through clear water reserviors secondary precipitation process, make the water of desulphurization circulating mouth piece remain clear state, thus reaches the object reducing desulfuration recycle pump fault rate.Compare the endless form of traditional desulphurization circulating system, because this technology reasonably make use of otherness and its principle at water body flow that different material exists density, degree of depth settlement treatment is carried out to water source in clear water reserviors, significantly can reduce desulfuration recycle pump fault rate and greatly reduce.Above-mentioned Novel desulfurizing dust removing treatment system, can effectively promote decontamination effect of settling, while reducing desulphurization circulating failure of pump, decrease equipment manufacturing cost and the operating cost of the whole circulatory system, the long-time normal runs continuously of whole desulfurization and dedusting treatment system can be ensured; Therefore, the Novel desulfurizing dust removing treatment system that the utility model embodiment provides decreases manufacturing enterprise and runs and maintenance cost, and actual production operation effectiveness highly significant, has good application value and economic worth.
Last it is noted that above each embodiment is only in order to illustrate the technical solution of the utility model, be not intended to limit; Although be described in detail the utility model with reference to foregoing embodiments, those of ordinary skill in the art is to be understood that: it still can be modified to the technical scheme described in foregoing embodiments, or carries out equivalent replacement to wherein some or all of technical characteristic; And these amendments or replacement, do not make the essence of appropriate technical solution depart from the scope of each embodiment technical scheme of the utility model.
Claims (10)
1. a Novel desulfurizing dust removing treatment system, is characterized in that,
The secondary settlement barrel comprising granite duster, first stage precipitation tank, second-level settling pond, clear water reserviors and be arranged in described clear water reserviors and desulfuration recycle pump;
Wherein, the delivery port of described granite duster is communicated with described first stage precipitation tank, described second-level settling pond and described clear water reserviors successively by connecting pipe; The water inlet of described granite duster is communicated with the described secondary settlement barrel in described desulfuration recycle pump, described clear water reserviors successively by connecting pipe; The connecting pipe of the suction inlet connection of described desulfuration recycle pump stretches into the bottom of described secondary settlement barrel, and the connecting pipe of the outlet of described desulfuration recycle pump is communicated with the water inlet of described granite duster;
Described secondary settlement barrel is positioned at the middle part of described clear water reserviors, and the cylinder edge, top of described secondary settlement barrel is positioned at below the horizontal plane of described clear water reserviors.
2. Novel desulfurizing dust removing treatment system as claimed in claim 1, is characterized in that,
The top cylinder of described secondary settlement barrel is along 500mm position below the horizontal plane being positioned at described clear water reserviors all the time.
3. Novel desulfurizing dust removing treatment system as claimed in claim 1, is characterized in that,
In concrete structure, the delivery port of described granite duster is communicated with the water inlet of described first stage precipitation tank by first stage precipitation tank inlet channel; And the delivery port of described granite duster is positioned at the bottom of described granite duster, the water inlet of described first stage precipitation tank is positioned at the top of described first stage precipitation tank.
4. Novel desulfurizing dust removing treatment system as claimed in claim 3, is characterized in that,
The delivery port of described first stage precipitation tank is communicated with the water inlet of described second-level settling pond by second-level settling pond inlet channel; And the delivery port of described first stage precipitation tank is positioned at the bottom of described first stage precipitation tank, the water inlet of described second-level settling pond is positioned at the top of described second-level settling pond.
5. Novel desulfurizing dust removing treatment system as claimed in claim 4, is characterized in that,
The delivery port of described second-level settling pond is communicated with the water inlet of described clear water reserviors by three grades of sedimentation basin inlet channels; And the delivery port of described second-level settling pond is positioned at the bottom of described second-level settling pond, the water inlet of described clear water reserviors is positioned at the top of described clear water reserviors.
6. Novel desulfurizing dust removing treatment system as claimed in claim 5, is characterized in that,
The connecting pipe of the suction inlet connection of described desulfuration recycle pump stretches into the bottom of described secondary settlement barrel, and the connecting pipe of the outlet of described desulfuration recycle pump stretches into the water inlet of described granite duster as desulfuration spraying tube road.
7. Novel desulfurizing dust removing treatment system as claimed in claim 6, is characterized in that,
The delivery port place height of described granite duster is higher than the water inlet place height of described first stage precipitation tank;
The delivery port place height of described first stage precipitation tank is higher than the water inlet place height of described second-level settling pond; And the delivery port place height of described second-level settling pond is higher than the water inlet place height of described clear water reserviors.
8. Novel desulfurizing dust removing treatment system as claimed in claim 1, is characterized in that,
Described clear water reserviors entirety is positioned at ground level with upper/lower positions.
9. Novel desulfurizing dust removing treatment system as claimed in claim 6, is characterized in that,
The connecting pipe of the suction inlet connection of described desulfuration recycle pump is also provided with check-valves.
10. Novel desulfurizing dust removing treatment system as claimed in claim 1, is characterized in that,
Described Novel desulfurizing dust removing treatment system also comprises fluid level control device; Described fluid level control device is electrically connected with described desulfuration recycle pump; And the liquid-level switch on described fluid level control device is positioned at the fixing liquid level position of described clear water reserviors.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520146803.8U CN204485655U (en) | 2015-03-16 | 2015-03-16 | Novel desulfurizing dust removing treatment system |
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| CN201520146803.8U CN204485655U (en) | 2015-03-16 | 2015-03-16 | Novel desulfurizing dust removing treatment system |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106955577A (en) * | 2017-05-15 | 2017-07-18 | 湖南源洁美环保科技有限公司 | A kind of Ecology woods flue gas desulfurization and dedusting all-in-one |
| CN112870898A (en) * | 2021-01-19 | 2021-06-01 | 佛山盆森建材有限公司 | High-efficient dust pelletizing system |
-
2015
- 2015-03-16 CN CN201520146803.8U patent/CN204485655U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106955577A (en) * | 2017-05-15 | 2017-07-18 | 湖南源洁美环保科技有限公司 | A kind of Ecology woods flue gas desulfurization and dedusting all-in-one |
| CN112870898A (en) * | 2021-01-19 | 2021-06-01 | 佛山盆森建材有限公司 | High-efficient dust pelletizing system |
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Granted publication date: 20150722 |