CN205099498U - High efficiency contains lime -ash water separator of micronic dust and lime -ash separation of water system thereof - Google Patents
High efficiency contains lime -ash water separator of micronic dust and lime -ash separation of water system thereof Download PDFInfo
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- CN205099498U CN205099498U CN201520874028.8U CN201520874028U CN205099498U CN 205099498 U CN205099498 U CN 205099498U CN 201520874028 U CN201520874028 U CN 201520874028U CN 205099498 U CN205099498 U CN 205099498U
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Abstract
The utility model relates to a high efficiency contains lime -ash water separator of micronic dust and lime -ash separation of water system thereof. Including the main jar of body, the main jar of body include and go up jar body group one -tenth by the lower jar body of taper shape with columniform, the bottom of the lower jar of body be provided with the export of outlet of sewer and first lime -ash, lower jar the body upper portion be provided with the lime -ash water inlet, jar top of the body of going up there is solution tank through the pipe connection, solution tank above be provided with clear water export, go up the inside from up divideing into the settling area and the district of packing down of jar body, the bottom of settling area be provided with album hawk and the export of second lime -ash, the central authorities of collection hawk be provided with the inlet tube, the bottom in filler district be provided with the filler backup pad, be provided with the inlet opening in the filler backup pad. The utility model discloses a high efficiency contains more than the lime -ash water separator's of micronic dust the purification efficiency 98%, retrieve clear water rate 90 -95%.
Description
Technical field
The utility model relates to a kind of solid-liquid separator, and especially a kind of high-level efficiency contains clinker water separator and the clinker water separation system thereof of micronic dust.
Background technology
In Industrial Boiler, in order to process the discharge of flue dust, generally adopting wet dedusting, a large amount of clinker waters containing micronic dust can be produced.The emission problem of clinker water becomes serious environmental problem day by day.The way of general process clinker water is multi stage precipitation method now, but this complex technical process, and structures floor space is large, and capital cost is high, and processing cost is also high.
Utility model content
The problems such as the utility model provides clinker water separator and the clinker water separation system thereof that a kind of high-level efficiency contains micronic dust, solves existing treatment complex technical process, and structures floor space is large, and capital cost is high, and processing cost is high;
For solving the problems of the technologies described above, the technical solution adopted in the utility model is:
A kind of high-level efficiency is containing the clinker water separator of micronic dust, comprise main tank body, described main tank body comprises and being made up of conical lower tank and columniform upper tank body, the bottom of described lower tank is provided with sewage outlet and the outlet of the first lime-ash, the top of described lower tank is provided with clinker water import, the top of described upper tank body is connected with filtered water tank by pipeline, clear water output is provided with above described filtered water tank, the inside of described upper tank body is divided into negative area and packing area from the bottom up, the bottom of described negative area is provided with collection hawk and the outlet of the second lime-ash, the central authorities of described collection hawk are provided with water inlet pipe, the bottom of described packing area is provided with packing support plate, packing support plate is provided with prosopyle.
Further, a kind of preferred version of the present utility model: be provided with backwash tube above described filtered water tank, described backwash tube is connected with filtered water tank by the top of Y-junction respectively at upper tank body, pipeline between connecting tee joint and filtered water tank is provided with the first valve, backwash tube is provided with the second valve.
Further, a kind of preferred version of the present utility model: described negative area is provided with visor.
Further, a kind of preferred version of the present utility model: described water inlet pipe is turbination.
The utility model also provides a kind of clinker water separation system, comprise sewage lagoon, the water-in of described sewage lagoon is connected with the ash slag waste water discharge outlet of boiler, the discharge of wastewater mouth of wet cleaner respectively, the water outlet of described sewage lagoon is connected by the clinker water import of sump pump with clinker water separator of the present utility model, and the clear water output of clinker water separator is connected with the water-in of wet cleaner.
The beneficial effects of the utility model:
High-level efficiency of the present utility model is containing the purification efficiency more than 98% of the clinker water separator of micronic dust; Reclaim clear water rate 90-95%, the closed cycle of non-wastewater discharge can be accomplished; Reclaim clear water containing concentration of suspension: be less than 50 mg/litre, much smaller than emission standard.
Accompanying drawing explanation
In order to be illustrated more clearly in the utility model embodiment or technical scheme of the prior art, be briefly described to the accompanying drawing used required in embodiment or description of the prior art below, apparently, accompanying drawing in the following describes is only 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.
Fig. 1 is the structural representation sketch of clinker water separator of the present utility model;
Fig. 2 is the structural representation sketch of clinker water separation system of the present utility model;
In figure, 1 is sewage outlet, and 2 is lower tank, and 3 is the second lime-ash outlet, 4 is visor, and 5 is packing area, and 6 is clear water output, and 7 is filtered water tank, 8 is the first valve, and 9 is Y-junction, and 10 is the second valve, and 11 is packing support plate, 12 is water inlet pipe, and 13 is collection hawk, and 14 is clinker water import, and 15 is the first lime-ash outlet, 16 is boiler, and 17 is wet cleaner, and 18 is blower fan, 19 is chimney, and 20 is water pump, and 21 is settling tank.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, be clearly and completely described the technical scheme in the utility model embodiment, obviously, described embodiment is only 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.
As shown in Figure 1, a kind of high-level efficiency is containing the clinker water separator of micronic dust, comprise main tank body, described main tank body comprises and being made up of conical lower tank 2 and columniform upper tank body, the bottom of described lower tank 2 is provided with sewage outlet 1 and the first lime-ash outlet 15, the top of described lower tank 2 is provided with clinker water import 14, the top of described upper tank body is connected with filtered water tank 7 by pipeline, described filtered water tank 7 is provided with clear water output 6 above, the inside of described upper tank body is divided into negative area and packing area 5 from the bottom up, the bottom of described negative area is provided with collection hawk 13 and the second lime-ash outlet 3, the central authorities of described collection hawk 13 are provided with water inlet pipe 12, the bottom of described packing area 5 is provided with packing support plate 11, packing support plate 11 is provided with prosopyle.
Preferably: described filtered water tank 7 is provided with backwash tube above, described backwash tube is connected with filtered water tank 7 by the top of Y-junction 9 respectively at upper tank body, pipeline between connecting tee joint 9 and filtered water tank 7 is provided with the first valve 8, backwash tube is provided with the second valve 10.By arranging counter-flushing pipeline, back flushing can be carried out to the filler of packing area 5 easily, improving the operation stability of system.
Preferably: described negative area is provided with visor 4.By arranging visor 4, the situation of negative area can be observed easily, facilitate adjust operation condition.
Preferably: described water inlet pipe 12 is turbination.Water inlet pipe 12 is turbination, makes into water slow, is conducive to the precipitation of micronic dust.Also can increase the traverse baffle of inclination in negative area, so that increase the distance of micronic dust precipitation, improve sedimentation effect.
As shown in Figure 2, a kind of clinker water separation system, comprise sewage lagoon, the water-in of described sewage lagoon is connected with the ash slag waste water discharge outlet of boiler 16, the discharge of wastewater mouth of wet cleaner 17 respectively, the water outlet of described sewage lagoon is connected with the clinker water import 14 of clinker water separator by sump pump 20, and the clear water output 6 of clinker water separator is connected with the water-in of wet cleaner 17.Also a grey slag bath can be increased, for depositing the lime-ash precipitated.
Operational process of the present utility model:
Flue gas inside chimney 19 enters wet cleaner 17 under the effect of blower fan 18, dust in removing flue gas, and boiler 16 produces clinker water that clinker water and wet cleaner 17 produce and enters settling tank 21 and carry out first time lime-ash and precipitate, the clinker water that settling tank is 21 li enters clinker water separator under the effect of water pump 20; The clinker water entering separator carries out centrifugation inside conical lower tank 2, removing macrobead micronic dust; Then clinker water enters negative area by obconic water inlet pipe 12, and under gravity, the micronic dust inside clinker water precipitates removing further; Then enter packing area 5, the micronic dust under the effect of filler inside final removing clinker water, obtains clear water; Clear water enters filtered water tank 7, and the clear water inside filtered water tank 7 enters wet cleaner 17 by pipeline, as its water source.Time equipment runs to certain, by the first lime-ash outlet 15 and the second lime-ash outlet 3, discharge lime-ash.Clinker water precipitates through four times, purification efficiency more than 98%; Reclaim clear water rate 90-95%, the closed cycle of non-wastewater discharge can be accomplished; Reclaim clear water containing concentration of suspension: be less than 50 mg/litre, much smaller than emission standard.
The clinker water that boiler generation clinker water and wet cleaner 17 produce in addition also without settling tank, can directly enter clinker water separator, carries out the isolation of purified of clinker water.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all within spirit of the present utility model and principle, any amendment done, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (5)
1. a high-level efficiency is containing the clinker water separator of micronic dust, it is characterized in that: comprise main tank body, described main tank body comprises and being made up of conical lower tank and columniform upper tank body, the bottom of described lower tank is provided with sewage outlet and the outlet of the first lime-ash, the top of described lower tank is provided with clinker water import, the top of described upper tank body is connected with filtered water tank by pipeline, clear water output is provided with above described filtered water tank, the inside of described upper tank body is divided into negative area and packing area from the bottom up, the bottom of described negative area is provided with collection hawk and the outlet of the second lime-ash, the central authorities of described collection hawk are provided with water inlet pipe, the bottom of described packing area is provided with packing support plate, packing support plate is provided with prosopyle.
2. high-level efficiency according to claim 1 is containing the clinker water separator of micronic dust, it is characterized in that: above described filtered water tank, be provided with backwash tube, described backwash tube is connected with filtered water tank by the top of Y-junction respectively at upper tank body, pipeline between connecting tee joint and filtered water tank is provided with the first valve, backwash tube is provided with the second valve.
3. high-level efficiency according to claim 1 is containing the clinker water separator of micronic dust, it is characterized in that: described negative area is provided with visor hole.
4. high-level efficiency according to claim 1 is containing the clinker water separator of micronic dust, it is characterized in that: described water inlet pipe is turbination.
5. a clinker water separation system, it is characterized in that: comprise sewage lagoon, the water-in of described sewage lagoon is connected with the ash slag waste water discharge outlet of boiler, the discharge of wastewater mouth of wet cleaner respectively, the water outlet of described sewage lagoon is connected by the clinker water import of the first sump pump with clinker water separator according to claim 1, and the clear water output of clinker water separator is connected with the water-in of wet cleaner.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520874028.8U CN205099498U (en) | 2015-11-05 | 2015-11-05 | High efficiency contains lime -ash water separator of micronic dust and lime -ash separation of water system thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520874028.8U CN205099498U (en) | 2015-11-05 | 2015-11-05 | High efficiency contains lime -ash water separator of micronic dust and lime -ash separation of water system thereof |
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| CN205099498U true CN205099498U (en) | 2016-03-23 |
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| CN201520874028.8U Active CN205099498U (en) | 2015-11-05 | 2015-11-05 | High efficiency contains lime -ash water separator of micronic dust and lime -ash separation of water system thereof |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108585141A (en) * | 2018-04-02 | 2018-09-28 | 宁波帝杨电子科技有限公司 | A kind of device that sewage disposal is carried out using quantitative alum of upper lower tank separation |
| CN108658187A (en) * | 2018-04-02 | 2018-10-16 | 宁波帝杨电子科技有限公司 | A kind of device that sewage disposal is carried out using alum of upper lower tank separation |
| CN108675414A (en) * | 2018-04-02 | 2018-10-19 | 宁波帝杨电子科技有限公司 | It is a kind of to carry out the device of sewage disposal by detaching upper tank body and lower tank |
-
2015
- 2015-11-05 CN CN201520874028.8U patent/CN205099498U/en active Active
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108585141A (en) * | 2018-04-02 | 2018-09-28 | 宁波帝杨电子科技有限公司 | A kind of device that sewage disposal is carried out using quantitative alum of upper lower tank separation |
| CN108658187A (en) * | 2018-04-02 | 2018-10-16 | 宁波帝杨电子科技有限公司 | A kind of device that sewage disposal is carried out using alum of upper lower tank separation |
| CN108675414A (en) * | 2018-04-02 | 2018-10-19 | 宁波帝杨电子科技有限公司 | It is a kind of to carry out the device of sewage disposal by detaching upper tank body and lower tank |
| CN108585141B (en) * | 2018-04-02 | 2021-03-09 | 张倩瑜 | Device for sewage treatment by quantitative alum by upper tank body and lower tank body |
| CN108658187B (en) * | 2018-04-02 | 2021-03-12 | 王玉涛 | Device for sewage treatment by alum by upper tank body and lower tank body |
| CN108675414B (en) * | 2018-04-02 | 2021-09-21 | 宁波帝杨电子科技有限公司 | Device for treating sewage through separating upper tank body and lower tank body |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Yunnan yanyuxuan Environmental Engineering Co.,Ltd. Assignor: YUNNAN WATER ENVIRONMENTAL ENGINEERING CO.,LTD. Contract record no.: X2023530000005 Denomination of utility model: High efficiency ash water separator containing micro dust and its ash water separation system Granted publication date: 20160323 License type: Common License Record date: 20230306 |