CN202470879U - Decontamination device of wastewater heat exchanger - Google Patents
Decontamination device of wastewater heat exchanger Download PDFInfo
- Publication number
- CN202470879U CN202470879U CN2012200909010U CN201220090901U CN202470879U CN 202470879 U CN202470879 U CN 202470879U CN 2012200909010 U CN2012200909010 U CN 2012200909010U CN 201220090901 U CN201220090901 U CN 201220090901U CN 202470879 U CN202470879 U CN 202470879U
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- Prior art keywords
- water
- dirt separator
- heat exchanger
- wastewater
- dirt
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Abstract
The utility model discloses a decontamination device of a wastewater heat exchanger, belonging to the technical field of energy utilization. A bypass pipeline at the wastewater inlet side of the water feeding end of a dirt separator of the device is communicated with a bypass pipeline at the wastewater inlet side of the water discharging end of the dirt separator, and a valve is arranged between the communicated pipelines; a bypass pipeline at the water discharging side of the water feeding end of the dirt separator is communicated with a bypass pipeline at the water discharging side of the water discharging end of the dirt separator, and a valve is arranged between the communicated pipelines; and a bypass pipeline in the middle of the water feeding end of the dirt separator is communicated with a bypass pipeline in the middle of the water discharging end of the dirt separator, and a water-water heat exchanger, a third filter and a valve are arranged on the communicated pipelines. By using the decontamination device, relevant pipelines can be switched through opening the valves; a washing ball is driven to reciprocate in a wastewater channel in a tube of the heat exchanger under the push of wastewater to run into a dirt layer on the inner wall of a friction tube, and thus, the dirt layer on the inner wall of the tube is removed, the dirt heat resistance of the heat exchanger is reduced, and furthermore, the heat exchanging performance of the wastewater heat exchanger is improved.
Description
Technical field
The utility model belongs to the energy utilization technology field, is specifically related to a kind of wastewater heat exchange device decontamination apparatus.
Background technology
Along with rapid economy development and growth in the living standard, domestic hot-water's energy consumption sharply increases.The sanitary wastewater temperature generally between 28～38 ℃, belongs to low-grade heat at present.Especially, barber shop, bath center sanitary wastewater discharge capacity are bigger, and concentrated relatively, and the waste heat that is wherein contained is easy to be recovered utilization.Because waste water includes a certain amount of mud, impurity, the inside pipe wall that is easy to stick to the wastewater heat exchange device forms certain thickness schmutzband.This has not only increased dirtiness resistance, but also has increased flow resistance.In general, after the wastewater heat exchange device used a period of time, its heat transfer property was significantly decayed, and its flow resistance significantly improves.Because there are some problems like this in the waste water water heater, make waste water residual heat recycle and be difficult to apply, cause a large amount of waste heats directly to be disposed in the environment and wasted.
This shows that the dirt that how to solve regularly, removes simply, efficiently the wastewater heat exchange device is the key that the waste water residual heat recovery and utilization technology is applied.
The utility model content
The utility model forms schmutzband easily to the inside pipe wall of present wastewater heat exchange device, and the problem that waste heat recovery is difficult proposes a kind of wastewater heat exchange device decontamination apparatus.
A kind of wastewater heat exchange device decontamination apparatus, on the dirt separator under the bypass line of the waste water inlet side of water end (W.E.) and the dirt separator bypass line of the waste water inlet side of water end (W.E.) be connected, and between connecting pipeline mounted valve; On the dirt separator under the bypass line of the following water side of water end (W.E.) and the dirt separator bypass line of the following water side of water end (W.E.) be connected, and between connecting pipeline mounted valve; On the dirt separator under the middle part bypass line of water end (W.E.) and the dirt separator middle part bypass line of water end (W.E.) be connected, and water hydro-thermal parallel operation WEX, the 3rd filter R are installed on connecting pipeline
3And valve.
The structure of water end (W.E.) is on the said dirt separator: the first filter R
1With the second filter R
2Between fill scrubbing ball CS, form scrubbing ball storage chamber V
b, scrubbing ball storage chamber V
bTwo ends are communicated with through annulus line, and valve is set.
Said water hydro-thermal parallel operation WEX is double pipe heat exchanger or shell and tube exchanger.
The said first filter R
1With the second filter R
2Mesh aperture less than 85% of scrubbing ball CS diameter.
The beneficial effect of the utility model: the wastewater heat exchange device decontamination apparatus of the utility model can pass through valve opening; The realization associated pipe is switched; Back and forth movement in the waste water tunnel that orders about under the promotion of waste water in the pipe of scrubbing ball at heat exchanger; The schmutzband of collision and friction tube inwall, thus remove the schmutzband on the inside pipe wall, reduce the heat exchanger dirtiness resistance to improve the heat exchange property of wastewater heat exchange device.This wastewater heat exchange device decontamination apparatus is that the waste water residual heat recovery is provided convenience, and improves the service life that waste water residual heat reclaims heat exchanger, for applying of waste water residual heat recovery provides technical support.
Description of drawings
Fig. 1 is that the wastewater heat exchange device decontamination apparatus of the utility model is formed and pipeline connects;
Fig. 2 is that the device of water end (W.E.) on the dirt separator of the utility model is formed and pipeline connects;
Fig. 3 is that the device of water end (W.E.) under the dirt separator of the utility model is formed and pipeline connects;
Among the figure, V
b-scrubbing ball storage chamber, R
1-the first filter, R
2-the second filter, R
3-Di three filters, WEX-water water-to-water heat exchanger, CS-scrubbing ball, V
1～V
5-valve.
The specific embodiment
Below in conjunction with accompanying drawing and specific embodiment the utility model is further specified.
Shown in Fig. 1-3; A kind of wastewater heat exchange device decontamination apparatus of present embodiment is become by water end (W.E.), water water-to-water heat exchanger WEX, connecting line, valve and other enclosure group under water end (W.E.), the dirt separator on the dirt separator; Connecting line in the said device is divided into water pipeline, waste water pipeline; Wherein, the water water-to-water heat exchanger is double pipe heat exchanger or shell and tube exchanger.Water end (W.E.) is by the first filter R on the dirt separator
1, the second filter R
2, scrubbing ball CS, scrubbing ball storage chamber V
b, connecting line, valve V
1, V
2And other enclosure group becomes; The scrubbing ball stores chamber V
bThe straight length both sides of influent waste water side the first filter R is installed respectively
1, the second filter R
2, another one outlet C-C is connected with the waste water entrance point of wastewater heat exchange device; Water end (W.E.) is by the 3rd filter R under the dirt separator
3, connecting line, valve V3, V4, V5 and other enclosure group become.
The waste water inlet tube of water end (W.E.) is connected with waste water incoming flow pipeline on the dirt separator, and its C-C pipeline opening is connected with the water intake of water water-to-water heat exchanger WEX; The E-E pipeline opening of the following water end (W.E.) of dirt separator is connected with the discharge of wastewater mouth of water water-to-water heat exchanger WEX; On the dirt separator under the bypass line of the waste water inlet side B-B of water end (W.E.) and the dirt separator bypass line of the waste water inlet side D-D of water end (W.E.) be connected; On the dirt separator under the bypass pipe of the following water side A-A of water end (W.E.) and the dirt separator bypass pipe of the following water side F-F of water end (W.E.) be connected.
When wastewater heat exchange device decontamination apparatus carries out scrubbing, generally need to start several times repeatedly.Its working procedure is divided into: forward washes away program and backward erosion program.Forward washes away the stage, need open valve V
2, V
4, valve-off V
1, V
3, V
5, sanitary wastewater is through valve V
2, filter R
2, impact scrubbing ball CS and get in the heat exchanger tube of water water-to-water heat exchanger WEX, the scrubbing ball CS of disturbance is in the motion state of chaotic, through with collision, the friction of inside pipe wall dirt, dirt is sneaked in the waste water, through filter R
3, valve V
4The pipeline at place directly discharges, because the 3rd filter R
3Mesh less than the diameter of scrubbing ball CS, therefore be trapped in the 3rd filter R
3The place, and dirt emits with waste water, thus realize the function of the inside pipe wall dirt of removal water water-to-water heat exchanger; In the backward erosion stage, need open valve V
3, V
5, valve-off V
1, V
4, V
2, sanitary wastewater is through valve V
3, the 3rd filter R
3, the impact forward washes away and accumulates in the 3rd filter R
3Scrubbing ball CS, get in the heat exchanger tube of water water-to-water heat exchanger WEX, the scrubbing ball CS of disturbance is in the motion state of chaotic, through with collision, the friction of inside pipe wall dirt, dirt is sneaked in the waste water, flow through, the scrubbing ball stores chamber V
b, the 3rd filter R
2, valve V
5Directly discharging is because the second filter R
2Mesh less than scrubbing ball CS diameter, therefore be trapped in filter R
2The scrubbing ball at place stores chamber V
b, and dirt emits with waste water, thus realize the function of the inside pipe wall dirt of removal water water-to-water heat exchanger.
Regularly adopt forward to wash away program and backward erosion program repeatedly; Can remove the dirt on the heat exchanger tube inwall of wastewater heat exchange device; Each scrubbing operation is all operated to guarantee that scrubbing ball CS is back to the scrubbing ball and stores chamber V as last scrubbing with the backward erosion program
bIn.
When water water-to-water heat exchanger WEX is in normal operating conditions, Open valve V
1, V
4, valve-off V
2, V
3, V
5, at this moment, sanitary wastewater is successively through valve V
1, filter R
1, get in the heat exchanger tube of water water-to-water heat exchanger WEX, and then through the 3rd filter R
3, valve V
4, be disposed to waste pipe.
Claims (4)
1. a wastewater heat exchange device decontamination apparatus is characterized in that, on the dirt separator under the bypass line of the waste water inlet side of water end (W.E.) and the dirt separator bypass line of the waste water inlet side of water end (W.E.) be connected, and between connecting pipeline mounted valve; On the dirt separator under the bypass line of the following water side of water end (W.E.) and the dirt separator bypass line of the following water side of water end (W.E.) be connected, and between connecting pipeline mounted valve; On the dirt separator under the middle part bypass line of water end (W.E.) and the dirt separator middle part bypass line of water end (W.E.) be connected, and on connecting pipeline, water hydro-thermal parallel operation (WEX), the 3rd filter (R are installed
3) and valve.
2. according to the said a kind of wastewater heat exchange device decontamination apparatus of claim 1, it is characterized in that the structure of water end (W.E.) is on the said dirt separator: the first filter (R
1) and the second filter (R
2) between fill scrubbing ball (CS), form scrubbing ball storage chamber (V
b), scrubbing ball storage chamber (V
b) two ends are communicated with through annulus line, and valve is set.
3. according to the said a kind of wastewater heat exchange device decontamination apparatus of claim 1, it is characterized in that said water hydro-thermal parallel operation (WEX) is double pipe heat exchanger or shell and tube exchanger.
4. according to the said a kind of wastewater heat exchange device decontamination apparatus of claim 1, it is characterized in that the said first filter (R
1) and the second filter (R
2) mesh aperture less than 85% of scrubbing ball (CS) diameter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200909010U CN202470879U (en) | 2012-03-12 | 2012-03-12 | Decontamination device of wastewater heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200909010U CN202470879U (en) | 2012-03-12 | 2012-03-12 | Decontamination device of wastewater heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202470879U true CN202470879U (en) | 2012-10-03 |
Family
ID=46919033
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012200909010U Withdrawn - After Issue CN202470879U (en) | 2012-03-12 | 2012-03-12 | Decontamination device of wastewater heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202470879U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102564214A (en) * | 2012-03-12 | 2012-07-11 | 北京建筑工程学院 | Decontamination system for wastewater heat exchanger |
| CN108097674A (en) * | 2017-11-21 | 2018-06-01 | 中国能源建设集团华东电力试验研究院有限公司 | 660MW supercritical pressure turbine debugging apparatus |
| CN110088464A (en) * | 2016-11-28 | 2019-08-02 | 水涡轮机有限公司 | Equipment for heating liquid |
-
2012
- 2012-03-12 CN CN2012200909010U patent/CN202470879U/en not_active Withdrawn - After Issue
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102564214A (en) * | 2012-03-12 | 2012-07-11 | 北京建筑工程学院 | Decontamination system for wastewater heat exchanger |
| CN102564214B (en) * | 2012-03-12 | 2013-10-16 | 北京建筑工程学院 | Decontamination system for wastewater heat exchanger |
| CN110088464A (en) * | 2016-11-28 | 2019-08-02 | 水涡轮机有限公司 | Equipment for heating liquid |
| CN108097674A (en) * | 2017-11-21 | 2018-06-01 | 中国能源建设集团华东电力试验研究院有限公司 | 660MW supercritical pressure turbine debugging apparatus |
| CN108097674B (en) * | 2017-11-21 | 2020-06-05 | 中国能源建设集团华东电力试验研究院有限公司 | 660MW supercritical steam turbine debugging device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20121003 Effective date of abandoning: 20131016 |
|
| RGAV | Abandon patent right to avoid regrant |