CN203238344U - Electroplate liquid evaporator of tinning unit - Google Patents
Electroplate liquid evaporator of tinning unit Download PDFInfo
- Publication number
- CN203238344U CN203238344U CN 201320121034 CN201320121034U CN203238344U CN 203238344 U CN203238344 U CN 203238344U CN 201320121034 CN201320121034 CN 201320121034 CN 201320121034 U CN201320121034 U CN 201320121034U CN 203238344 U CN203238344 U CN 203238344U
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- CN
- China
- Prior art keywords
- separation chamber
- steam
- electroplate liquid
- storage tank
- chamber
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 26
- 238000003860 storage Methods 0.000 claims abstract description 31
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 31
- 238000000926 separation method Methods 0.000 claims abstract description 26
- 239000012530 fluid Substances 0.000 claims description 9
- 239000006200 vaporizer Substances 0.000 claims description 8
- 238000010992 reflux Methods 0.000 claims description 7
- 238000013022 venting Methods 0.000 claims description 3
- 229910000831 Steel Inorganic materials 0.000 abstract description 4
- 239000010959 steel Substances 0.000 abstract description 4
- 238000005096 rolling process Methods 0.000 abstract description 2
- 238000007599 discharging Methods 0.000 abstract 3
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000010808 liquid waste Substances 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model belongs to the technical field of steel rolling devices, and particularly relates to an electroplate liquid evaporator of a tinning unit. The electroplate liquid evaporator comprises a storage tank with electroplate liquid, a heater, a separation chamber, a steam-water separation chamber and a condenser; an outlet of the storage tank is connected to an inlet of the heater through a supply pump, and an inlet of the storage tank is connected to an outlet of the heater through a backflow pump; the outlet of the heater is connected to an inlet of the separation chamber, a liquid discharging port on the bottom end of the separation chamber is connected to the heater, the top of an inner cavity of the separation chamber is provided with a filter net, a steam outlet on the top end of the separation chamber is connected to an inlet of the steam-water separation chamber, a liquid discharging port on the bottom end of the steam-water separation chamber is connected to the separation chamber, and a vent port of the steam-water separation chamber is connected to an inlet of the condenser; the electroplate liquid evaporator also comprises a water storage chamber, and an inlet of the water storage chamber is connected to the liquid discharging port on the bottom end of the condenser. The evaporator is reasonable in structure and can effectively condense the electroplate liquid of the tinning unit.
Description
Technical field
The utility model belongs to the steel rolling equipment technical field, relates in particular to a kind of zinc-plated unit electroplate liquid vaporizer.
Background technology
In the production process with steel, usually need to carry out surface treatment strengthening its performance to the band steel, as zinc-plated, zinc-plated etc.Electroplate liquid need to concentrate and could continue to use after the use of experience for some time.Owing to lacking vaporizer rational in infrastructure, undesirable to the concentrated effect of electroplate liquid in the existing zinc-plated unit, this caused electroplate liquid waste, promoted production cost.
The utility model content
The utility model provides a kind of vaporizer that zinc-plated unit electroplate liquid is effectively concentrated for solving the technical problem that exists in the known technology.
The technical scheme that the utility model is taked for the technical problem that exists in the solution known technology is: zinc-plated unit electroplate liquid vaporizer comprises storage tank, well heater, separate chamber, steam-water separation chamber and the condenser that has electroplate liquid; The outlet of described storage tank is connected to the entrance of described well heater by supply pump, the entrance of described storage tank is connected to the outlet of described well heater by reflux pump; The outlet of described well heater is connected to the entrance of described separate chamber, the leakage fluid dram of bottom, described separate chamber is connected to described well heater, top at described separate chamber inner chamber is provided with filter screen, the steam outlet on top, described separate chamber is connected to the entrance of described steam-water separation chamber, the leakage fluid dram of described steam-water separation chamber bottom is connected to described separate chamber, and the venting port of described steam-water separation chamber is connected to the entrance of described condenser; Also comprise water storage room, its entrance is connected to the leakage fluid dram of described condenser bottom.
Advantage of the present utility model and positively effect are: owing to having adopted above-mentioned design, the utility model is rational in infrastructure.Electroplate liquid supplies at a high speed well heater through supply pump, by well heater intensification evaporation, the mixing steam that forms is separated in the separate chamber, filter screen is held back the effective constituent in the electroplate liquid, concentrated solution dependence self gravitation is back to heater base downwards and further is back in the storage tank again, water vapor after the separation experiences successively steam-water separation chamber and condenser forms liquid water again, and concentrated effect is good.
Preferably: described storage tank is two, comprises 1# storage tank and 2# storage tank, and described supply pump is connected to simultaneously both outlets, described reflux pump and is connected to simultaneously both entrances.
Preferably: also comprise surge tank and the vacuum pump that is attached thereto, described surge tank is connected to described condenser.
Description of drawings
Fig. 1 is structural representation of the present utility model.
Among the figure: 1, filter screen; 2, separate chamber; 3, well heater; 4, reflux pump; 5, supply pump; 6,2# storage tank; 7,1# storage tank; 8, steam-water separation chamber; 9, condenser; 10, surge tank; 11, water storage room; 12, vacuum pump.
Embodiment
For further understanding summary of the invention of the present utility model, Characteristic, hereby exemplify following examples and be described in detail as follows:
See also Fig. 1, the utility model comprises storage tank, well heater 3, separate chamber 2, steam-water separation chamber 8 and the condenser 9 that has electroplate liquid.
The outlet of storage tank is connected to the entrance of well heater 3 by supply pump 5, the entrance of storage tank is connected to the outlet of well heater 3 by reflux pump 4.In this example, storage tank is two, comprises 1# storage tank 7 and 2# storage tank 6, and supply pump 5 is connected to both outlets, the entrance that reflux pump 4 is connected to both simultaneously simultaneously.Well heater 3 adopts the form of high-temperature steam heating to heat.
The outlet of well heater 3 is connected to the entrance of separate chamber 2, and the leakage fluid dram of 2 bottoms, separate chamber is connected to well heater 3, and the top of 2 inner chambers is provided with filter screen 1 in the separate chamber.
The steam outlet on 2 tops, separate chamber is connected to the entrance of steam-water separation chamber 8, and the leakage fluid dram of steam-water separation chamber 8 bottoms is connected to separate chamber 2, and liquid water is refluxed.The venting port of steam-water separation chamber 8 is connected to the entrance of condenser 9.
Also comprise water storage room 11, its entrance is connected to the leakage fluid dram of condenser 9 bottoms.After water vapor was liquefied, the liquid water of formation was temporary in water storage room 11.
In this example, also comprise surge tank 10 and the vacuum pump 12 that is attached thereto, surge tank 11 is connected to condenser 9.Vacuum pump 12 makes in the surge tank 10 and keeps negative pressure state, and the steam that is more conducive in the steam-water separation chamber 8 enters in the condenser 9.
Claims (3)
1. a zinc-plated unit electroplate liquid vaporizer is characterized in that: comprise the storage tank, well heater (3), separate chamber (2), steam-water separation chamber (8) and the condenser (9) that there are electroplate liquid; The outlet of described storage tank is connected to the entrance of described well heater (3) by supply pump (5), the entrance of described storage tank is connected to the outlet of described well heater (3) by reflux pump (4); The outlet of described well heater (3) is connected to the entrance of described separate chamber (2), the leakage fluid dram of bottom, described separate chamber (2) is connected to described well heater (3), top at described separate chamber (2) inner chamber is provided with filter screen (1), the steam outlet on top, described separate chamber (2) is connected to the entrance of described steam-water separation chamber (8), the leakage fluid dram of described steam-water separation chamber (8) bottom is connected to described separate chamber (2), and the venting port of described steam-water separation chamber (8) is connected to the entrance of described condenser (9); Also comprise water storage room (11), its entrance is connected to the leakage fluid dram of described condenser (9) bottom.
2. according to zinc-plated unit electroplate liquid vaporizer claimed in claim 1, it is characterized in that: described storage tank is two, comprise 1# storage tank (7) and 2# storage tank (6), described supply pump (5) is connected to simultaneously both outlets, described reflux pump (4) and is connected to simultaneously both entrances.
3. according to zinc-plated unit electroplate liquid vaporizer claimed in claim 1, it is characterized in that: the vacuum pump (12) that also comprises surge tank (10) and be attached thereto, described surge tank (10) is connected to described condenser (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320121034 CN203238344U (en) | 2013-03-18 | 2013-03-18 | Electroplate liquid evaporator of tinning unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320121034 CN203238344U (en) | 2013-03-18 | 2013-03-18 | Electroplate liquid evaporator of tinning unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203238344U true CN203238344U (en) | 2013-10-16 |
Family
ID=49315660
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320121034 Expired - Fee Related CN203238344U (en) | 2013-03-18 | 2013-03-18 | Electroplate liquid evaporator of tinning unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203238344U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106139622A (en) * | 2015-03-31 | 2016-11-23 | 北京东华原医疗设备有限责任公司 | Liquid vacuum enrichment facility and method for concentration thereof |
| CN110512270A (en) * | 2019-10-08 | 2019-11-29 | 常德威尔博金属表面处理有限责任公司 | A kind of plating pollution emission reduction device |
-
2013
- 2013-03-18 CN CN 201320121034 patent/CN203238344U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106139622A (en) * | 2015-03-31 | 2016-11-23 | 北京东华原医疗设备有限责任公司 | Liquid vacuum enrichment facility and method for concentration thereof |
| CN106139622B (en) * | 2015-03-31 | 2018-01-30 | 北京东华原医疗设备有限责任公司 | Liquid vacuum enrichment facility and its method for concentration |
| CN110512270A (en) * | 2019-10-08 | 2019-11-29 | 常德威尔博金属表面处理有限责任公司 | A kind of plating pollution emission reduction device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20131016 Termination date: 20150318 |
|
| EXPY | Termination of patent right or utility model |