CN205236515U - Drainage recycle's device is washed to aluminium alloy oxidation hot water - Google Patents
Drainage recycle's device is washed to aluminium alloy oxidation hot water Download PDFInfo
- Publication number
- CN205236515U CN205236515U CN201521005315.1U CN201521005315U CN205236515U CN 205236515 U CN205236515 U CN 205236515U CN 201521005315 U CN201521005315 U CN 201521005315U CN 205236515 U CN205236515 U CN 205236515U
- Authority
- CN
- China
- Prior art keywords
- water
- soup
- heat exchanger
- washed
- washing trough
- 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.)
- Active
Links
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model discloses a drainage recycle's device is washed to aluminium alloy oxidation hot water, including purified water tank, hot water washtrough, heat exchanger and sprayed tank, the heat exchanger is equipped with water inlet A, water inlet B, delivery port A and delivery port B, water inlet A and purified water tank intercommunication, delivery port A and water inlet B and hot water washtrough intercommunication, delivery port B and sprayed tank intercommunication. Adopt the utility model discloses, but the waste heat of make full use of hot water washtrough overflow water reduces the production energy consumption.
Description
Technical field
The utility model relates to a kind of thermocirculator, relates in particular to a kind of aluminium section bar oxidation soup and washes the device that draining is recycled.
Background technology
Washing is the important step of aluminium alloy extrusions pre-treatment, and object is to clean residual chemical substance or the dust impurity of upper one process product. And whether need heating, washing can be divided into normal temperature washing and hot water wash (being referred to as traditionally soup washes) by tank liquor. Soup washing trough is to water quality requirement high (electrical conductivity of water≤80 μ s/cm), must carry out stabilizing water quality do moisturizing with pure water, and temperature when pure water moisturizing is normal temperature, moisturizing can make soup washing trough temperature decline after soup washing trough, guarantee soup washing trough temperature in processing range (more than 80 DEG C) must be constantly to soup washing trough heat, thermal energy consumption is large.
Utility model content
Technical problem to be solved in the utility model is, provides a kind of aluminium section bar oxidation soup to wash the device that draining is recycled, and can make full use of the waste heat of soup washing trough overflow water, reduces energy consumption.
In order to solve the problems of the technologies described above, the utility model provides a kind of aluminium section bar oxidation soup to wash the device that draining is recycled, comprise pure water tank, soup washing trough, heat exchanger and sprayed tank, described heat exchanger is provided with water inlet A, water inlet B, water outlet A and water outlet B, described water inlet A is communicated with pure water tank, described water outlet A and water inlet B are communicated with soup washing trough, and described water outlet B is communicated with sprayed tank.
As the improvement of such scheme, described soup washing trough is provided with water supplement port and overfall, and described water supplement port is communicated with water outlet A, and described overfall is communicated with water inlet B.
As the improvement of such scheme, described water supplement port is located at the bottom of soup washing trough, and described overfall is located at the side wall upper part of soup washing trough.
As the improvement of such scheme, described heat exchanger is the one in plate type heat exchanger, jacketed type exchanger, double pipe heat exchanger and shell-and-tube heat exchanger.
As the improvement of such scheme, the outlet temperature of described outlet A is 60-70 DEG C.
As the improvement of such scheme, the outlet temperature of described outlet B is room temperature.
Implement the utility model, there is following beneficial effect:
The utility model is by setting up a heat exchanger, make high temperature overflow water and low temperature pure water heat-shift in heat exchanger, on the one hand can carry out heat temperature raising to the pure water that is about to enter soup washing trough, reduce low temperature pure water and enter the fluctuation that high lukewarm water washing trough causes the interior temperature of groove to cause, and be also reduced to the energy that keeps soup washing trough technological temperature and consume; On the other hand, the contained impurity of the overflow water of high temperature is few, can be used for the spray processing after alkali, but water temperature over-high is not suitable for directly spraying, and the utility model makes overflow water cooling after heat exchange, can directly be recycled.
Brief description of the drawings
Fig. 1 is the structural representation that a kind of aluminium section bar oxidation of the utility model soup is washed the device of draining recycling.
Detailed description of the invention
For making the purpose of this utility model, technical scheme and advantage clearer, below in conjunction with accompanying drawing, the utility model is described in further detail.
The pure water filling into due to existing soup washing trough is normal temperature, passes into the temperature that will inevitably reduce liquid in groove in soup washing trough, in order to keep technological temperature in groove within the scope of 80-85 DEG C, needs water temperature control device to continue soup washing trough heating, and energy resource consumption is large. But the object of scalder skill is to remove the residual chemical substance of aluminium shape surface or dust impurity, therefore require the water electric conductivity≤80 μ s/cm in soup wash pool, to guarantee that aluminium section bar cleans up. In order to keep the water quality in groove, scalder skill has adopted the mode of moisturizing and overflow combination to change trough inner water body, it is directly pure water to be inputed in soup washing trough that existing soup is washed equipment, when trough inner water position arrives gap, overflow and going out, but the temperature of overflow water arrives the technological temperature of 80-85 DEG C, directly discharges, waste heat energy, and be unfavorable for being recycled of high temperature overflow water.
For this reason, as shown in Figure 1, the utility model provides a kind of aluminium section bar oxidation soup to wash the device that draining is recycled, comprise pure water tank, soup washing trough, heat exchanger and sprayed tank, described heat exchanger is provided with water inlet A, water inlet B, water outlet A and water outlet B, described water inlet A is communicated with pure water tank, and described water outlet A and water inlet B are communicated with soup washing trough, and described water outlet B is communicated with sprayed tank.
Described soup washing trough is provided with water supplement port and overfall, and described water supplement port is communicated with water outlet A, and described overfall is communicated with water inlet B.
Pure water in described pure water tank is delivered to the water inlet A of heat exchanger by water pump, on the other hand, in soup washing trough groove, the overflow water of high temperature enters heat exchanger in overfall and water inlet B, high temperature overflow water and low temperature pure water heat-shift in heat exchanger, pure water is heated up, overflow water cooling, the pure water after finally heating up is realized moisturizing through water outlet A and the washing trough of water supplement port inflow soup, and the overflow water of cooling flows to sprayed tank from water outlet B, as the spray processing after alkali.
The utility model is by setting up a heat exchanger, make high temperature overflow water and low temperature pure water heat-shift in heat exchanger, on the one hand can carry out heat temperature raising to the pure water that is about to enter soup washing trough, reduce low temperature pure water and enter the fluctuation that high lukewarm water washing trough causes the interior temperature of groove to cause, and be also reduced to the energy that keeps soup washing trough technological temperature and consume; On the other hand, the contained impurity of the overflow water of high temperature is few, can be used for the spray processing after alkali, but water temperature over-high is not suitable for directly spraying, and the utility model makes overflow water cooling after heat exchange, can directly be recycled.
Preferably, described water supplement port is located at the bottom of soup washing trough, and described overfall is located at the side wall upper part of soup washing trough. Pure water enters from the water supplement port of soup washing trough bottom, and overflow water flows out from the groove face of soup washing trough, can make the water body in groove flow from bottom to up, and water body, all the time in changing mobile state, is guaranteed trough inner water matter quality.
It should be noted that, the selected heat exchanger of the utility model should be applicable to liquid-liquid heat exchange mode, and preferably, described heat exchanger is the one in plate type heat exchanger, jacketed type exchanger, double pipe heat exchanger and shell-and-tube heat exchanger. More preferably, described heat exchanger is plate type heat exchanger.
Preferably, the outlet temperature of described outlet A is 60-70 DEG C.
Preferably, the outlet temperature of described outlet B is room temperature. Wherein the temperature of room temperature arranges according to the indoor temperature recording at that time.
Pure water and overflow water are by after the heat exchange of heat exchanger, and the outlet temperature of heat exchanger control outlet A is 60-70 DEG C, i.e. temperature after pure water heat exchange is 60-70 DEG C, and this temperature approaches temperature in soup washing trough, can reduce heating energy consumption. And after overflow water heat exchange, reduce temperature to room temperature, because temperature is lower, in water, impurity is less, can be directly used in spray.
Above disclosed is only a kind of preferred embodiment of the utility model, certainly can not limit with this interest field of the utility model, and the equivalent variations of therefore doing according to the utility model claim, still belongs to the scope that the utility model is contained.
Claims (6)
1. an aluminium section bar oxidation soup is washed the device that draining is recycled, it is characterized in that, comprise pure water tank, soup washing trough, heat exchanger and sprayed tank, described heat exchanger is provided with water inlet A, water inlet B, water outlet A and water outlet B, described water inlet A is communicated with pure water tank, described water outlet A and water inlet B are communicated with soup washing trough, and described water outlet B is communicated with sprayed tank.
2. aluminium section bar oxidation soup is washed the device that draining is recycled as claimed in claim 1, it is characterized in that, described soup washing trough is provided with water supplement port and overfall, and described water supplement port is communicated with water outlet A, and described overfall is communicated with water inlet B.
3. aluminium section bar oxidation soup is washed the device that draining is recycled as claimed in claim 2, it is characterized in that, described water supplement port is located at the bottom of soup washing trough, and described overfall is located at the side wall upper part of soup washing trough.
4. aluminium section bar oxidation soup is washed the device that draining is recycled as claimed in claim 1, it is characterized in that, described heat exchanger is the one in plate type heat exchanger, jacketed type exchanger, double pipe heat exchanger and shell-and-tube heat exchanger.
5. aluminium section bar oxidation soup is washed the device that draining is recycled as claimed in claim 1, it is characterized in that, the outlet temperature of described outlet A is 60-70 DEG C.
6. aluminium section bar oxidation soup is washed the device that draining is recycled as claimed in claim 1, it is characterized in that, the outlet temperature of described outlet B is room temperature.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521005315.1U CN205236515U (en) | 2015-11-30 | 2015-11-30 | Drainage recycle's device is washed to aluminium alloy oxidation hot water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521005315.1U CN205236515U (en) | 2015-11-30 | 2015-11-30 | Drainage recycle's device is washed to aluminium alloy oxidation hot water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205236515U true CN205236515U (en) | 2016-05-18 |
Family
ID=55935594
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521005315.1U Active CN205236515U (en) | 2015-11-30 | 2015-11-30 | Drainage recycle's device is washed to aluminium alloy oxidation hot water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205236515U (en) |
-
2015
- 2015-11-30 CN CN201521005315.1U patent/CN205236515U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206907566U (en) | A kind of high reliability cable processing water cooling plant | |
| CN204255099U (en) | The water system of metallurgical furnace cooling water | |
| CN106011902A (en) | Pickling tank | |
| CN205236515U (en) | Drainage recycle's device is washed to aluminium alloy oxidation hot water | |
| CN203546148U (en) | On-line temperature control system for acid-pickling solution | |
| CN105251739A (en) | Cleaning technology for sterilization system | |
| CN204891845U (en) | Degreasing agent preparation is with reposition of redundant personnel cooling system | |
| CN205893395U (en) | Acid washing tank | |
| CN104315885A (en) | Water cooling heat exchanger | |
| CN102923661B (en) | Anolyte clarifying tank waste chlorine gas recovery technology in ionic membrane caustic soda production | |
| CN213143220U (en) | Environment-friendly water-saving water supply equipment | |
| CN205495556U (en) | Chemical industry indirect heating equipment | |
| CN203443394U (en) | Cooling water cooling device | |
| CN204255100U (en) | The cooling water supply facility of metallurgical furnace | |
| CN108127895A (en) | A kind of uniform water cooling plant for pvc pipe production | |
| CN203955209U (en) | Integrated cooling heating system | |
| CN207290612U (en) | A kind of water-cooling groove for the production of Tourmaline master batch | |
| CN209508421U (en) | A kind of metallic steel ironworking processing acid washing phosphorization equipment | |
| CN219168401U (en) | Bromination reaction temperature control device for bromination SBS production | |
| CN207577136U (en) | A kind of cooling device for electric contact type continuous hot drawing mould | |
| CN105413613A (en) | Heat exchange device | |
| CN204894295U (en) | Energy -conserving temperature control system of general section mould utensil | |
| CN213400695U (en) | Electrode paste cooling forming device | |
| CN206986290U (en) | Copper sulfate electrolyte cooling device | |
| CN206285856U (en) | A kind of material-compound tank water circulation system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |