CN220845600U - Waste cooling liquid component separation recovery processing device - Google Patents
Waste cooling liquid component separation recovery processing device Download PDFInfo
- Publication number
- CN220845600U CN220845600U CN202322542239.9U CN202322542239U CN220845600U CN 220845600 U CN220845600 U CN 220845600U CN 202322542239 U CN202322542239 U CN 202322542239U CN 220845600 U CN220845600 U CN 220845600U
- Authority
- CN
- China
- Prior art keywords
- water
- evaporation
- lifting box
- cooling liquid
- waste
- 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
- 239000002699 waste material Substances 0.000 title claims abstract description 38
- 239000000110 cooling liquid Substances 0.000 title claims abstract description 34
- 238000000926 separation method Methods 0.000 title claims abstract description 14
- 238000011084 recovery Methods 0.000 title claims abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 114
- 238000001704 evaporation Methods 0.000 claims abstract description 40
- 230000008020 evaporation Effects 0.000 claims abstract description 40
- 239000007788 liquid Substances 0.000 claims abstract description 37
- 238000003860 storage Methods 0.000 claims abstract description 23
- 238000009825 accumulation Methods 0.000 claims abstract description 20
- 238000007667 floating Methods 0.000 claims abstract description 5
- 239000002826 coolant Substances 0.000 claims description 15
- 238000010438 heat treatment Methods 0.000 claims description 7
- 238000007599 discharging Methods 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 3
- 239000000839 emulsion Substances 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- 239000012153 distilled water Substances 0.000 description 6
- 238000004659 sterilization and disinfection Methods 0.000 description 5
- 238000005189 flocculation Methods 0.000 description 4
- 230000016615 flocculation Effects 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 230000001954 sterilising effect Effects 0.000 description 4
- 230000009471 action Effects 0.000 description 3
- 230000006866 deterioration Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000004064 recycling Methods 0.000 description 3
- 238000003754 machining Methods 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 230000003044 adaptive effect Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000005485 electric heating Methods 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000003801 milling Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000000053 physical method Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000011550 stock solution Substances 0.000 description 1
- 238000005482 strain hardening Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000007514 turning Methods 0.000 description 1
Landscapes
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The utility model discloses a waste cooling liquid component separation and recovery treatment device, which comprises a waste cooling liquid water storage device, wherein a water accumulation tank is arranged on the right side of the waste cooling liquid water storage device, a lifting tank is arranged on the upper side of the water accumulation tank, a water feeding structure is arranged between the lifting tank and the waste cooling liquid water storage device, an evaporation structure is arranged in the lifting tank, a drainage structure is arranged in the water accumulation tank, and a floating ball liquid level switch for controlling the water feeding structure is arranged in the lifting tank.
Description
Technical Field
The utility model relates to the technical field of machining, in particular to a waste cooling liquid component separation and recovery treatment device.
Background
Emulsified cooling liquid is widely applied in metal processing in the mechanical manufacturing industry. The emulsion cooling liquid for turning, milling and grinding of cold working has the concentration of 5% -10%, after a certain period of use, the main component, namely water, can produce bacterial deterioration, and after deterioration, the emulsion cooling liquid can produce adverse effects on corrosion of workpieces, maintenance of machine tools, service life of cutters and the like, and the serious threat of malodorous volatile gas on the health of operators and the influence on working environment are great. However, the problem of deterioration treatment of a large amount of coolant due to various reasons has not been solved. At present, a physical method treatment device for separating and recovering components of modified cooling liquid is lacked, and the problems of effective sterilization and flocculation separation of waste cooling liquid, sewage and the like can be solved.
Disclosure of Invention
According to the defects of the prior art, the invention aims to provide a waste emulsion separating and recycling treatment device which can realize sterilization treatment and simultaneously perform emulsion breaking flocculation separation and recycling or concentrate a small amount of concentrated waste to request professional treatment. The treatment cost is reduced, and the field operation environment is improved.
In order to achieve the above purpose, the utility model is realized by the following technical scheme: the utility model provides a useless coolant liquid composition separation recovery processing device, includes useless coolant liquid water reservoir, the water tank is installed on useless coolant liquid water reservoir's right side, the lifting tank is installed to the upside of water tank, the lifting tank with install the structure of going up between the useless coolant liquid water reservoir, install evaporation structure in the lifting tank, install drainage structure in the water tank, install in the lifting tank and be used for controlling the floater liquid level switch of structure of going up.
Preferably, the water feeding structure comprises a water feeding pump, the water feeding pump is arranged in the waste cooling liquid water reservoir, a waste liquid lifting water pipe is arranged at the water outlet end of the water feeding pump, and the waste liquid lifting water pipe is communicated with the lifting box.
Preferably, the evaporation structure comprises an evaporator, the evaporator is arranged on the inner right side of a lifting box, a water storage cavity is formed in the inner left side of the lifting box, an evaporation outer chamber is formed between the water storage cavity and the evaporator and in the lifting box, a water inlet pipe is inserted in the right side of the water storage cavity, the water inlet pipe penetrates through the evaporation outer chamber and is communicated with the evaporator, a communicating pipe is inserted in the water storage tank, the communicating pipe is communicated with the evaporation outer chamber, and the water storage cavity is communicated with the waste cooling liquid water storage device through a water feeding structure.
Preferably, the evaporator comprises an evaporation cavity arranged on the right side in the lifting box, a notch communicated with the evaporation outer chamber is arranged on the upper left side of the evaporation cavity, a floating ball liquid level valve for controlling a water inlet pipe is arranged in the evaporation cavity, a plurality of heating rods are arranged on the lower side of the evaporation cavity and outside the lifting box, and a residual liquid discharging pipe communicated with the evaporation cavity is arranged outside the lifting box.
Preferably, the number of the heating rods is three.
Preferably, the drainage structure comprises a submersible pump, the submersible pump is arranged in the water accumulation tank, a drainage pipe is arranged at the water outlet end of the submersible pump, and the drainage pipe penetrates through the water accumulation tank.
Advantageous effects
The utility model provides a waste cooling liquid component separation and recovery treatment device. The device has the beneficial effects that the device for separating, recovering and treating the waste cooling liquid components effectively separates high Wen Poru flocculation of emulsion stock solution and water with corresponding proportion, and the following purposes are satisfied:
The physical high-temperature sterilization eliminates equipment pollution and air pollution of a machining site, improves the using effect of the cutter and ensures the product quality of machined parts;
Distilled water can be repeatedly utilized to blend cooling liquid, the concentrated residual liquid amount is obviously reduced, the treatment cost is compared with the entrusted professional high-volume treatment cost, and the treatment cost is only about fifteen percent of the existing sewage treatment cost, so that the treatment cost of enterprises on dangerous wastes is reduced, and the processing cost is saved. Solves the difficult problem in the mechanical processing industry.
Drawings
Fig. 1 is a schematic structural view of the present utility model.
Fig. 2 is a schematic diagram of the structure at a in the present utility model.
In the figure: 1. a waste coolant reservoir; 2. a water accumulation tank; 3. a lifting box; 4. an evaporation outer chamber; 5. an evaporator; 6. a waste liquid lifting water pipe; 7. a float ball liquid level switch; 8. a water inlet pipe; 9. a float ball liquid level valve; 10. a heating rod; 11. a communicating pipe; 12. a residual liquid discharging tube; 13. feeding a water pump; 14. submersible pump; 15. and (5) a water drain pipe.
Detailed Description
The following description of the embodiments of the present utility model will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present utility model, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
All electric components in the scheme are connected with an adaptive power supply through wires by a person skilled in the art, and an appropriate controller is selected according to actual conditions so as to meet control requirements, specific connection and control sequences, and the electric connection is completed by referring to the following working principles in the working sequence among the electric components, wherein the detailed connection means are known in the art, and the following main description of the working principles and processes is omitted from the description of electric control.
Referring to fig. 1-2, the present utility model provides a technical solution: the utility model provides a useless coolant liquid composition separation recovery processing device, includes useless coolant liquid water storage 1, water accumulation tank 2 is installed on useless coolant liquid water storage 1's right side, lift box 3 is installed to water accumulation tank 2's upside, lift box 3 with install the structure of going up between the useless coolant liquid water storage 1, install evaporation structure in the lift box 3, install drainage structures in the water accumulation tank 2, install in the lift box 3 and be used for controlling the floater liquid level switch 7 of structure of going up.
Embodiment one: the water feeding structure comprises a water feeding pump 13, the water feeding pump 13 is arranged in the waste cooling liquid water reservoir 1, a waste liquid lifting water pipe 6 is arranged at the water outlet end of the water feeding pump 13, and the waste liquid lifting water pipe 6 is communicated with the lifting box 3.
Embodiment two: the evaporation structure comprises an evaporator 5, the evaporator 5 is arranged on the inner right side of a lifting box 3, a water storage cavity is formed in the inner left side of the lifting box 3, an evaporation outer chamber 4 is formed between the water storage cavity and the evaporator 5 and in the lifting box 3, a water inlet pipe 8 is inserted in the right side of the water storage cavity, the water inlet pipe 8 penetrates through the evaporation outer chamber 4 and is communicated with the evaporator 5, a communicating pipe 11 is inserted in a water accumulation box 2, the communicating pipe 11 is communicated with the evaporation outer chamber 4, and the water storage cavity is communicated with the waste cooling liquid water storage device 1 through the water feeding structure.
The evaporator 5 comprises an evaporation cavity arranged on the right side in the lifting box 3, a notch communicated with the evaporation outer chamber 4 is arranged on the upper left side of the evaporation cavity, a floating ball liquid level valve 9 for controlling the water inlet pipe 8 is arranged in the evaporation cavity, a plurality of heating rods 10 are arranged on the lower side of the evaporation cavity and positioned outside the lifting box 3, and a residual liquid discharging pipe 12 communicated with the evaporation cavity is arranged outside the lifting box 3.
The number of the heating rods 10 is three.
Embodiment III: the water draining structure comprises a submersible pump 14, wherein the submersible pump 14 is arranged in the water accumulation tank 2, a water draining pipe 15 is arranged at the water outlet end of the submersible pump 14, and the water draining pipe 15 penetrates through the water accumulation tank 2;
Specifically, the discarded cooling liquid is poured into the waste cooling liquid water storage device 1 for precipitation and storage, and the precipitated waste cooling liquid is guided into the lifting box 3 by the water pump 13 through the waste liquid lifting water pipe 6. The float level switch 7 controls the level of the liquid in the lifting box 3 to generate a certain water level pressure difference with the evaporator 5. The waste cooling liquid flows into the evaporator 5 from the lifting box 3 through the water inlet pipe 8, the floating ball liquid level valve 9 is arranged in the evaporator 5, and the liquid level in the evaporator 5 is controlled. Three groups of electric heating rods 10 are arranged at intervals in parallel at the lower part in the evaporator 5, and the waste cooling liquid in the evaporator 5 is heated to be boiled. Because the evaporator 5 is arranged in the airtight evaporation chamber, a part of generated vapor is cooled through the outer wall of the evaporation chamber and the lifting box 3, and because a certain amount of cooling liquid exists in the lifting box 3, the vapor in the evaporation chamber can be quickly condensed while being preheated, and distilled water which is condensed together with the evaporation outer chamber 4 flows into the water accumulation tank 2 through the communicating pipe 11. Meanwhile, the water vapor which is not condensed enters the water accumulation tank 2 through the communicating pipe 11, and the water vapor is continuously and fully condensed into distilled water in the water accumulation tank 2. Distilled water in the two areas is concentrated in the water accumulation tank 2 and is then discharged and recovered by the submersible pump 14 in the water accumulation tank 2 through the drain pipe 15, and the blended cooling liquid is continuously reconstituted and put into use. The concentrated emulsion after evaporation is left in the evaporator 5, and is discharged through the drain pipe 15 for centralized use or treatment at regular timing by stopping. The distilled water and the concentrated emulsion are boiled, vaporized and condensed to complete the disinfection, sterilization and the distillation flocculation of the emulsion, the distilled water is recycled after separation, and the cooling liquid is continuously blended to achieve the aim of separating and recycling the components of the waste cooling liquid. Solves the difficult problem in the mechanical processing industry.
It is noted that relational terms such as first and second, and the like are used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Moreover, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus. Without further limitation. The term "comprising" an element defined by the term "comprising" does not exclude the presence of other identical elements in a process, method, article or apparatus that comprises the element.
Although embodiments of the present utility model have been shown and described, it will be understood by those skilled in the art that various changes, modifications, substitutions and alterations can be made therein without departing from the principles and spirit of the utility model, the scope of which is defined in the appended claims and their equivalents.
Claims (6)
1. The utility model provides a useless coolant liquid composition separation recovery processing device, its characterized in that, including useless coolant liquid water reservoir (1), ponding case (2) are installed on the right side of useless coolant liquid water reservoir (1), lifting box (3) are installed to the upside of ponding case (2), lifting box (3) with install the structure of going up between useless coolant liquid water reservoir (1), install evaporation structure in lifting box (3), install drainage structure in ponding case (2), install in lifting box (3) and be used for controlling floater liquid level switch (7) of structure of going up.
2. The waste cooling liquid component separation and recovery treatment device according to claim 1, wherein the water supply structure comprises a water supply pump (13), the water supply pump (13) is arranged in the waste cooling liquid water reservoir (1), a waste liquid lifting water pipe (6) is arranged on the water outlet end of the water supply pump (13), and the waste liquid lifting water pipe (6) is communicated with the lifting box (3).
3. The device for separating, recovering and treating the waste cooling liquid components according to claim 1, wherein the evaporation structure comprises an evaporator (5), the evaporator (5) is arranged on the inner right side of a lifting box (3), a water storage cavity is formed on the inner left side of the lifting box (3), an evaporation outer chamber (4) is formed between the water storage cavity and the evaporator (5) and in the lifting box (3), a water inlet pipe (8) is inserted on the right side of the water storage cavity, the water inlet pipe (8) penetrates through the evaporation outer chamber (4) and is communicated with the evaporator (5), a communicating pipe (11) is inserted on the water accumulation box (2), the communicating pipe (11) is communicated with the evaporation outer chamber (4), and the water storage cavity is communicated with the waste cooling liquid water reservoir (1) through the water feeding structure.
4. The waste cooling liquid component separation and recovery treatment device according to claim 3, wherein the evaporator (5) comprises an evaporation cavity arranged on the right side in the lifting box (3), a notch communicated with the evaporation outer chamber (4) is arranged on the upper left side of the evaporation cavity, a floating ball liquid level valve (9) for controlling the water inlet pipe (8) is arranged in the evaporation cavity, a plurality of heating rods (10) are arranged on the lower side of the evaporation cavity and positioned outside the lifting box (3), and a residual liquid discharging pipe (12) communicated with the evaporation cavity is arranged outside the lifting box (3).
5. The apparatus for separating, recovering and treating a waste coolant component according to claim 4, wherein the number of the plurality of heating rods (10) is three.
6. The waste cooling liquid component separation and recovery treatment device according to claim 1, wherein the drainage structure comprises a submersible pump (14), the submersible pump (14) is arranged in the water accumulation tank (2), a drainage pipe (15) is arranged on the water outlet end of the submersible pump (14), and the drainage pipe (15) penetrates through the water accumulation tank (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322542239.9U CN220845600U (en) | 2023-09-19 | 2023-09-19 | Waste cooling liquid component separation recovery processing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322542239.9U CN220845600U (en) | 2023-09-19 | 2023-09-19 | Waste cooling liquid component separation recovery processing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220845600U true CN220845600U (en) | 2024-04-26 |
Family
ID=90747348
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322542239.9U Active CN220845600U (en) | 2023-09-19 | 2023-09-19 | Waste cooling liquid component separation recovery processing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220845600U (en) |
-
2023
- 2023-09-19 CN CN202322542239.9U patent/CN220845600U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104016529B (en) | Based on the Coal Chemical Industry salt-containing waste water treatment method of multi-stage countercurrent pole-reversing electroosmosis device | |
| CN104532283B (en) | A kind of light salt brine replaces method and the device of part refined brine electrolysis caustic soda | |
| CN1902437A (en) | Method for production of high pressure steam from produced water | |
| CN107555692A (en) | A kind of water oil separating method of emulsion waste liquid | |
| CN104973638A (en) | Processing technology of high-salt high-concentration organic waste liquid | |
| CN104355431A (en) | Device capable of efficiently treating and recycling reverse osmosis concentrated water and high-salt wastewater | |
| CN107628660A (en) | A kind of high salinity waste water mechanical vapor recompresses MVR systems technologies | |
| CN220845600U (en) | Waste cooling liquid component separation recovery processing device | |
| JP4264950B2 (en) | Evaporative concentration apparatus for aqueous waste liquid and aqueous cleaning apparatus using the same | |
| CN107555693A (en) | A kind of emulsion waste liquid water oil piece-rate system | |
| WO2000010922A1 (en) | Treatment of aqueous wastes | |
| CN109502858A (en) | A kind of photovoltaic industry fluorine-contained wastewater treatment system and its processing method | |
| CN108249670A (en) | A kind of acid etching liquid treatment acid solution and the technique for recycling copper | |
| WO2022247111A1 (en) | Hydrochloric acid pickling solution purification and sludge treatment process | |
| CN207391187U (en) | A kind of emulsion waste liquid water oil piece-rate system | |
| CN213416350U (en) | Sewage treatment device | |
| CN107857323A (en) | The apparatus and method handled with reference to MVR garbage percolation concentrate | |
| CN209065643U (en) | A kind of coating wastewater vaporising device | |
| CN209065644U (en) | Waste water evaporation process equipment before a kind of coating | |
| CN110078290A (en) | A kind of processing method of high organic wastewater with high salt | |
| CN207596651U (en) | A kind of wastewater treatment equipment in the production for stainless steel | |
| CN216687795U (en) | Degreasing wastewater treatment system | |
| CN111747467A (en) | Sewage treatment method and device | |
| CN220907310U (en) | Emulsion liquid film concentration evaporation disposal system | |
| CN111690976A (en) | Electroplating bath liquid management, concentration and reuse process |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |