CN219751961U - Cutting fluid waste liquid enrichment facility - Google Patents
Cutting fluid waste liquid enrichment facility Download PDFInfo
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- CN219751961U CN219751961U CN202321124647.6U CN202321124647U CN219751961U CN 219751961 U CN219751961 U CN 219751961U CN 202321124647 U CN202321124647 U CN 202321124647U CN 219751961 U CN219751961 U CN 219751961U
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- waste liquid
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- evaporation
- liquid
- cutting fluid
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- 239000007788 liquid Substances 0.000 title claims abstract description 119
- 239000002699 waste material Substances 0.000 title claims abstract description 69
- 239000002173 cutting fluid Substances 0.000 title claims abstract description 31
- 238000001704 evaporation Methods 0.000 claims abstract description 80
- 230000008020 evaporation Effects 0.000 claims abstract description 69
- 230000007246 mechanism Effects 0.000 claims abstract description 27
- 238000003756 stirring Methods 0.000 claims description 15
- 239000012530 fluid Substances 0.000 claims description 11
- 229910010293 ceramic material Inorganic materials 0.000 claims description 6
- 238000004140 cleaning Methods 0.000 claims description 6
- 238000010438 heat treatment Methods 0.000 abstract description 13
- 239000012141 concentrate Substances 0.000 abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 19
- 239000000706 filtrate Substances 0.000 description 17
- 238000003860 storage Methods 0.000 description 12
- 230000009286 beneficial effect Effects 0.000 description 8
- 239000007787 solid Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 238000005406 washing Methods 0.000 description 5
- 239000000428 dust Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- 230000007797 corrosion Effects 0.000 description 3
- 238000005260 corrosion Methods 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 238000000227 grinding Methods 0.000 description 3
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 3
- 230000005068 transpiration Effects 0.000 description 3
- 230000000903 blocking effect Effects 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 125000004122 cyclic group Chemical group 0.000 description 2
- 238000010790 dilution Methods 0.000 description 2
- 239000012895 dilution Substances 0.000 description 2
- 238000005485 electric heating Methods 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 230000001050 lubricating effect Effects 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 239000012752 auxiliary agent Substances 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 238000005536 corrosion prevention Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- -1 ferrous metals Chemical class 0.000 description 1
- 238000003754 machining Methods 0.000 description 1
- 231100000989 no adverse effect Toxicity 0.000 description 1
- 231100000956 nontoxicity Toxicity 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Abstract
The utility model provides a cutting fluid waste liquid concentration device, which relates to the technical field of cutting fluid waste liquid treatment and comprises a vacuum low-temperature evaporation mechanism and a pretreatment mechanism, wherein the vacuum low-temperature evaporation mechanism comprises an evaporation tank, the pretreatment mechanism comprises a waste liquid tank, a liquid guide pipe is arranged on one side of the bottom end of the waste liquid tank, the other end of the liquid guide pipe is communicated with the evaporation tank, an air guide pipe is arranged on one side of the top of the evaporation tank, a condenser is communicated with the other end of the air guide pipe, a vacuum pump connecting port is arranged on one side of the bottom end of the condenser, a liquid receiving tank is arranged at the bottom of the condenser, a liquid outlet is formed in the bottom of the liquid receiving tank, and a discharge outlet is formed in the bottom of the evaporation tank. The utility model can effectively concentrate the cutting fluid waste liquid, does not need to arrange a heating device, is more energy-saving and environment-friendly, and has higher practical value.
Description
Technical Field
The utility model belongs to the technical field of cutting fluid waste liquid treatment, and particularly relates to a cutting fluid waste liquid concentration device.
Background
The cutting fluid is an industrial liquid used in the metal cutting and grinding process and used for cooling and lubricating a cutter and a workpiece, is formed by scientifically compounding and matching a plurality of super functional auxiliary agents, and has the characteristics of good cooling performance, lubricating performance, rust resistance, oil removal and cleaning functions, corrosion prevention and easy dilution. Overcomes the defects of easy odor in summer, difficult dilution in winter and poor rust prevention effect of the traditional soap-based emulsion, has no adverse effect on lathe paint, is suitable for cutting and grinding ferrous metals, and belongs to the most leading grinding product at present. The cutting fluid has various indexes superior to those of saponified oil, and has the features of excellent cooling, cleaning, rust preventing, no toxicity, no smell, no corrosion to human body, no corrosion to equipment, no environmental pollution, etc.
The Chinese patent with publication number CN215403593U discloses a waste cutting fluid concentration treatment device in the machining industry, which comprises a waste fluid storage tank, a heating tank, a volatilization chamber, a standing tank, a liquefaction condensing chamber and a water storage tank; the waste liquid storage box is positioned above the heating box, a first pipeline is inserted into the waste liquid storage box and is connected with a water pump, the water pump pumps liquid in the heating box into the volatilizing chamber, the first pipeline falls on the heating box and is wound with an electric heating wire, and the first pipeline is inserted into the waste liquid storage box and enters the heating box after penetrating through the top of the waste liquid storage box;
according to the technical scheme, water is volatilized into water vapor through preheating and then spray heating, then the water vapor enters a liquefaction condensing chamber to be condensed into water and then flows into a water storage tank, and the water of the waste cutting fluid is removed; the waste cutting fluid evaporated with water is kept still and layered through a standing box, the upper layer returns to the waste liquid storage box to be rewritten and heated for volatilization again, and the lower layer dregs are discharged through a cleaning pull rod.
But this scheme uses the electric heating net to carry out the mode of heating to the heating cabinet and carries out the concentration to cutting fluid waste liquid, and the power consumption is relatively higher, still evaporates out the heat-sensitive material in the waste liquid easily simultaneously, leads to the purification water quality of condensation not good.
Accordingly, the present utility model has been made in view of the above problems, and an object of the present utility model is to provide a cutting fluid waste liquid concentrating device which has a more practical value.
Disclosure of Invention
In order to solve the technical problems, the utility model provides a cutting fluid waste liquid concentrating device.
The utility model discloses a purpose and an effect of a cutting fluid waste liquid concentration device, which are achieved by the following specific technical means:
the utility model provides a cutting fluid waste liquid enrichment facility, includes vacuum low temperature evaporation mechanism and pretreatment mechanism, vacuum low temperature evaporation mechanism includes the evaporation tank, pretreatment mechanism includes the waste liquid jar, waste liquid jar bottom one side is equipped with the catheter, the catheter other end and evaporation tank intercommunication, evaporation tank top one side is equipped with the air duct, the air duct other end intercommunication has the condenser, just condenser bottom one side is equipped with the vacuum pump connector, the condenser bottom is equipped with receives the fluid reservoir, receive the fluid reservoir bottom to offer the liquid outlet, the discharge gate has been seted up to evaporation tank bottom.
Adopt the beneficial effect of above-mentioned further scheme, through the setting of evaporation pot, be convenient for provide the place that the filtrate carries out evaporation concentration, through catheter other end and evaporation pot intercommunication, be convenient for with the filtrate after pretreatment mechanism handles leading-in vacuum low temperature evaporation mechanism, setting through the condenser, be convenient for condense the vapor of evaporation into liquid, be equipped with the vacuum pump connector through condenser bottom one side, be convenient for connect the vacuum pump, make evaporation pot inside be vacuum negative pressure state, carry out evaporation concentration with the filtrate and handle, do not need to set up heating device, more energy-concerving and environment-protective, through the setting that receives the fluid reservoir, be convenient for collect the condensate of condenser condensation, through the setting of liquid outlet, be convenient for with receiving fluid reservoir intercommunication storage water tank, thereby be convenient for processing workshop cyclic utilization, the discharge gate has been seted up through the evaporation pot bottom, be convenient for collect the concentrated evaporating concentrate of accomplishing the concentration evaporation inside the evaporation of evaporation pot.
Further, the top of the air duct is fixedly provided with a gas-liquid separator, the bottom of the gas-liquid separator is provided with a return pipe, and the other end of the return pipe is communicated with the evaporation tank.
The beneficial effect of adopting above-mentioned further scheme is, through gas-liquid separator's setting, the droplet of vapor and transpiration of being convenient for separates, blocks that the droplet from getting into the condenser, communicates with the evaporation tank through the back flow other end, is convenient for with blocking the droplet backward flow that gets into the condenser to the evaporation tank to it is more abundant to make the concentration.
Further, the motor is fixedly arranged at the top of the evaporation tank, the stirring paddle is arranged in the evaporation tank, and the output end of the motor is fixedly connected with the stirring paddle.
The technical scheme has the beneficial effects that the motor output end is fixedly connected with the stirring paddle, so that the motor is convenient to work to drive the stirring paddle to rotate and stir the filtrate in the evaporation tank, and evaporation concentration of the filtrate is accelerated.
Further, the top of the waste liquid tank is provided with a liquid inlet, and a filter screen is fixedly arranged in the middle of the inner side of the waste liquid tank.
The beneficial effect of adopting above-mentioned further scheme is, through the setting of filter screen, be convenient for separate filtering oil slick, suspended solid and solid dust granule in the waste liquid, carry out pretreatment to the concentration of waste liquid.
Further, the filter screen is made of ceramic materials.
The beneficial effect of adopting above-mentioned further scheme is, is ceramic material through the material of filter screen, makes the filter screen anticorrosive, and the filter effect is good.
Further, a drain outlet is formed in one side of the waste liquid tank, and the lowest position of the drain outlet is higher than the filter screen.
The filter screen has the beneficial effects that the filter screen is convenient to clean filter residues filtered by the filter screen through the arrangement of the drain outlet.
Furthermore, a backflushing cleaner is arranged at the bottom of the part, which is provided with the filter screen, of the inner side of the waste liquid tank, and a cleaning liquid outlet is formed in the bottom of the waste liquid tank.
The beneficial effect of adopting above-mentioned further scheme is, through recoil purger, is convenient for recoil to the filter screen, to the abundant clearance of filter screen, prevents that the filter screen from blockking up, through the setting of washing liquid export, is convenient for will carry out the washing liquid that washes to the filter screen and flow out.
Compared with the prior art, the utility model has the following beneficial effects:
1. according to the cutting fluid waste liquid concentration device, a place where filtrate is evaporated and concentrated is conveniently provided through the arrangement of the evaporation tank, the other end of the liquid guide pipe is communicated with the evaporation tank, the filtrate treated by the pretreatment mechanism is conveniently led into the vacuum low-temperature evaporation mechanism, the evaporated vapor is conveniently condensed into liquid through the arrangement of the condenser, a vacuum pump connection port is arranged on one side of the bottom end of the condenser, the vacuum pump is conveniently connected, the inside of the evaporation tank is in a vacuum negative pressure state, the filtrate is evaporated and concentrated, a heating device is not required, the device is more energy-saving and environment-friendly, the evaporated water condensed by the condenser is conveniently collected through the arrangement of the liquid receiving tank, the liquid receiving tank is conveniently communicated with the water storage tank, so that the processing workshop is conveniently recycled, and the discharge port is conveniently formed in the bottom of the evaporation tank, so that concentrated and evaporated concentrate is conveniently collected;
2. according to the cutting fluid waste liquid concentration device, floating oil, suspended matters and solid dust particles in waste liquid are conveniently separated and filtered through the arrangement of the filter screen, the waste liquid is concentrated and pretreated, the filter screen is made of ceramic materials, so that the filter screen is corrosion-resistant, the filtering effect is good, the filter screen is conveniently backflushed through the backflushing cleaner, the filter screen is fully cleaned, and the filter screen is prevented from being blocked; the utility model can effectively concentrate the cutting fluid waste liquid, does not need to arrange a heating device, is more energy-saving and environment-friendly, and has higher practical value.
Drawings
FIG. 1 is a perspective view of a cutting fluid waste liquid concentrating apparatus of the present utility model;
FIG. 2 is a perspective view of the vacuum cryogenic vaporization mechanism of the present utility model;
FIG. 3 is a system diagram of a cutting fluid waste liquid concentrating apparatus according to the present utility model.
In the figure, the correspondence between the component names and the drawing numbers is:
101. a vacuum low-temperature evaporation mechanism; 10101. an evaporation tank; 10102. an air duct; 10103. a gas-liquid separator; 10104. a condenser; 10105. a return pipe; 10106. a motor; 10107. stirring paddles; 10108. a discharge port; 10109. a vacuum pump connection port; 10110. a liquid receiving tank; 10111. a liquid outlet; 102. a pretreatment mechanism; 10201. a waste liquid tank; 10202. a liquid inlet; 10203. a sewage outlet; 10204. a cleaning liquid outlet; 10205. a filter screen; 10206. a backflushing cleaner; 10207. a catheter.
Detailed Description
Embodiments of the present utility model are described in further detail below with reference to the accompanying drawings and examples. The following examples are illustrative of the utility model but are not intended to limit the scope of the utility model.
Examples:
as shown in fig. 1 to 3:
the utility model provides a cutting fluid waste liquid concentrating device, which comprises a vacuum low-temperature evaporating mechanism 101 and a pretreatment mechanism 102, wherein the vacuum low-temperature evaporating mechanism 101 comprises an evaporating pot 10101, a place convenient for providing filtrate for evaporation concentration is provided by the arrangement of the evaporating pot 10101, the pretreatment mechanism 102 comprises a waste liquid pot 10201, a liquid guide tube 10207 is arranged at one side of the bottom end of the waste liquid pot 10201, the other end of the liquid guide tube 10207 is communicated with the evaporating pot 10101, the filtrate treated by the pretreatment mechanism 102 is conveniently led into the vacuum low-temperature evaporating mechanism 101 by the other end of the liquid guide tube 10207, an air guide tube 10102 is arranged at one side of the top of the evaporating pot 10101, the other end of the air guide tube 10102 is communicated with a condenser 10104, the evaporated water vapor is conveniently condensed into liquid by the arrangement of the condenser 10104, and condenser 10104 bottom one side is equipped with vacuum pump connector 10109, be equipped with vacuum pump connector 10109 through condenser 10104 bottom one side, be convenient for connect the vacuum pump, make the evaporation pot 10101 inside be vacuum negative pressure state, carry out evaporation concentration processing with the filtrate, need not set up heating device, it is more energy-concerving and environment-protective, condenser 10104 bottom is equipped with receives fluid reservoir 10110, through the setting that receives fluid reservoir 10110, be convenient for collect condenser 10104 condensed evaporation water, receive fluid reservoir 10110 bottom to offer liquid outlet 10111, through the setting of liquid outlet 10111, be convenient for receive fluid reservoir 10110 intercommunication storage water tank, thereby be convenient for process shop cyclic utilization, discharge gate 10108 has been seted up to the evaporation pot 10101 bottom, be convenient for collect the concentrated liquid that the evaporation was accomplished to evaporation pot 10101 inside through evaporation pot 10108 bottom.
The top of the air duct 10102 is fixedly provided with a gas-liquid separator 10103, small liquid drops which are convenient to separate water vapor and transpiration are arranged through the gas-liquid separator 10103, the small liquid drops are prevented from entering the condenser 10104, a return pipe 10105 is arranged at the bottom of the gas-liquid separator 10103, the other end of the return pipe 10105 is communicated with the evaporation tank 10101, and the other end of the return pipe 10105 is communicated with the evaporation tank 10101, so that the small liquid drops which enter the condenser 10104 in a blocking mode can be conveniently returned to the evaporation tank 10101, and therefore concentration is more sufficient.
Wherein, the motor 10106 is fixedly installed at the top of the evaporating pot 10101, the stirring paddle 10107 is arranged in the evaporating pot 10101, the output end of the motor 10106 is fixedly connected with the stirring paddle 10107, and the motor 10106 is conveniently operated to drive the stirring paddle 10107 to rotate and stir the filtrate in the evaporating pot 10101, so that the evaporation and concentration of the filtrate are accelerated.
Wherein, waste liquid jar 10201 top is equipped with inlet 10202, and waste liquid jar 10201 inboard middle part fixed mounting has filter screen 10205, through the setting of filter screen 10205, is convenient for separate filtering oil slick, suspended solid and the solid dust granule in the waste liquid, carries out pretreatment to the concentration of waste liquid.
Wherein, the material of filter screen 10205 is ceramic material, and the material through filter screen 10205 is ceramic material, makes filter screen 10205 anticorrosive, and the filter effect is good.
Wherein, drain 10203 has been seted up to waste liquid jar 10201 one side, and the lowest of drain 10203 is higher than filter screen 10205, through the setting of drain 10203, is convenient for clear up the filter residue that filter screen 10205 filtered down.
Wherein, waste liquid jar 10201 inboard is equipped with filter screen 10205 department bottom and is equipped with recoil purger 10206, through recoil purger 10206, is convenient for carry out the recoil to filter screen 10205, to the abundant clearance of filter screen 10205, prevents filter screen 10205 and blocks up, and waste liquid jar 10201 bottom has seted up washing liquid export 10204, through the setting of washing liquid export 10204, is convenient for will carry out the washing liquid that washes filter screen 10205 and flow.
Specific use and action of the embodiment:
when the product is used, firstly, whether the connecting part of the device is fastened or not is detected, the device is placed at a designated position after the device is ensured to be intact, cutting fluid waste liquid generated in a processing workshop is put into a waste liquid tank 10201 through a liquid inlet 10202, floating oil, suspended matters and solid dust particles in the waste liquid are conveniently separated and filtered through the arrangement of a filter screen 10205, the concentration of the waste liquid is pretreated, the other end of a liquid guide tube 10207 is communicated with an evaporation tank 10101, the filtrate treated by a pretreatment mechanism 102 is introduced into a vacuum low-temperature evaporation mechanism 101, a vacuum pump connecting port 10109 is arranged at one side of the bottom end of a condenser 10104 so as to be conveniently connected with a vacuum pump, the inside of the evaporation tank 10101 is in a vacuum negative pressure state, the filtrate is subjected to evaporation concentration treatment, the output end of a motor 10106 is fixedly connected with a stirring paddle 10107, the motor 10106 works to drive the stirring paddle 10107 to rotate and stir the filtrate inside the evaporation tank 10101, accelerate the evaporation and concentration of the filtrate, through the setting of the liquid receiving tank 10110, through the setting of the gas-liquid separator 10103, separate vapor and transpiration droplets, block the droplets to enter the condenser 10104, communicate with the evaporation tank 10101 through the other end of the return pipe 10105, will block the droplets entering the condenser 10104 to flow back to the evaporation tank 10101, thereby make the concentration more abundant, collect the evaporated water condensed by the condenser 10104, through the setting of the liquid outlet 10111, be convenient for with the liquid receiving tank 10110 intercommunication storage tank, thereby be convenient for processing workshop circulation use, discharge gate 10108 has been seted up through the bottom of the evaporation tank 10101, collect the concentrated liquid that the concentration and evaporation are accomplished inside the evaporation tank 10101.
The embodiments of the utility model have been presented for purposes of illustration and description, and are not intended to be exhaustive or limited to the utility model in the form disclosed. Many modifications and variations will be apparent to those of ordinary skill in the art. The embodiments were chosen and described in order to best explain the principles of the utility model and the practical application, and to enable others of ordinary skill in the art to understand the utility model for various embodiments with various modifications as are suited to the particular use contemplated.
Claims (7)
1. A cutting fluid waste liquid enrichment facility, its characterized in that: including vacuum cryogenic evaporation mechanism (101) and pretreatment mechanism (102), vacuum cryogenic evaporation mechanism (101) include evaporation tank (10101), pretreatment mechanism (102) are including waste liquid jar (10201), waste liquid jar (10201) bottom one side is equipped with catheter (10207), catheter (10207) other end and evaporation tank (10101) intercommunication, evaporation tank (10101) top one side is equipped with air duct (10102), air duct (10102) other end intercommunication has condenser (10104), just condenser (10104) bottom one side is equipped with vacuum pump connector (10109), condenser (10104) bottom is equipped with receives fluid reservoir (10110), liquid outlet (10111) have been seted up to receiving fluid reservoir (10110) bottom, discharge gate (10108) have been seted up to evaporation tank (10101) bottom.
2. The cutting fluid waste liquid concentrating apparatus of claim 1, wherein: the top of the air duct (10102) is fixedly provided with a gas-liquid separator (10103), the bottom of the gas-liquid separator (10103) is provided with a return pipe (10105), and the other end of the return pipe (10105) is communicated with the evaporation tank (10101).
3. The cutting fluid waste liquid concentrating apparatus of claim 1, wherein: the top of the evaporation tank (10101) is fixedly provided with a motor (10106), a stirring paddle (10107) is arranged inside the evaporation tank (10101), and the output end of the motor (10106) is fixedly connected with the stirring paddle (10107).
4. The cutting fluid waste liquid concentrating apparatus of claim 1, wherein: the top of the waste liquid tank (10201) is provided with a liquid inlet (10202), and a filter screen (10205) is fixedly arranged in the middle of the inner side of the waste liquid tank (10201).
5. The cutting fluid waste liquid concentrating apparatus of claim 4, wherein: the filter screen (10205) is made of ceramic materials.
6. The cutting fluid waste liquid concentrating apparatus of claim 4, wherein: a drain outlet (10203) is formed in one side of the waste liquid tank (10201), and the lowest position of the drain outlet (10203) is higher than the filter screen (10205).
7. The cutting fluid waste liquid concentrating apparatus of claim 6, wherein: the waste liquid tank (10201) is provided with a filter screen (10205) inside, the bottom of the part is provided with a backflushing cleaner (10206), and the bottom of the waste liquid tank (10201) is provided with a cleaning liquid outlet (10204).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321124647.6U CN219751961U (en) | 2023-05-10 | 2023-05-10 | Cutting fluid waste liquid enrichment facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321124647.6U CN219751961U (en) | 2023-05-10 | 2023-05-10 | Cutting fluid waste liquid enrichment facility |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN219751961U true CN219751961U (en) | 2023-09-26 |
Family
ID=88082946
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321124647.6U Active CN219751961U (en) | 2023-05-10 | 2023-05-10 | Cutting fluid waste liquid enrichment facility |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN219751961U (en) |
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2023
- 2023-05-10 CN CN202321124647.6U patent/CN219751961U/en active Active
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