CN217265341U - Industrial waste liquid purification device - Google Patents
Industrial waste liquid purification device Download PDFInfo
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- CN217265341U CN217265341U CN202221266544.9U CN202221266544U CN217265341U CN 217265341 U CN217265341 U CN 217265341U CN 202221266544 U CN202221266544 U CN 202221266544U CN 217265341 U CN217265341 U CN 217265341U
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- liquid
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- waste liquid
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- industrial waste
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
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Abstract
The utility model discloses an industrial waste liquid purifier, including the stock solution bucket that is equipped with the feed liquor pipe, the clean part of being connected through the high-pressure pump with the stock solution bucket and the fluid-discharge tube of being connected with the clean part, the stock solution bucket is equipped with the cooler, is equipped with the clean barrel that has filtration between fluid-discharge tube and the clean part, and filtration includes fungus pond, softener, filter and electrolyzer etc, the utility model discloses in using, can carry out effectual purification treatment with the produced sewage of industry, cooling structure design is more reasonable, has improved waste liquid purification efficiency, has alleviated industrial sewage's blowdown pressure, has reduced the maintenance cost, has realized more green's production mode.
Description
Technical Field
The utility model belongs to the technical field of waste liquid treatment equipment, particularly, what relate to is used for an industrial waste liquid purifier in the middle of the industrial production.
Background
The water consumption becomes higher and higher along with the development of productivity in the industry, and then the production of more industrial waste liquid that brings, if not to handle industrial waste liquid well, can cause serious pollution and destruction to the environment, heavy metal ion and the organic matter that wherein contains can lead to the water eutrophication, cause ecological balance's serious unbalance, especially when the waste liquid produces, often have certain temperature or even high temperature, can not be handled by subsequent filtration the very first time, lead to filtration efficiency not good, and current cooling structure uses inconvenient maintenance difficulty that causes, so both increased the cost of enterprise, and lead to the filter effect poor.
SUMMERY OF THE UTILITY MODEL
To the technical defect who exists in the background art, the utility model provides an industrial waste liquid purifier has solved above-mentioned technical problem and has satisfied the actual demand, and concrete technical scheme is as follows:
the industrial waste liquid purifying device comprises a raw liquid barrel provided with a liquid inlet pipe, a purifying part connected with the raw liquid barrel through a high-pressure pump, and a liquid discharge pipe connected with the purifying part, wherein the purifying part comprises a sedimentation tank, a water softener, a biological bacteria pool, a filter and an exposure pool which are sequentially connected between the high-pressure pump and the liquid discharge pipe, a cooling pipe group is arranged between the raw liquid barrel and the liquid inlet pipe, the cooling pipe group comprises a raw liquid net pipe connected between the liquid inlet pipe and the raw liquid barrel and a cooling liquid net pipe which is inserted between the raw liquid net pipes and is tightly attached to the raw liquid net pipe, the water inlet end and the water outlet end of the cooling liquid net are both connected with a circulating pump communicated with the exposure pool, and the liquid discharge pipe is connected with the exposure pool and is provided with an electric on-off valve.
As the utility model discloses further technical scheme, the end height that highly is less than out the water end of intaking of stoste pipe network, the end height that highly is higher than out the water end of intaking of coolant liquid pipe network.
As a further technical scheme of the utility model, the play water end of coolant liquid pipe network with be equipped with the wraparound between the circulating pump the straight-through alternate pipeline of the bottom in sedimentation tank and biological fungus pond.
As a further technical scheme of the utility model, the bottom of former liquid bucket is equipped with the flat conduction part of a plurality of, be equipped with between the conduction part with external communicating letter of ventilating, all the conduction part assemble in the feed liquor end of high-pressure pump.
As a further technical scheme of the utility model, the conduction part is narrow stage body form under wide, just be equipped with in the conduction part connect in the outside driving motor's of former liquid bucket stirring vane.
As a further technical scheme of the utility model, still be equipped with the electrically controlled device that electronic on-off valve links to each other, electrically controlled device is connected with flow sensor, flow sensor set up in the end of intaking of circulating pump perhaps goes out the water end.
The utility model discloses the beneficial effect who has lies in: in practical application, the utility model discloses can carry out effectual purification treatment with the produced sewage of industry, cooling structure design is more reasonable, has improved waste liquid purification efficiency, has alleviated the blowdown pressure of industrial sewage, has reduced the maintenance cost, has realized more green's production methods.
Drawings
Fig. 1 is a schematic view of the overall structure of the present invention.
Wherein: the device comprises a liquid inlet pipe 1, a raw liquid barrel 2, a conducting part 20, a ventilating channel 21, a driving motor 22, a stirring blade 23, a high-pressure pump 3, a liquid discharge pipe 4, a sedimentation tank 5, a biological bacteria tank 6, a water softener 7, a filter 8, an insolation tank 9, a raw liquid network pipe 10, a cooling liquid network pipe 11, a circulating pump 12, an electric on-off valve 13, a straight-through penetrating pipeline 14, an electric control device 15 and a flow sensor 16.
Detailed Description
The embodiments of the present invention will be described with reference to the accompanying drawings and related examples, but the embodiments of the present invention are not limited to the following examples, and the relevant essential components of the present invention related to the technical field should be regarded as known in the art, and can be known and grasped by those skilled in the art.
An industrial waste liquid purifying device comprises a stock solution barrel 2 provided with a liquid inlet pipe 1, a purifying part connected with the stock solution barrel 2 through a high-pressure pump 3 and a liquid discharge pipe 4 connected with the purifying part, the purification part comprises a sedimentation tank 5, a water softener 7, a biological bacteria tank 6, a filter 8 and an insolation tank 9 which are connected between the high-pressure pump 3 and the liquid discharge pipe 4 in sequence, a cooling pipe group is arranged between the stock solution barrel 2 and the liquid inlet pipe 1, the cooling pipe group comprises a stock solution net pipe 10 connected between the liquid inlet pipe 1 and the stock solution barrel 2 and a cooling liquid net pipe 11 inserted between the stock solution net pipes 10 and tightly jointed with the stock solution net pipe 10, the water inlet end and the water outlet end of the cooling liquid pipe network 11 are both connected with a circulating pump 12 communicated with the solarization pool 9, and the liquid discharge pipe 4 is connected with the solarization pool 9 and is provided with an electric on-off valve 13.
Combine the attached drawing, the arrow point direction is the flow direction of liquid, the utility model provides a sedimentation tank 5, biological fungus pond 6, water softener 7, filter 8 and insolate pond 9 for structure commonly used and the attached equipment among the water purification technology field, the utility model discloses well direct calling or change above-mentioned structure, make its mutual intercommunication form complete waste liquid filtration way, let the waste liquid can change into the dischargeable water harmless to the environment through normal waste water treatment flow, and then by the natural water body in the middle of purifying the normal hydrologic cycle of entering at last, avoid causing the pollution to the environment.
The water softener 7 is an automatic dosing device for softening permanent hard water, and is a common structure for changing water into softened water after hard water components in the water are precipitated by adding a proper amount of chemical agents into the water, or can be replaced by an existing automatic dosing device. And the filter 8 is the commonly used filtration structure of water filtration such as active carbon filter screen, can satisfy the utility model discloses a operation requirement based on the structure that can replace easy to maintain. The water softener 7 and the filter 8 are provided with pipelines with enough inner diameters for water to pass through, or the water softener 7 is arranged in the sedimentation tank 5, and the filter is arranged between the biological bacteria tank 6 and the solarization tank 9, so that the common arrangement mode of the technicians in the field can be met.
And the waste liquid can flow into whole filter equipment through feed liquor pipe 1 after discharging from the mill, and as is known, the waste liquid often has certain temperature or even high temperature, if not in time cool down will influence subsequent waste liquid treatment process, such as can't reach suitable softening chemical reaction temperature etc. current cooling structure generally lets its natural cooling in as to a transfer pond, and it is lower to consume time like this, efficiency. In the utility model, the waste liquid will enter the stock solution barrel 2 after passing through the cooling pipe group, only need short stay and can send into subsequent filtration purification process through the high-pressure pump 3, in the cooling pipe group, the stock solution pipe network 10 through which the waste liquid flows will intersect with the cooling liquid pipe network 11, but the two are not communicated with each other but can exchange heat, after the waste liquid and the cooling liquid carry out total heat exchange, the temperature will be reduced remarkably, thus the temperature of the waste liquid entering the stock solution barrel 2 will be lower, only need short stay and can enter into the subsequent filtration process, as for the source of the cooling liquid, purified water is accomplished in the solarization pool 9, after the filtration operation is accomplished, the purified water will be stood in large quantities to solarize, because the temperature is normal temperature, low temperature for the waste liquid stock solution, therefore, the circulating pump 12 is utilized, pump it to the cooling liquid pipe network 11 and stock solution pipe network 10 to carry out total heat exchange, the reuse of the purified water before the discharge is realized, and after the circulation for a plurality of times, the solarization pool 9 reaches the rated discharge capacity, the electric on-off valve 13 is started to discharge, and the environmental protection requirement is met.
The utility model discloses one of the preferred embodiment, the end of intaking of stoste pipe network 10 highly is less than the height of play water end, the end of intaking of coolant liquid pipe network 11 highly is higher than the height of play water end, and in order to let the total heat exchange between waste liquid and the coolant liquid more thoroughly, through the mode that sets up of this embodiment, has improved the flow velocity of coolant liquid, and has reduced the velocity of flow of stoste, and the waste liquid stoste will be taken away the heat by more cooling purified water, make full use of the specific heat capacity of cooling purified water, convenience very.
The utility model discloses one of the preferred embodiment, coolant liquid pipe network 11's play water end with be equipped with the warp between the circulating pump 12 the straight-through pipeline 14 that alternates of the bottom of sedimentation tank 5 and biological fungus pond 6, give off for letting the heat of the cooling purified water through total heat exchange faster, reduce the influence to sedimentation tank 5 and biological fungus pond 6 simultaneously for keep comparatively reasonable heat balance among the two, consequently adopted straight-through pipeline 14 that alternates, let it can heat transfer to a certain extent, but do not significantly influence the set operating temperature of 2 above-mentioned structures.
The utility model discloses one of the preferred embodiment, the bottom of stoste bucket 2 is equipped with the flat conduction part 20 of a plurality of, be equipped with between the conduction part 20 with external communicating letter way 21 of ventilating, all conduction part 20 assemble in the feed liquor end of high-pressure pump 3, for the cooling efficiency who improves the stoste, stoste bucket 2 utilizes conduction part 20 and the letter way 21 of ventilating to cooperate, lets the new trend can be when the letter way 21 of ventilating, takes away the heat of the stoste in the conduction part 20 of both sides, realizes the supplementary refrigerated technical purpose of nature.
The utility model discloses one of the preferred embodiment, conduction portion 20 is narrow stage form under the upper width, just be equipped with in conduction portion 20 connect in the stirring vane 23 of the outside driving motor 22 of stoste bucket 2, in order to cool off the stoste better and avoid waste liquid stoste to block up stoste bucket 2, conduction portion 20 has adopted narrow stage form structure under the upper width to utilize stirring vane 23 to stir stoste bucket 2 often, and then promote the mobility of waste liquid stoste, make it get into the purification operation of accomplishing the waste liquid in the subsequent cooling purification process better.
The utility model discloses one of the preferred embodiment, still be equipped with the electrically controlled device 15 that electronic on-off valve 13 links to each other, electrically controlled device 15 is connected with flow sensor 16, flow sensor 16 set up in circulating pump 14 intake end or go out the water end, in order to avoid cooling the problem that cooling effect reduces and take place to overflow in solarization pond 9 after the cooling purified water cools off many times, through setting up flow sensor 16 at circulating pump 14, calculate cooling cycle's total flow, in electrically controlled device 15-adopt common singlechip electrically controlled structure can-set up corresponding rated flow, make when the flow reaches the upper limit, electrically controlled device 15 automatic start-up electronic on-off valve 13 opens the procedure of draining, ensure that whole purifier's operation is normal, especially the normal operating of cooling stoste procedure.
The utility model discloses the beneficial effect who has lies in: in practical application, the utility model discloses can carry out effectual purification treatment with the produced sewage of industry, cooling structure design is more reasonable, has improved waste liquid purification efficiency, has alleviated the blowdown pressure of industrial sewage, has reduced the maintenance cost, has realized more green's mode of production.
The foregoing is only a preferred embodiment of the present invention, and it should be noted that, for those skilled in the art, a plurality of improvements and decorations can be made without departing from the principle of the present invention, and these improvements and decorations should also be regarded as the protection scope of the present invention.
Claims (6)
1. The industrial waste liquid purifying device is characterized in that a cooling pipe group is arranged between the raw liquid barrel and the liquid inlet pipe, the cooling pipe group comprises a raw liquid net pipe connected between the liquid inlet pipe and the raw liquid barrel and a cooling liquid net pipe which is inserted between the raw liquid net pipe and closely attached to the raw liquid net pipe, the water inlet end and the water outlet end of the cooling liquid net pipe are both connected with a circulating pump communicated with the exposure pool, and the liquid outlet pipe is connected with the exposure pool and is provided with an electric on-off valve.
2. The industrial waste liquid purification device of claim 1, wherein the height of the water inlet end of the stock solution pipe network is lower than that of the water outlet end, and the height of the water inlet end of the cooling liquid pipe network is higher than that of the water outlet end.
3. The industrial waste liquid purification device according to claim 2, wherein a straight-through penetrating pipeline which is wound through the bottoms of the sedimentation tank and the biological bacteria tank is arranged between the water outlet end of the cooling liquid pipe network and the circulating pump.
4. The industrial waste liquid purification device according to claim 1, wherein the bottom of the raw liquid barrel is provided with a plurality of flat plate-shaped conducting parts, a ventilating duct communicated with the outside is arranged between the conducting parts, and all the conducting parts are converged at the liquid inlet end of the high-pressure pump.
5. The industrial waste liquid purification apparatus according to claim 4, wherein the conduction part is a table-shaped body having a wide top and a narrow bottom, and a stirring blade connected to a drive motor outside the raw liquid tank is provided in the conduction part.
6. The industrial waste liquid purification device according to claim 1, further comprising an electric control device connected to the electric on-off valve, wherein the electric control device is connected to a flow sensor, and the flow sensor is disposed at a water inlet end or a water outlet end of the circulating pump.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN202221266544.9U CN217265341U (en) | 2022-05-24 | 2022-05-24 | Industrial waste liquid purification device |
Applications Claiming Priority (1)
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CN202221266544.9U CN217265341U (en) | 2022-05-24 | 2022-05-24 | Industrial waste liquid purification device |
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CN217265341U true CN217265341U (en) | 2022-08-23 |
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CN202221266544.9U Active CN217265341U (en) | 2022-05-24 | 2022-05-24 | Industrial waste liquid purification device |
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2022
- 2022-05-24 CN CN202221266544.9U patent/CN217265341U/en active Active
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