CN113800697A - Electrophoresis wastewater multi-stage environment-friendly treatment equipment and treatment method thereof - Google Patents
Electrophoresis wastewater multi-stage environment-friendly treatment equipment and treatment method thereof Download PDFInfo
- Publication number
- CN113800697A CN113800697A CN202111192854.0A CN202111192854A CN113800697A CN 113800697 A CN113800697 A CN 113800697A CN 202111192854 A CN202111192854 A CN 202111192854A CN 113800697 A CN113800697 A CN 113800697A
- Authority
- CN
- China
- Prior art keywords
- wastewater
- storehouse
- bin
- flocculation
- gas
- 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.)
- Pending
Links
- 239000002351 wastewater Substances 0.000 title claims abstract description 92
- 238000001962 electrophoresis Methods 0.000 title claims abstract description 22
- 238000000034 method Methods 0.000 title claims abstract description 18
- 238000005189 flocculation Methods 0.000 claims abstract description 50
- 230000016615 flocculation Effects 0.000 claims abstract description 50
- 238000001914 filtration Methods 0.000 claims abstract description 44
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 28
- 239000008394 flocculating agent Substances 0.000 claims abstract description 26
- 238000001179 sorption measurement Methods 0.000 claims abstract description 21
- 239000002244 precipitate Substances 0.000 claims abstract description 20
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims abstract description 16
- 229910021645 metal ion Inorganic materials 0.000 claims abstract description 12
- 230000001954 sterilising effect Effects 0.000 claims abstract description 12
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 12
- 239000010452 phosphate Substances 0.000 claims abstract description 9
- 230000001105 regulatory effect Effects 0.000 claims abstract description 9
- 229910001463 metal phosphate Inorganic materials 0.000 claims abstract description 8
- 239000004094 surface-active agent Substances 0.000 claims abstract description 8
- 239000007788 liquid Substances 0.000 claims description 51
- 239000007789 gas Substances 0.000 claims description 37
- 239000002912 waste gas Substances 0.000 claims description 26
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 19
- 238000007599 discharging Methods 0.000 claims description 18
- 239000007921 spray Substances 0.000 claims description 16
- 238000006243 chemical reaction Methods 0.000 claims description 13
- 238000009434 installation Methods 0.000 claims description 12
- 238000005201 scrubbing Methods 0.000 claims description 12
- 239000006004 Quartz sand Substances 0.000 claims description 10
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 10
- 239000011347 resin Substances 0.000 claims description 10
- 229920005989 resin Polymers 0.000 claims description 10
- 239000004575 stone Substances 0.000 claims description 10
- 229910052799 carbon Inorganic materials 0.000 claims description 9
- -1 iron ions Chemical class 0.000 claims description 9
- 239000003513 alkali Substances 0.000 claims description 8
- 239000002585 base Substances 0.000 claims description 8
- 230000005484 gravity Effects 0.000 claims description 8
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 7
- 229910052742 iron Inorganic materials 0.000 claims description 7
- 238000005406 washing Methods 0.000 claims description 7
- 235000017166 Bambusa arundinacea Nutrition 0.000 claims description 6
- 235000017491 Bambusa tulda Nutrition 0.000 claims description 6
- 241001330002 Bambuseae Species 0.000 claims description 6
- 235000015334 Phyllostachys viridis Nutrition 0.000 claims description 6
- 239000011425 bamboo Substances 0.000 claims description 6
- 230000007613 environmental effect Effects 0.000 claims description 5
- 238000010521 absorption reaction Methods 0.000 claims description 4
- 239000002253 acid Substances 0.000 claims description 4
- 230000005540 biological transmission Effects 0.000 claims description 4
- 239000012530 fluid Substances 0.000 claims description 4
- 210000003437 trachea Anatomy 0.000 claims description 4
- 230000001276 controlling effect Effects 0.000 claims description 3
- 230000000249 desinfective effect Effects 0.000 claims description 3
- 230000001376 precipitating effect Effects 0.000 claims description 3
- 239000003795 chemical substances by application Substances 0.000 claims 3
- 239000011148 porous material Substances 0.000 abstract description 8
- 230000000694 effects Effects 0.000 abstract description 5
- 238000004065 wastewater treatment Methods 0.000 abstract description 2
- 235000021317 phosphate Nutrition 0.000 description 8
- 238000000746 purification Methods 0.000 description 5
- 229910019142 PO4 Inorganic materials 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 238000013475 authorization Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 231100000956 nontoxicity Toxicity 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 235000013547 stew Nutrition 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/302—Treatment of water, waste water, or sewage by irradiation with microwaves
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/105—Phosphorus compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
- C02F2101/203—Iron or iron compound
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/02—Odour removal or prevention of malodour
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
Abstract
The invention provides an electrophoresis wastewater multi-stage environment-friendly treatment device and a treatment method thereof, which relate to the technical field of wastewater treatment and comprise a regulating reservoir, a filtering bin, an adsorption bin, a sterilization bin and a storage pool, wherein the filtering bin is provided with a flocculation bin; the invention adjusts the PH of the waste water in the pool through the adjusting tank, removes suspended matters and surfactant in the water by adding flocculating agent into the flocculation bin to react, generates precipitate, then filters the waste water through the sieve pores of the filter cylinder, filters the precipitate in the filter cylinder, finally adsorbs organic matters, metal ions and phosphate away through the adsorption bin, removes chromaticity and smell, generates microwave by matching with a microwave generator, sterilizes the waste water in the transparent pipeline, and has better effect by multi-stage treatment.
Description
Technical Field
The invention relates to the technical field of wastewater treatment, in particular to an electrophoresis wastewater multistage environment-friendly treatment device and a treatment method thereof.
Background
The electrophoretic coating is a special coating forming method developed in recent years, has the characteristics of water solubility, no toxicity, easiness in automatic control and the like, and is widely applied to industries such as aluminum profiles, automobiles, electronics, building materials, hardware and the like; therefore, the electrophoretic wastewater is generated along with the generation of the electrophoretic wastewater, and becomes more widely-appearing industrial wastewater, the wastewater has the characteristics of multiple pollutant types and complex components, and if the black wastewater is directly discharged, the wastewater can cause serious pollution to the natural environment;
in the prior art, for example, the authorization publication No. CN211338881U discloses 'a multi-stage environmental protection treatment for electrophoresis wastewater', the arrangement of the liquid pump is favorable for realizing the circular flow of the wastewater in the liquid containing box, and further the circular purification treatment of the wastewater can be realized, active carbon is placed in the purification cylinder, and the purification treatment of the wastewater in the liquid containing box is realized by using the active carbon, however, in the above-mentioned technology, only the active carbon is used for treatment, the effect is not good, and the standard of wastewater purification can not be reached far, and in the prior art, some of the active carbon is added with coagulant and other chemicals for treatment, then simply fixed by a filter screen, the treatment mode has poor filtering effect on the generated precipitate and is easy to cause secondary pollution, therefore, the invention provides an electrophoresis wastewater multi-stage environment-friendly treatment device and a treatment method thereof to solve the problems in the prior art.
Disclosure of Invention
Aiming at the problems, the invention provides the electrophoresis wastewater multi-stage environment-friendly treatment equipment and the treatment method thereof, the electrophoresis wastewater multi-stage environment-friendly treatment equipment and the treatment method thereof carry out multi-stage treatment, the effect is better, and the standard of wastewater purification is achieved.
In order to realize the purpose of the invention, the invention is realized by the following technical scheme: a multi-stage environment-friendly treatment device for electrophoresis wastewater comprises an adjusting tank, a filtering bin, an adsorption bin, a sterilization bin and a storage tank, wherein the filtering bin is provided with a flocculation bin;
the top of crossing the filter house is equipped with the race ring, and the inboard rotation of race ring installs first cartridge filter, the inside bottom of crossing the filter house is rotated and is installed the second cartridge filter, the second cartridge filter cover is established the outside of first cartridge filter, the lower extreme intercommunication in flocculation storehouse has the spigot, and the spigot extends to the inside of first cartridge filter, be equipped with the valve on the spigot.
The further improvement lies in that: the utility model discloses a liquid storage tank, including equalizing basin, baffle, acidizing fluid and alkali lye, the inside of equalizing basin is equipped with the baffle, and the baffle is equipped with the multiunit and crisscross setting, one side of the inside of equalizing basin is equipped with acid-base sensor, and the top of equalizing basin is equipped with the support, be equipped with the liquid fill on the support, and the liquid fill is equipped with two sets ofly, two sets of the liquid fill is equipped with acidizing fluid and alkali lye respectively, be equipped with gravity sensor between liquid fill and the support, and the below intercommunication of liquid fill has the drain pipe, the output orientation of drain pipe the equalizing basin, be equipped with the solenoid valve on the drain pipe.
The further improvement lies in that: one side of crossing the filter house is equipped with first motor, and is connected with the belt between the output of first motor and the first cartridge filter, the inside bottom of crossing the filter house is equipped with the installation cavity, and is equipped with the second motor in the installation cavity, the output of second motor with the second cartridge filter is connected.
The further improvement lies in that: the outside of first cartridge filter is equipped with first sieve mesh, and first sieve mesh equidistance is equipped with the multiunit, the outside of second cartridge filter is equipped with the second sieve mesh, and second sieve mesh equidistance is equipped with the multiunit, the bore of second sieve mesh is less than the bore of first sieve mesh.
The further improvement lies in that: one side in flocculation storehouse is equipped with force (forcing) pump and flocculating agent box, the inside flocculating agent that is equipped with of flocculating agent box, the input and the flocculating agent box intercommunication of force (forcing) pump, and the output and the flocculation storehouse intercommunication of force (forcing) pump, the outside in flocculation storehouse is equipped with the heater.
The further improvement lies in that: the inside in absorption storehouse is equipped with the installation section of thick bamboo, and the inside of installation section of thick bamboo is equipped with quartz sand, active carbon, softening resin and medical stone ball from top to bottom in proper order.
The further improvement lies in that: the inside in storehouse of disinfecting is equipped with transparent pipeline, and transparent pipeline is equipped with the multiunit, the input and the absorption storehouse intercommunication of transparent pipeline, and the output and the reservoir intercommunication of transparent pipeline, disinfect and be equipped with microwave generator on the inside wall in storehouse.
The further improvement lies in that: the utility model discloses a flocculation storehouse, including flocculation storehouse, inlet, outlet, inlet, outlet, inlet, outlet, inlet, outlet, and outlet, and outlet, and a like are connected with, and a like.
A multi-stage environment-friendly treatment method for electrophoresis wastewater comprises the following steps:
the method comprises the following steps: pouring the electrophoretic wastewater to be treated into an adjusting tank, sensing the pH value of the electrophoretic wastewater by using an acid-base sensor, then opening a solenoid valve of a corresponding liquid bucket according to the pH value, discharging acid liquid or alkali liquid into the adjusting tank, controlling the discharge amount by using the numerical value of a gravity sensor, adjusting the pH value of the wastewater in the tank to 9, standing under an alkaline condition, and precipitating iron ions and phosphate ions to primarily remove metal ions and phosphate ions in water;
step two: starting a first liquid pump, discharging the wastewater into a flocculation bin, starting a pressure pump, discharging a flocculating agent in a flocculating agent box into the flocculation bin, and simultaneously starting a heater to provide reaction temperature, so that the wastewater reacts with the flocculating agent, suspended matters and a surfactant in the wastewater are removed, and precipitates are generated;
step three: opening a valve of the liquid discharging nozzle, discharging the wastewater into a filtering bin, driving a first filter cylinder to rotate by matching a first motor with a belt, driving a second filter cylinder to rotate by driving a second motor, performing secondary filtering on the wastewater by utilizing a first sieve pore and a second sieve pore, and filtering precipitates in the filter cylinders;
step four: starting a second liquid pump, discharging the wastewater into an adsorption bin, adsorbing organic matters, metal ions and phosphate by the wastewater through quartz sand, activated carbon, softening resin and medical stone balls, and removing chromaticity and smell;
step five: and the wastewater after adsorption treatment flows into the transparent pipeline, at this time, the microwave generator is started to generate microwaves, the wastewater in the transparent pipeline is sterilized, and after the sterilization, clean water flows into the storage pool to be stored.
The further improvement lies in that: and in the second step, waste gas is generated in the reaction process of the flocculation bin, at this time, the air pump is started to pump the waste gas into the gas filtering bin, the sieve plate is used for filtering the waste gas, the water pump is started simultaneously to send the scrubbing solution in the scrubbing solution tank into the spray pipe, the scrubbing solution is sprayed out from the spray head to wash the waste gas, and after the waste gas is washed, the gas is discharged from the gas outlet.
The invention has the beneficial effects that:
1. the invention adjusts the PH of the wastewater in the tank through the adjusting tank, and stands to cause iron ions and phosphate radical ions to generate precipitation, then adds a flocculating agent into the flocculation bin to generate reaction, removes suspended matters and surfactants in the water to generate precipitates, then filters the wastewater through sieve pores of the filter cartridge, filters the precipitates in the filter cartridge, finally adsorbs away organic matters, metal ions and phosphates through quartz sand, active carbon, softening resin and medical stone balls in the adsorption bin, removes chromaticity and smell, and generates microwaves by matching with a microwave generator to sterilize the wastewater in a transparent pipeline.
2. In the filtering process, the first motor is matched with the belt to drive the first filter cylinder to rotate, the second motor is used to drive the second filter cylinder to rotate, the first sieve pore and the second sieve pore are used for secondary filtering of wastewater, and precipitates generated by flocculation are filtered in the filter cylinders, so that secondary pollution is avoided.
3. According to the invention, waste gas generated in the reaction process of the flocculation bin is pumped into the gas filtering bin through the air pump, the waste gas is filtered by the sieve plate, and the gas washing solution in the gas washing solution tank is sent into the spray pipe by the water pump and sprayed out from the spray head to wash the waste gas, so that the waste gas is prevented from polluting the environment, and the device has an environment-friendly function.
Drawings
FIG. 1 is a front view of the present invention;
FIG. 2 is a schematic view of the interior of the filtration cartridge of the present invention;
FIG. 3 is a schematic view of a first filter cartridge of the present invention;
FIG. 4 is a schematic view of the interior of the adsorption and sterilization chambers of the present invention;
FIG. 5 is a schematic view of the interior of the air filtering silo of the present invention.
Wherein: 1. a regulating tank; 2. a filtering bin; 3. an adsorption bin; 4. a sterilization bin; 5. a storage tank; 6. a flocculation bin; 7. a first liquid pump; 8. a second liquid pump; 9. a bearing ring; 10. a first filter cartridge; 11. a second filter cartridge; 12. a liquid discharging nozzle; 13. a partition plate; 14. an acid-base sensor; 15. a support; 16. a liquid hopper; 17. a gravity sensor; 18. a liquid outlet pipe; 19. an electromagnetic valve; 20. a first motor; 21. a belt; 22. a second motor; 23. a first screen hole; 24. a second sieve pore; 25. a pressure pump; 26. a flocculating agent box; 27. a heater; 28. mounting the cylinder; 29. quartz sand; 30. activated carbon; 31. softening the resin; 32. medical stone balls; 33. a transparent conduit; 34. a microwave generator; 35. a gas filtering bin; 36. a sieve plate; 37. a scrubbing solution tank; 38. a water pump; 39. a nozzle; 40. a spray head; 41. an air inlet; 42. an air pump; 43. and an air outlet.
Detailed Description
In order to further understand the present invention, the following detailed description will be made with reference to the following examples, which are only used for explaining the present invention and are not to be construed as limiting the scope of the present invention.
Example one
According to the drawings of fig. 1, 2, 3, 4 and 5, the embodiment provides a multistage environment-friendly treatment device for electrophoresis wastewater, which comprises an adjusting tank 1, a filtering bin 2, an adsorption bin 3, a sterilization bin 4 and a storage tank 5, wherein the filtering bin 2 is provided with a flocculation bin 6, one side of the adjusting tank 1 is communicated with the flocculation bin 6 through a transmission pipe, the transmission pipe is provided with a first liquid pump 7, one side of the filtering bin 2 is communicated with the adsorption bin 3 through a liquid guide pipe, the liquid guide pipe is provided with a second liquid pump 8, the lower end of the adsorption bin 3 is communicated with the sterilization bin 4, and one side of the sterilization bin 4 is communicated with the storage tank 5;
the top of crossing filter house 2 is equipped with race ring 9, and race ring 9's inboard rotation installs first cartridge filter 10, the bottom of crossing filter house 2 inside is rotated and is installed second cartridge filter 11, the 11 covers of second cartridge filter are established the outside of first cartridge filter 10, the lower extreme intercommunication in flocculation storehouse 6 has spigot 12, and spigot 12 extends to the inside of first cartridge filter 10, be equipped with the valve on spigot 12. During the use, through equalizing basin 1, waste water PH in the equalizing basin, and it makes iron ion and phosphate radical ion produce the sediment to stew, produce the reaction through adding the flocculating agent in flocculation storehouse 6 next, get rid of aquatic suspended solid and surfactant, produce the precipitate, then filter waste water through the cartridge filter, filter the precipitate in the cartridge filter, adsorb away the organic matter through adsorption storehouse 3 at last, metal ion, phosphate, and get rid of colourity and smell, the cooperation is disinfected the storehouse 4 and is disinfected waste water, to sum up, multi-stage treatment, the effect is better.
The inside of equalizing basin 1 is equipped with baffle 13, and baffle 13 is equipped with the multiunit and crisscross setting, the inside one side of equalizing basin 1 is equipped with acid-base sensor 14, and the top of equalizing basin 1 is equipped with support 15, be equipped with liquid fill 16 on support 15, and liquid fill 16 is equipped with two sets ofly, and is two sets of liquid fill 16 is equipped with acidizing fluid and alkali lye respectively, be equipped with gravity sensor 17 between liquid fill 16 and the support 15, and the below intercommunication of liquid fill 16 has drain pipe 18, the output orientation of drain pipe 18 equalizing basin 1, be equipped with solenoid valve 19 on the drain pipe 18. When the device is used, electrophoretic wastewater to be treated is poured into the regulating reservoir 1, the pH value of the electrophoretic wastewater is sensed by the acid-base sensor 14, then the electromagnetic valve 19 of the corresponding liquid bucket 16 is opened according to the pH value, acid liquor or alkali liquor is discharged into the regulating reservoir 1, the discharge amount is controlled by the numerical value of the gravity sensor 17, the PH value of the wastewater in the regulating reservoir is regulated to 9, standing is carried out under the alkaline condition, iron ions and phosphate ions are precipitated, and metal ions and phosphate ions in the water are removed preliminarily.
One side of filtering storehouse 2 is equipped with first motor 20, and is connected with belt 21 between the output of first motor 20 and the first cartridge filter 10, the inside bottom of filtering storehouse 2 is equipped with the installation cavity, and is equipped with second motor 22 in the installation cavity, the output of second motor 22 with second cartridge filter 11 is connected. The outside of first cartridge filter 10 is equipped with first sieve mesh 23, and first sieve mesh 23 equidistance is equipped with the multiunit, the outside of second cartridge filter 11 is equipped with second sieve mesh 24, and second sieve mesh 24 equidistance is equipped with the multiunit, the bore of second sieve mesh 24 is less than the bore of first sieve mesh 23. During the use, open the valve of spigot 12, arrange into waste water and filter storehouse 2, it is rotatory to drive first cartridge filter 10 through first motor 20 cooperation belt 21, and it is rotatory to drive second cartridge filter 11 through second motor 22, utilizes first sieve mesh 23 and second sieve mesh 24 to carry out the secondary filter to waste water, filters the precipitate in the cartridge filter.
One side of flocculation storehouse 6 is equipped with force (forcing) pump 25 and flocculating agent box 26, the inside flocculating agent box 26 is equipped with the flocculating agent, the input and the flocculating agent box 26 intercommunication of force (forcing) pump 25, and force (forcing) pump 25's output and flocculation storehouse 6 intercommunication, the outside in flocculation storehouse 6 is equipped with heater 27. When the device is used, the first liquid pump 7 is started, wastewater is discharged into the flocculation bin 6, the pressurizing pump 25 is started, the flocculating agent in the flocculating agent box 26 is discharged into the flocculation bin 6, and the heater 27 is started to provide reaction temperature, so that the wastewater reacts with the flocculating agent, suspended matters in water and surfactant are removed, and precipitates are generated.
The inside of adsorbing the storehouse 3 is equipped with an installation section of thick bamboo 28, and the inside of installation section of thick bamboo 28 is equipped with quartz sand 29, active carbon 30, softening resin 31 and medical stone ball 32 from top to bottom in proper order. When the device is used, the second liquid pump 8 is started to discharge the wastewater into the adsorption bin 3, and the wastewater passes through the quartz sand 29, the activated carbon 30, the softening resin 31 and the medical stone balls 32 to be adsorbed with organic matters, metal ions and phosphate, and remove chromaticity and smell.
The inside in storehouse 4 of disinfecting is equipped with transparent pipeline 33, and transparent pipeline 33 is equipped with the multiunit, the input and the absorption storehouse 3 intercommunication of transparent pipeline 33, and the output and the reservoir 5 intercommunication of transparent pipeline 33, disinfect and be equipped with microwave generator 34 on the inside wall in storehouse 4. When the device is used, the wastewater after adsorption treatment flows into the transparent pipeline 33, at this time, the microwave generator 34 is started to generate microwaves to sterilize the wastewater in the transparent pipeline 33, and after the completion, clean water flows into the storage pool 5 for storage.
Example two
Referring to fig. 1, 2, 3, 4 and 5, this embodiment provides a multi-stage environmental protection treatment method for electrophoresis wastewater, comprising the following steps:
the method comprises the following steps: pouring the electrophoretic wastewater to be treated into an adjusting tank 1, sensing the pH value of the electrophoretic wastewater by using an acid-base sensor 14, then opening a corresponding electromagnetic valve 19 of a liquid hopper 16 according to the pH value, discharging acid liquid or alkali liquid into the adjusting tank 1, controlling the discharge amount by using the numerical value of a gravity sensor 17, adjusting the pH value of the wastewater in the tank to 9, standing under an alkaline condition, and precipitating iron ions and phosphate ions to primarily remove the metal ions and the phosphate ions in the water;
step two: starting the first liquid pump 7 to discharge wastewater into the flocculation bin 6, starting the pressure pump 25 to discharge a flocculating agent in the flocculating agent box 26 into the flocculation bin 6, simultaneously starting the heater 27 to provide reaction temperature so that the wastewater reacts with the flocculating agent to remove suspended matters and surfactants in water and generate precipitates, generating waste gas in the reaction process of the flocculation bin 6, starting the air pump 42 to pump the waste gas into the gas filtering bin 35 at the moment, filtering the waste gas by using the sieve plate 36, simultaneously starting the water pump 38 to send a gas washing solution in the gas washing solution pool 37 into the spray pipe 39, spraying the gas from the spray nozzle 40 to wash the waste gas, and discharging the gas from the gas outlet 43 after the gas washing is finished;
step three: opening a valve of the liquid discharging nozzle 12, discharging the wastewater into the filtering bin 2, driving the first filtering cylinder 10 to rotate by matching a first motor 20 with a belt 21, driving the second filtering cylinder 11 to rotate by matching a second motor 22, performing secondary filtering on the wastewater by utilizing the first sieve holes 23 and the second sieve holes 24, and filtering the precipitate in the filtering cylinder;
step four: starting a second liquid pump 8, discharging the wastewater into the adsorption bin 3, adsorbing organic matters, metal ions and phosphate by the wastewater through quartz sand 29, activated carbon 30, softening resin 31 and medical stone balls 32, and removing chromaticity and smell;
step five: the wastewater after the adsorption treatment flows into the transparent pipeline 33, at this time, the microwave generator 34 is started to generate microwaves, the wastewater in the transparent pipeline 33 is sterilized, and after the sterilization, clean water flows into the storage tank 5 for storage.
According to the invention, the PH of the wastewater in the tank is regulated through the regulating tank 1, the wastewater is kept stand to enable iron ions and phosphate ions to generate precipitates, then a flocculating agent is added into the flocculation bin 6 to generate a reaction, suspended matters and a surfactant in the water are removed to generate precipitates, then the wastewater is filtered through the sieve pores of the filter cartridge, the precipitates are filtered in the filter cartridge, finally, organic matters, metal ions and phosphate are adsorbed away through quartz sand 29, active carbon 30, softening resin 31 and medical stone balls 32 in the adsorption bin 3, chromaticity and odor are removed, microwaves are generated by matching with the microwave generator 34, and the wastewater in the transparent pipeline 33 is sterilized. And at filterable in-process, it is rotatory to drive first cartridge filter 10 through first motor 20 cooperation belt 21, drives second cartridge filter 11 through second motor 22 and rotates, utilizes first sieve mesh 23 and second sieve mesh 24 to carry out secondary filter to waste water, filters the precipitate that the flocculation produced in the cartridge filter, avoids secondary pollution. Simultaneously, through the air pump, with the in-process production waste gas suction of flocculation 6 reaction in storehouse and strain gas storehouse 35, utilize sieve 36 to filter waste gas to utilize water pump 38, send the scrubbing solution in scrubbing solution pond 37 into spray tube 39, spout from shower nozzle 40, wash waste gas, avoid waste gas pollution environment, have the function of environmental protection.
The foregoing illustrates and describes the principles, general features, and advantages of the present invention. It will be understood by those skilled in the art that the present invention is not limited to the embodiments described above, which are described in the specification and illustrated only to illustrate the principle of the present invention, but that various changes and modifications may be made therein without departing from the spirit and scope of the present invention, which fall within the scope of the invention as claimed. The scope of the invention is defined by the appended claims and equivalents thereof.
Claims (10)
1. The utility model provides a multistage environmental protection treatment equipment of electrophoresis waste water, includes equalizing basin (1), filters storehouse (2), adsorbs storehouse (3), disinfects storehouse (4) and reservoir (5), its characterized in that: a flocculation bin (6) is arranged on the filtering bin (2), one side of the regulating pool (1) is communicated with the flocculation bin (6) through a transmission pipe, a first liquid pump (7) is arranged on the transmission pipe, one side of the filtering bin (2) is communicated with the adsorption bin (3) through a liquid guide pipe, a second liquid pump (8) is arranged on the liquid guide pipe, the lower end of the adsorption bin (3) is communicated with the sterilization bin (4), and one side of the sterilization bin (4) is communicated with the storage pool (5);
the top of crossing filter house (2) is equipped with race ring (9), and the inboard rotation of race ring (9) installs first cartridge filter (10), the bottom of crossing filter house (2) inside is rotated and is installed second cartridge filter (11), second cartridge filter (11) cover is established the outside of first cartridge filter (10), the lower extreme intercommunication in flocculation storehouse (6) has spigot (12), and spigot (12) extend to the inside of first cartridge filter (10), be equipped with the valve on spigot (12).
2. The electrophoresis wastewater multi-stage environment-friendly treatment equipment as claimed in claim 1, wherein: the inside of equalizing basin (1) is equipped with baffle (13), and baffle (13) are equipped with the multiunit and crisscross the setting, the inside one side of equalizing basin (1) is equipped with acid-base sensor (14), and the top of equalizing basin (1) is equipped with support (15), be equipped with liquid fill (16) on support (15), and liquid fill (16) are equipped with two sets ofly, two sets of liquid fill (16) are equipped with acidizing fluid and alkali lye respectively, be equipped with gravity sensor (17) between liquid fill (16) and support (15), and the below intercommunication of liquid fill (16) has drain pipe (18), the output orientation of drain pipe (18) equalizing basin (1), be equipped with solenoid valve (19) on drain pipe (18).
3. The electrophoresis waste water multistage environment-friendly treatment device as claimed in claim 2, wherein: one side of filtering storehouse (2) is equipped with first motor (20), and is connected with belt (21) between the output of first motor (20) and first cartridge filter (10), the inside bottom of filtering storehouse (2) is equipped with the installation cavity, and is equipped with second motor (22) in the installation cavity, the output of second motor (22) with second cartridge filter (11) are connected.
4. The electrophoresis wastewater multi-stage environment-friendly treatment device as claimed in claim 3, wherein: the outside of first cartridge filter (10) is equipped with first sieve mesh (23), and first sieve mesh (23) equidistance is equipped with the multiunit, the outside of second cartridge filter (11) is equipped with second sieve mesh (24), and second sieve mesh (24) equidistance is equipped with the multiunit, the bore of second sieve mesh (24) is less than the bore of first sieve mesh (23).
5. The electrophoresis wastewater multi-stage environment-friendly treatment equipment as claimed in claim 4, wherein: one side in flocculation storehouse (6) is equipped with force (25) pump and flocculation agent box (26), the inside of flocculation agent box (26) is equipped with the flocculating agent, the input and the flocculation agent box (26) intercommunication of force (25), and the output and the flocculation storehouse (6) intercommunication of force (25), the outside in flocculation storehouse (6) is equipped with heater (27).
6. The electrophoresis waste water multistage environment-friendly treatment device as claimed in claim 5, wherein: the inside in absorption storehouse (3) is equipped with installation section of thick bamboo (28), and the inside of installation section of thick bamboo (28) is equipped with quartz sand (29), active carbon (30), softened resin (31) and medical stone ball (32) from top to bottom in proper order.
7. The electrophoresis wastewater multi-stage environment-friendly treatment equipment as claimed in claim 6, wherein: the inside in storehouse (4) of disinfecting is equipped with transparent pipeline (33), and transparent pipeline (33) are equipped with the multiunit, the input of transparent pipeline (33) with adsorb storehouse (3) intercommunication, and the output and the apotheca (5) intercommunication of transparent pipeline (33), disinfect and be equipped with microwave generator (34) on the inside wall in storehouse (4).
8. The multistage environmental protection treatment equipment for electrophoresis wastewater according to any one of claims 1 to 7, characterized in that: flocculation storehouse (6) are connected with and strain gas storehouse (35), strain the inside middle-end in gas storehouse (35) and be equipped with sieve (36), and strain the inside bottom in gas storehouse (35) and be equipped with scrubbing solution pond (37), the one side of straining gas storehouse (35) is equipped with water pump (38), and the input and scrubbing solution pond (37) intercommunication of water pump (38), the output of water pump (38) is equipped with spray tube (39), the output of spray tube (39) extends to the inside in flocculation storehouse (6) and is equipped with shower nozzle (40), the below of straining gas storehouse (35) one side is equipped with air inlet (41), and air inlet (41) are through trachea and flocculation storehouse (6) intercommunication, be equipped with air pump (42) on the trachea, the top intercommunication of straining gas storehouse (35) has gas outlet (43).
9. The multistage environment-friendly treatment method for electrophoresis wastewater is characterized by comprising the following steps:
the method comprises the following steps: pouring electrophoretic wastewater to be treated into an adjusting tank (1), sensing the pH value of the electrophoretic wastewater by using an acid-base sensor (14), then opening a solenoid valve (19) of a corresponding liquid hopper (16) according to the pH value, discharging acid liquor or alkali liquor into the adjusting tank (1), controlling the discharge amount by using the numerical value of a gravity sensor (17), adjusting the pH value of the wastewater in the adjusting tank to 9, standing under an alkaline condition, precipitating iron ions and phosphate ions, and preliminarily removing metal ions and phosphate ions in the water;
step two: starting a first liquid pump (7), discharging the wastewater into a flocculation bin (6), starting a pressure pump (25), discharging a flocculating agent in a flocculating agent box (26) into the flocculation bin (6), and simultaneously starting a heater (27) to provide a reaction temperature, so that the wastewater reacts with the flocculating agent, suspended matters and a surfactant in the water are removed, and precipitates are generated;
step three: opening a valve of the liquid discharging nozzle (12), discharging the wastewater into the filtering bin (2), driving the first filtering cylinder (10) to rotate by matching a first motor (20) with a belt (21), driving the second filtering cylinder (11) to rotate by matching a second motor (22), performing secondary filtering on the wastewater by utilizing the first sieve holes (23) and the second sieve holes (24), and filtering the precipitate in the filtering cylinder;
step four: starting a second liquid pump (8), discharging the wastewater into an adsorption bin (3), and adsorbing organic matters, metal ions and phosphate by the wastewater through quartz sand (29), activated carbon (30), softening resin (31) and medical stone balls (32) to remove chromaticity and smell;
step five: the wastewater after the adsorption treatment flows into the transparent pipeline (33), at this time, the microwave generator (34) is started to generate microwaves, the wastewater in the transparent pipeline (33) is sterilized, and after the sterilization, clean water flows into the storage pool (5) for storage.
10. The multistage environment-friendly treatment method for electrophoresis wastewater according to claim 9, characterized in that: in the second step, in the reaction process of the flocculation bin (6), waste gas is generated, at this time, the air pump (42) is started, the waste gas is pumped into the gas filtering bin (35), the waste gas is filtered by the sieve plate (36), the water pump (38) is started simultaneously, the gas washing solution in the gas washing solution pool (37) is sent into the spray pipe (39) and sprayed out from the spray head (40), the waste gas is washed, and after the gas is discharged from the gas outlet (43).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202111192854.0A CN113800697A (en) | 2021-10-13 | 2021-10-13 | Electrophoresis wastewater multi-stage environment-friendly treatment equipment and treatment method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202111192854.0A CN113800697A (en) | 2021-10-13 | 2021-10-13 | Electrophoresis wastewater multi-stage environment-friendly treatment equipment and treatment method thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN113800697A true CN113800697A (en) | 2021-12-17 |
Family
ID=78897689
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202111192854.0A Pending CN113800697A (en) | 2021-10-13 | 2021-10-13 | Electrophoresis wastewater multi-stage environment-friendly treatment equipment and treatment method thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN113800697A (en) |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201189445Y (en) * | 2008-03-17 | 2009-02-04 | 陈显忠 | Waste gas treatment device |
| CN201264923Y (en) * | 2008-08-06 | 2009-07-01 | 王庆凯 | Microwave treatment device for wastewater |
| CN107188344A (en) * | 2017-05-10 | 2017-09-22 | 安阳工学院 | A kind of sewage-treatment plant and sewage water treatment method |
| CN208684681U (en) * | 2018-05-30 | 2019-04-02 | 幸南（丹阳）涂装工业有限公司 | A kind of coating sewage discharge processing equipment |
| CN210085201U (en) * | 2019-04-03 | 2020-02-18 | 刘广荣 | Sewage treatment device capable of recycling |
| CN211813871U (en) * | 2020-03-19 | 2020-10-30 | 朱博 | Recovery unit for treating automobile coating wastewater |
| CN216073423U (en) * | 2021-10-13 | 2022-03-18 | 浙江明泉工业装备科技有限公司 | Multistage environmental protection treatment equipment of electrophoresis waste water |
-
2021
- 2021-10-13 CN CN202111192854.0A patent/CN113800697A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201189445Y (en) * | 2008-03-17 | 2009-02-04 | 陈显忠 | Waste gas treatment device |
| CN201264923Y (en) * | 2008-08-06 | 2009-07-01 | 王庆凯 | Microwave treatment device for wastewater |
| CN107188344A (en) * | 2017-05-10 | 2017-09-22 | 安阳工学院 | A kind of sewage-treatment plant and sewage water treatment method |
| CN208684681U (en) * | 2018-05-30 | 2019-04-02 | 幸南（丹阳）涂装工业有限公司 | A kind of coating sewage discharge processing equipment |
| CN210085201U (en) * | 2019-04-03 | 2020-02-18 | 刘广荣 | Sewage treatment device capable of recycling |
| CN211813871U (en) * | 2020-03-19 | 2020-10-30 | 朱博 | Recovery unit for treating automobile coating wastewater |
| CN216073423U (en) * | 2021-10-13 | 2022-03-18 | 浙江明泉工业装备科技有限公司 | Multistage environmental protection treatment equipment of electrophoresis waste water |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107487917A (en) | Continuous type free from extraneous odour sewage-treatment plant | |
| CN105481164B (en) | A kind of tobacco wastewater treatment process | |
| CN202046957U (en) | Full-automatic high-purity water producing system | |
| CN216073423U (en) | Multistage environmental protection treatment equipment of electrophoresis waste water | |
| CN111908680A (en) | Rural sewage treatment integration equipment is used to environmental protection with disinfection function | |
| KR20090111188A (en) | Discharged Water Treatment System and Method for Treating Discharged Water Using the Same | |
| CN202576131U (en) | Treating and recycling system for industrial ferruginous waste water | |
| CN113800697A (en) | Electrophoresis wastewater multi-stage environment-friendly treatment equipment and treatment method thereof | |
| CN207957995U (en) | A kind of reaction tank for grey water system | |
| CN208949049U (en) | A kind of industry plating sewage treating and recovering device | |
| KR101206477B1 (en) | Method for Reusing The Agricultural Water of Wastewater Effluent and Water of River Using The Agricultural Water Apparatus | |
| CN213708053U (en) | Inorganic wastewater treatment device | |
| CN213680164U (en) | Integrated sewage treatment system | |
| CN210438556U (en) | Self-circulation disinfection cabinet type pure water treatment equipment | |
| KR101206476B1 (en) | Apparatus for Agricultural Water Reusing Wastewater Effluent and Water of River | |
| CN207748963U (en) | A kind of sewage purifier | |
| CN207483553U (en) | The industrial sewage purification device of circular treatment | |
| WO2011122986A2 (en) | Hydrodynamic water cleaning method | |
| CN206901985U (en) | A kind of sewage-treatment plant | |
| CN211226734U (en) | Environment-friendly sewage treatment equipment | |
| CN206828275U (en) | A kind of disinfection of tap water processing unit | |
| CN215480292U (en) | Sewage treatment device with anti-blocking structure | |
| CN210656525U (en) | Reverse osmosis treatment device | |
| CN208327695U (en) | A kind of water treatment facilities with automatically cleaning and sterilizing function | |
| CN214167532U (en) | Drinking water purifying device capable of automatically backwashing through water flow |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination |