CN112340927A - Waste water treatment system for powder coating process - Google Patents
Waste water treatment system for powder coating process Download PDFInfo
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- CN112340927A CN112340927A CN202011333056.0A CN202011333056A CN112340927A CN 112340927 A CN112340927 A CN 112340927A CN 202011333056 A CN202011333056 A CN 202011333056A CN 112340927 A CN112340927 A CN 112340927A
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- 239000000843 powder Substances 0.000 title claims abstract description 38
- 238000000576 coating method Methods 0.000 title claims abstract description 29
- 238000004065 wastewater treatment Methods 0.000 title claims abstract description 21
- 239000003814 drug Substances 0.000 claims abstract description 29
- 238000004062 sedimentation Methods 0.000 claims abstract description 19
- 239000011248 coating agent Substances 0.000 claims abstract description 10
- 238000007789 sealing Methods 0.000 claims abstract description 10
- 238000005243 fluidization Methods 0.000 claims abstract description 7
- 238000005188 flotation Methods 0.000 claims abstract description 6
- 238000002156 mixing Methods 0.000 claims description 13
- 238000001556 precipitation Methods 0.000 claims description 11
- 238000009434 installation Methods 0.000 claims description 5
- 238000001179 sorption measurement Methods 0.000 claims description 5
- 238000007790 scraping Methods 0.000 claims description 4
- 229920000742 Cotton Polymers 0.000 claims description 3
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- 235000019322 gelatine Nutrition 0.000 claims 1
- 235000011852 gelatine desserts Nutrition 0.000 claims 1
- 238000005189 flocculation Methods 0.000 abstract description 11
- 230000016615 flocculation Effects 0.000 abstract description 11
- 238000006243 chemical reaction Methods 0.000 abstract description 8
- 239000002351 wastewater Substances 0.000 description 32
- 239000007788 liquid Substances 0.000 description 17
- 239000012535 impurity Substances 0.000 description 16
- 239000013049 sediment Substances 0.000 description 16
- 238000007667 floating Methods 0.000 description 10
- 230000000694 effects Effects 0.000 description 8
- 239000010802 sludge Substances 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 239000002893 slag Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 6
- 238000005507 spraying Methods 0.000 description 6
- 239000010865 sewage Substances 0.000 description 4
- 239000003638 chemical reducing agent Substances 0.000 description 3
- 239000000701 coagulant Substances 0.000 description 3
- 238000007599 discharging Methods 0.000 description 3
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Classifications
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- 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
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
- C02F11/122—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering using filter presses
-
- 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
- C02F1/24—Treatment of water, waste water, or sewage by flotation
-
- 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
- C02F1/48—Treatment of water, waste water, or sewage with magnetic or electric fields
-
- 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
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
-
- 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
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
- C02F1/56—Macromolecular compounds
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The invention relates to the technical field of powder coating, in particular to a wastewater treatment system for a powder coating process. The integrated air flotation and sedimentation tank comprises a tank body and a column body provided with a sealing plate; the cylinder body comprises an outer shell and an inner shell, the wall of the inner shell is provided with an air hole, the bottom plate of the pool body is provided with an air inlet, the air cavity is provided with a mounting ring and a connecting shaft, the outer ring surface of the mounting ring is connected with the inner wall of the inner shell through a plurality of single rods, the connecting shaft is connected with the inner ring surface of the mounting ring through a rotating bearing, one end of the connecting shaft, which is close to the air inlet, is provided with a fan blade, and the other; a fluidization plate is arranged between the outer shell and the inner shell to divide a cavity between the outer shell and the inner shell into a medicament cavity and an electrostatic cavity, the medicament cavity is loaded with medicinal powder, and the electrostatic cavity is provided with an electrostatic generator; a plurality of through holes are formed in the wall of the outer shell barrel, and first one-way plates are covered in the through holes. The application has the characteristics of quick flocculation and complete reaction.
Description
Technical Field
The invention relates to the technical field of powder coating, in particular to a wastewater treatment system for a powder coating process.
Background
Powder coating is to spray powder coating on the surface of a workpiece by using powder spraying equipment, and the powder is uniformly adsorbed on the surface of the workpiece under the action of static electricity to form a powdery coating which is baked at high temperature, leveled and cured to form final coatings with different effects (different types of effects of the powder coating); the spraying effect of the powder spraying is superior to that of a paint spraying process in the aspects of mechanical strength, adhesive force, corrosion resistance, aging resistance and the like, and the cost is also lower than that of the paint spraying with the same effect.
The wastewater generated in the coating process is mainly divided into pretreatment wastewater, electrophoresis wastewater and paint spraying wastewater. Patent document No. CN205933486U discloses such a coating wastewater treatment device, which comprises an oil separation tank, an adjusting tank, a combined sedimentation tank, an air flotation tank, a sand filter and a carbon filter which are connected in sequence through a pipeline, wherein sludge generated by the combined sedimentation tank flows into a sludge drying tank through the pipeline, and filtrate generated by the sludge drying tank flows into the adjusting tank through the pipeline. The application uses the air floatation tank and the combined sedimentation tank separately, increases operation steps and has higher operation cost. Meanwhile, the use principle of the traditional air floatation tank is as follows: firstly, electrically connecting an aerator and a driving motor with an external power supply, then conveying wastewater to the inside of an aeration cavity through a water inlet pipe, then opening the aerator to generate a large amount of micro bubbles, fully mixing the micro bubbles and the wastewater, simultaneously entering the inside of a reaction cavity through a water outlet, then adding a coagulant into the inside of the reaction cavity through a slag scraping operation port to enable the coagulant to perform flocculation reaction with impurities in the wastewater, enabling the generated floccule and solid suspended matters contained in the wastewater to continuously rise and float on the surface of the liquid through the large amount of micro bubbles, then opening the driving motor to drive a slag scraper to scrape the floccule and the solid suspended matters floating on the surface of the liquid, discharging the flocculate and the solid suspended matters through a sewage discharge plate and a sewage discharge port, and finally discharging the residual water; when the existing air floatation tank is used, the driving chain is often loosened in the use process of the slag scraper, so that the slag scraping operation of the slag scraper is influenced, and the use reliability of the slag scraper is low; meanwhile, the added coagulant can not be fully mixed with the wastewater for reaction, so that the wastewater is not flocculated completely and the use limitation is high.
Disclosure of Invention
The invention aims to solve the problems and provides a wastewater treatment system for a powder coating process.
The technical scheme for solving the problems is that the invention provides a wastewater treatment system for a powder coating process, which comprises an air floatation and sedimentation integrated tank, wherein the air floatation and sedimentation integrated tank comprises a tank body and a column body, wherein the column body is arranged in the center of an inner cavity of the tank body, one end of the column body is connected with the inner bottom surface of the tank body, and the other end of the column body is provided with a sealing plate; the cylinder comprises an outer shell and an inner shell, an air cavity is formed in the inner cavity of the inner shell, an air hole is formed in the wall of the inner shell, an air inlet is formed in the part, located in the air cavity, of the bottom plate of the pool body, an installation ring and a connecting shaft are arranged in the air cavity, the outer ring surface of the installation ring is connected with the inner wall of the inner shell through a plurality of single rods, the connecting shaft is connected with the inner ring surface of the installation ring through a rotating bearing, a fan blade used for receiving air flow to rotate is arranged at one end, close to the air inlet, of the connecting shaft, the other end of the connecting shaft penetrates through the sealing plate and is provided with an air; a fluidization plate is arranged between the outer shell and the inner shell to divide a cavity between the outer shell and the inner shell into a medicament cavity and an electrostatic cavity, the medicament cavity is loaded with medicinal powder, and the electrostatic cavity is provided with an electrostatic generator; the wall of the shell barrel is provided with a plurality of through holes, the through holes are covered with first one-way plates, one end of each first one-way plate is connected with the outer side face of the shell barrel, the other end of each first one-way plate is attached to the outer side face of the shell barrel, and the body of each first one-way plate covers the through holes.
Preferably, the inner diameter of the through hole is smaller than the inner diameter of the air hole.
Preferably, a receiving plate for collecting the air-floated objects collected by the air-floated scraper is arranged in the tank body.
Preferably, one surface of the bearing plate close to the inner bottom surface of the tank body is provided with adsorption cotton.
Preferably, the receiving plate is connected to the lifter.
Preferably, a circular truncated cone-shaped precipitation guide plate is further arranged in the tank body, the upper end of the circular truncated cone of the precipitation guide plate is sleeved on the column body, and the lower end of the circular truncated cone is connected with the side face of the tank body; a sedimentation outlet is arranged on the side surface of the tank body; and activated sludge is paved on the surface of the precipitation guide plate.
Preferably, the through hole comprises an impact inclined hole positioned in the electrostatic cavity, and the impact inclined hole is parallel to a precipitation guide plate bus bar on the same vertical surface with the impact inclined hole.
Preferably, the through hole further comprises a material mixing inclined hole located in the medicament cavity, the material mixing inclined hole comprises an inner end close to the inner shell and an outer end far away from the inner shell, and the horizontal plane of the outer end is higher than that of the inner end.
Preferably, the air holes are covered with waterproof breathable films.
Preferably, the air holes are covered with second one-way plates, one end of each second one-way plate is connected with the outer side surface of the inner shell, the other end of each second one-way plate is attached to the outer side surface of the inner shell, and the body of each second one-way plate covers the air hole.
The invention has the beneficial effects that:
1. this application is through the setting in fan blade and medicament chamber, and at the in-process that utilizes fan blade admission flow, the air current through the medicament chamber, smuggle partly medicament secretly and get into the pond internal with the waste water and mix, the in-process that forms the microbubble at air current and waste water has accomplished waste water and medicament promptly mixes the flocculation, then the microbubble directly drives this part flocculation impurity and rises to the liquid level, and flocculation effect is good.
2. Meanwhile, the air-flotation scraper blade is connected with the air-flotation scraper blade, the process of mixing air, liquid and medicine is combined with the process of scraping impurities, and the larger the air inflow is, the more the generated micro bubbles are, and the more the micro bubbles drive the floating flocculation impurities to float; and the air input is bigger, and the rotational speed of air supporting scraper blade is also bigger, consequently can effectively strike off more flocculation impurity.
3. Meanwhile, the medicament powder is suspended in the medicament cavity in an electrified way through the electrostatic generator, so that on one hand, airflow from each air hole can drive a part of medicament to enter the tank body; on the other hand, the medicament with the charges can effectively adsorb impurities which can not generate flocculation reaction besides flocculation reaction on the impurities; in addition, after the air current with charges enters the wastewater, the activity of activated sludge on the precipitation guide plate can be improved, and bacteria, fungi, algae and other microorganisms in the activated sludge can combine heavy metals in the wastewater to the surface of cell walls through electrostatic adsorption, so that the wastewater treatment effect is further improved.
4. The air floatation scraper blade of the utility model works by means of rotation of the fan blade, is not provided with a connecting structure such as a transmission chain, can operate as long as the air inlet is filled with air flow, and has high operation reliability.
5. This application is through the setting of strikeing the inclined hole for the air current has partly can strike the direction of deposiing the export to the sediment of sediment on the sediment baffle, and the help is deposiing and is exported from deposiing the export and discharge.
Drawings
FIG. 1 is a schematic view showing the structure of a flotation-precipitation integrated tank in a wastewater treatment system for a powder coating process;
in the figure: the device comprises a tank body 1, an air inlet 11, a bearing plate 12, a precipitation guide plate 13, a precipitation outlet 14, a column body 2, an outer shell barrel 21, a fluidization plate 211, an electrostatic generator 212, a through hole 213, an impact inclined hole 2131, a material mixing inclined hole 2132, a first one-way plate 214, an inner shell barrel 22, an air hole 221, a mounting ring 222, a connecting shaft 223, a single rod 224, fan blades 225, an air floatation scraper 226 and a sealing plate 23.
Detailed Description
The following are specific embodiments of the present invention and are further described with reference to the accompanying drawings, but the present invention is not limited to these embodiments.
A wastewater treatment system for a powder coating process sequentially comprises an adjusting tank, an air floatation and sedimentation integrated tank, a neutralization reaction tank, a hydroxyl solution generation system, a filtering adsorber and a clean water recycling tank. When in use, the coating wastewater firstly passes through a regulating tank and enters an air floatation and sedimentation integrated tank, and water is discharged after air floatation and sedimentation; then, feeding the wastewater into a neutralization reaction tank, and adjusting the pH value of the wastewater through reaction with a reagent to ensure that the pH value of the wastewater is in a range of 6.0-9.0; then the wastewater after neutralization treatment is sent into a hydroxyl solution generating system by a sewage circulating pump, and OH and O generated by a strong ionization discharge device in the hydroxyl solution generating system3、O2+、 O2-、H2O+、H2O2And HO2Active particles for removing OH and O under the action of jet device and sewage circulating pump3、O2+、 O2-、H2O+、H2O2And HO2Injecting active particles into a gas-liquid mixing device, mixing with the wastewater to generate OH solution, and oxidizing and degrading the coating wastewater; the waste water after oxidative degradation flows into a gas-liquid separation device for gas-liquid separation, and meanwhile, undissolved O is separated2And O3Discharging; finally, inputting the treated wastewater into a filtering adsorber, and filtering the wastewater to enter a clear water recycling pool; meanwhile, scum and sediment collected in the air floatation and sedimentation integrated tank are dehydrated by a box type filter press, so that the water content of sludge is below 80%, and supernatant liquid flows back to the regulating tank.
As shown in fig. 1, the air flotation and sedimentation integrated tank comprises a tank body 1 and a column body 2 which is arranged in the center of an inner cavity of the tank body 1, one end of which is connected with the inner bottom surface of the tank body 1, and the other end of which is provided with a sealing plate 23; the column body 2 comprises an outer shell 21 and an inner shell 22, an air cavity is formed in the inner cavity of the inner shell 22, an air hole 221 is formed in the wall of the inner shell 22, and an air inlet 11 is formed in the part, located in the air cavity, of the bottom plate of the pool body 1. A fluidization plate 211 is arranged between the outer shell 21 and the inner shell 22 to divide a cavity between the outer shell 21 and the inner shell 22 into a medicament cavity and an electrostatic cavity, the medicament cavity is loaded with medicinal powder, and the electrostatic cavity is provided with an electrostatic generator 212; the wall of the housing tube 21 is provided with a plurality of through holes 213, the through holes 213 are covered with first one-way plates 214, one end of each first one-way plate 214 is connected with the outer side surface of the housing tube 21, the other end of each first one-way plate 214 is attached to the outer side surface of the housing tube 21, and the body of each first one-way plate covers the through holes 213. In addition, in order to avoid the flow of the medicine powder from the medicine cavity to the air cavity, the air holes 221 may be covered with waterproof and breathable films, or the air holes 221 may be covered with second one-way plates, one end of each second one-way plate is connected with the outer side surface of the inner shell 22, and the other end of each second one-way plate is attached to the outer side surface of the inner shell 22 and covers the air hole 221.
During the use, the air current gets into the wind chamber from air intake 11, then gets into medicament chamber and static chamber through waterproof ventilated membrane or second one-way plate from wind hole 221. The electrostatic generator in the electrostatic cavity charges the airflow, and then the airflow enters the medicament cavity through the fluidization plate 211, so that the medicinal powder loaded on the fluidization plate 211 is charged and uniformly fluidized under the charged airflow, and the medicinal powder is uniformly suspended in the medicament cavity under the action of static electricity. Then the airflow entering the medicament cavity drives the suspended medicinal powder to enter the through hole 213, and the first one-way plate 214 is opened under the action of the wind force, so that the airflow with the medicinal powder enters the tank body 1 to be mixed, flocculated and adsorbed with the wastewater. Meanwhile, the air flow entering the tank body 1 is mixed with the wastewater to form micro bubbles.
The powder comprises polyaluminium chloride, polyacrylamide and active strains, coagulation and flocculation of impurities in the wastewater are completed through the polyaluminium chloride and the polyacrylamide, and electrostatic adsorption of the impurities in the wastewater is completed through the active strains. The impurities which finish coagulation are naturally deposited at the bottom of the tank body 1, the impurities which finish flocculation rise to the liquid level along with the micro bubbles, and the adsorbed impurities are precipitated or floated according to the gravity of the impurities.
In order to increase the impact force of the air flow into the wastewater and increase the generation of micro bubbles, the inner diameter of the through hole 213 may be set smaller than the inner diameter of the wind hole 221. However, in order to avoid the impact of the airflow on the sediment at the bottom of the tank body 1, the sediment is stirred to be mixed with the wastewater again, so the through hole 213 includes a mixing inclined hole 2132 located in the chemical cavity, the mixing inclined hole 2132 includes an inner end close to the inner shell 22 and an outer end far away from the inner shell 22, and the horizontal plane of the outer end is higher than the horizontal plane of the inner end, so that the airflow is ejected towards the direction of the liquid surface. Based on this, in order to improve the degree of combination between the airflow and the powder in the medicament cavity, one end of the air hole 221 close to the medicament cavity is lower than the end far away from the medicament cavity, an air outlet of the air hole 221 close to the medicament cavity is located between air inlets of the two mixing inclined holes 2132, and meanwhile a stop plate is arranged at the top of the mixing inclined hole 2132 at the lower portion.
In order to remove floating impurities, in the present application, the air cavity is provided with a mounting ring 222 and a connecting shaft 223, an outer annular surface of the mounting ring 222 is connected with the inner wall of the inner shell 22 through a plurality of single rods 224, the connecting shaft 223 is connected with an inner annular surface of the mounting ring 222 through a rotating bearing, one end of the connecting shaft 223 near the air inlet 11 is provided with a fan blade 225 for receiving air flow to rotate, the other end of the connecting shaft 223 penetrates through the sealing plate 23 and is provided with an air floatation scraper 226, and the connecting shaft 223 is connected with the sealing plate 23 through the. When the air flow enters the air cavity from the air inlet 11, the fan blades 225 rotate, so as to drive the connecting shaft 223 and the air floating scraper 226 to rotate, so that the air floating scraper 226 can scrape off scum on the liquid level.
Generally, after scum is scraped, scum needs to be collected, so that a receiving plate 12 for collecting scum of air floatation objects collected by the air floatation scraper 226 is arranged in the tank body 1. The receiving surface of the receiving plate 12 is lower than the bottom surface of the air floating scraper 226, so that the air floating scraper 226 can scrape the scum onto the receiving plate 12. Meanwhile, as the receiving plate 12 shields a part of the liquid surface, the scum of the part of the liquid surface can not be collected by the air floatation scraper 26, and therefore, the surface of the receiving plate 12 close to the inner bottom surface of the tank body 1 is provided with adsorption cotton. Of course, any connecting member may be used to move the position of the receiving plate 12 on the liquid surface so as to avoid the receiving plate 12 blocking the floating slag, for example, a reducer (such as a planetary gear reducer) may be sleeved on the portion of the connecting shaft 223 outside the column 2, and the end of the receiving plate 13 is connected to the reducer so that the receiving plate 13 rotates along with the air floating scraper 226 in the same direction, but the rotation speed of the receiving plate 13 is less than the rotation speed of the air floating scraper 226.
After the receiving plate 12 collects a certain amount of scum, the scum on the receiving plate 12 needs to be disposed and then placed on the liquid level for utilization, and in this embodiment, the receiving plate 12 is connected with the lifting member, after the receiving plate 12 collects impurities, the receiving plate 12 drives the impurities to be lifted out of the water body through the lifting member, and after the treatment, the receiving plate 12 is placed on the liquid level. Meanwhile, the height of the receiving plate 12 in the wastewater can be adjusted according to the amount of the scum through the lifting piece, and the more scum is, the larger the distance between the receiving plate 12 and the liquid level is.
In order to remove the deposited sediment, in the embodiment, a circular truncated cone-shaped sediment guide plate 13 is further arranged in the tank body 1, the upper end of the circular truncated cone of the sediment guide plate 13 is sleeved on the column body 2, and the lower end of the circular truncated cone is connected with the side surface of the tank body 1; a sedimentation outlet 14 is arranged on the side surface of the tank body 1. After the sediment is deposited on the sediment guide 13, the sediment can slide down along the inclined side surface of the sediment guide to the sediment outlet 14 to be discharged. Meanwhile, for some sediments which are relatively high in viscosity and difficult to slide down to the sedimentation outlet 14, the through hole 213 comprises an impact inclined hole 2131 positioned in the electrostatic cavity, and the impact inclined hole 2131 is parallel to a generatrix of the sedimentation guide plate 13 on the same vertical plane, so that a part of airflow carries out targeted flushing on the sediments.
In addition, activated sludge can be paved on the surface of the precipitation guide plate 13, so that the wastewater treatment effect is further improved.
The specific embodiments described herein are merely illustrative of the spirit of the invention. Various modifications or additions may be made to the described embodiments or alternatives may be employed by those skilled in the art without departing from the spirit or ambit of the invention as defined in the appended claims.
Claims (10)
1. The utility model provides a waste water treatment system for powder coating technology which characterized in that: the air flotation and sedimentation integrated tank comprises a tank body (1) and a column body (2) which is arranged in the center of an inner cavity of the tank body (1), one end of the column body is connected with the inner bottom surface of the tank body (1), and the other end of the column body is provided with a sealing plate (23); the cylinder (2) comprises an outer shell (21) and an inner shell (22), an air cavity is formed in the inner cavity of the inner shell (22), the wall of the inner shell (22) is provided with an air hole (221), the part of the bottom plate of the tank body (1) positioned in the air cavity is provided with an air inlet (11), the wind cavity is provided with an installation ring (222) and a connecting shaft (223), the outer ring surface of the installation ring (222) is connected with the inner wall of the inner shell (22) through a plurality of single rods (224), the connecting shaft (223) is connected with the inner ring surface of the mounting ring (222) through a rotating bearing, one end of the connecting shaft (223) close to the air inlet (11) is provided with a fan blade (225) for receiving airflow to rotate, the other end of the connecting shaft passes through the sealing plate (23) and is provided with an air floatation scraper (226), the connecting shaft (223) is connected with the sealing plate (23) through a rotating bearing; a fluidization plate (211) is arranged between the outer shell cylinder (21) and the inner shell cylinder (22) to divide a cavity between the outer shell cylinder (21) and the inner shell cylinder (22) into a medicament cavity and an electrostatic cavity, the medicament cavity is loaded with medicinal powder, and the electrostatic cavity is provided with an electrostatic generator (212); the wall of the shell barrel (21) is provided with a plurality of through holes (213), the through holes (213) are covered with first one-way plates (214), one end of each first one-way plate (214) is connected with the outer side face of the shell barrel (21), the other end of each first one-way plate is attached to the outer side face of the shell barrel (21), and the body of each first one-way plate covers the through holes (213).
2. The wastewater treatment system for powder coating process according to claim 1, wherein: the inner diameter of the through hole (213) is smaller than that of the air hole (221).
3. The wastewater treatment system for powder coating process according to claim 1, wherein: a bearing plate (12) used for collecting the air-floated objects collected by the air-floated scraping plate (226) is arranged in the tank body (1).
4. The wastewater treatment system for powder coating process according to claim 3, wherein: and adsorption cotton is arranged on one surface of the bearing plate (12) close to the inner bottom surface of the tank body (1).
5. The wastewater treatment system for powder coating process according to claim 3, wherein: the bearing plate (12) is connected with the lifting piece.
6. The wastewater treatment system for powder coating process according to claim 1, wherein: a circular truncated cone-shaped sedimentation guide plate (13) is further arranged in the tank body (1), the upper end of the circular truncated cone of the sedimentation guide plate (13) is sleeved on the column body (2), and the lower end of the circular truncated cone is connected with the side face of the tank body (1); a sedimentation outlet (14) is arranged on the side surface of the tank body (1); active donkey-hide gelatin is laid on the surface of the precipitation guide plate (13).
7. The wastewater treatment system for powder coating process according to claim 6, wherein: the through hole (213) comprises an impact inclined hole (2131) positioned in the electrostatic cavity, and the impact inclined hole (2131) is parallel to a bus of the precipitation guide plate (13) which is positioned on the same vertical surface with the impact inclined hole.
8. The wastewater treatment system for powder coating process according to claim 7, wherein: the through hole (213) further comprises a mixing inclined hole (2132) positioned in the medicament cavity, the mixing inclined hole (2132) comprises an inner end close to the inner shell (22) and an outer end far away from the inner shell (22), and the horizontal plane of the outer end is higher than that of the inner end.
9. The wastewater treatment system for powder coating process according to claim 1, wherein: the air holes (221) are all covered with waterproof breathable films.
10. The wastewater treatment system for powder coating process according to claim 1, wherein: the air holes (221) are respectively covered with a second one-way plate, one end of each second one-way plate is connected with the outer side face of the inner shell (22), the other end of each second one-way plate is attached to the outer side face of the inner shell (22), and the body of each second one-way plate covers the air holes (221).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011333056.0A CN112340927A (en) | 2020-11-24 | 2020-11-24 | Waste water treatment system for powder coating process |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011333056.0A CN112340927A (en) | 2020-11-24 | 2020-11-24 | Waste water treatment system for powder coating process |
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| CN112340927A true CN112340927A (en) | 2021-02-09 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN202011333056.0A Pending CN112340927A (en) | 2020-11-24 | 2020-11-24 | Waste water treatment system for powder coating process |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN118324229A (en) * | 2024-05-15 | 2024-07-12 | 滨州盟威戴卡轮毂有限公司 | Hub coating sewage treatment system |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002186962A (en) * | 2000-12-21 | 2002-07-02 | Shigeru Yoshida | Pressurized whirl type floatation and separation wastewater treatment equipment |
| CN2562835Y (en) * | 2002-02-04 | 2003-07-30 | 张守政 | Pressure reducing self suction type gas float oil and water separator |
| CN202945077U (en) * | 2012-12-17 | 2013-05-22 | 成都源创环保工程有限公司 | Air floating device used in superficial layer |
| CN108483743A (en) * | 2018-05-25 | 2018-09-04 | 江苏大学 | A kind of coating wastewater processing system and method |
| CN215208959U (en) * | 2020-11-24 | 2021-12-17 | 浙江明泉工业装备科技有限公司 | Waste water treatment system for powder coating process |
-
2020
- 2020-11-24 CN CN202011333056.0A patent/CN112340927A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002186962A (en) * | 2000-12-21 | 2002-07-02 | Shigeru Yoshida | Pressurized whirl type floatation and separation wastewater treatment equipment |
| CN2562835Y (en) * | 2002-02-04 | 2003-07-30 | 张守政 | Pressure reducing self suction type gas float oil and water separator |
| CN202945077U (en) * | 2012-12-17 | 2013-05-22 | 成都源创环保工程有限公司 | Air floating device used in superficial layer |
| CN108483743A (en) * | 2018-05-25 | 2018-09-04 | 江苏大学 | A kind of coating wastewater processing system and method |
| CN215208959U (en) * | 2020-11-24 | 2021-12-17 | 浙江明泉工业装备科技有限公司 | Waste water treatment system for powder coating process |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN118324229A (en) * | 2024-05-15 | 2024-07-12 | 滨州盟威戴卡轮毂有限公司 | Hub coating sewage treatment system |
| CN118324229B (en) * | 2024-05-15 | 2024-10-29 | 滨州盟威戴卡轮毂有限公司 | Hub coating sewage treatment system |
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