CN205635285U - High -efficient sewage treatment device of integration - Google Patents
High -efficient sewage treatment device of integration Download PDFInfo
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- CN205635285U CN205635285U CN201620477227.XU CN201620477227U CN205635285U CN 205635285 U CN205635285 U CN 205635285U CN 201620477227 U CN201620477227 U CN 201620477227U CN 205635285 U CN205635285 U CN 205635285U
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Abstract
The utility model discloses a high -efficient sewage treatment device of integration, including synthesizing box, equalizing basin, equipment room, sludge impoundment and sludge tihckener, sludge impoundment and sludge tihckener series connection are synthesized and are equipped with oxygen deficiency pond, two at least good oxygen pond, sedimentation tank, coagulating basin, flocculation basin, secondary clarifier and clean water basins in the box, and good oxygen pond, sedimentation tank, coagulating basin, secondary clarifier, clean water basin all are close to with the oxygen deficiency pond mutually, being equipped with first sludge pump in the sedimentation tank, being equipped with the second sludge pump in the secondary clarifier, first sludge pump and second sludge pump all are connected with the sludge impoundment, be equipped with latent dirty pump in the equalizing basin, stealthily dirty pump is connected with the oxygen deficiency pond. The utility model discloses it is little to have area, and it is integrated to be convenient for, and convenient operation can realize the management of full automatic operation, goes out that water quality of water is good, the running cost low, system impact resistance is strong, the mud volume is few, and degree of automation is high, has greatly to the development prospect in high concentration organic wastewater field.
Description
Technical field
This utility model relates to the technical field of sewage disposal, is specifically related to a kind of integrated high-efficiency sewage treatment device, it is adaptable to the subsequent treatment of anaerobic treatment, percolate, the industrial wastewater such as livestock-raising, papermaking, fermentation, leather, pharmacy.
Background technology
It is one of main Environmental Problems of facing of China that water pollutes, economic development along with industries such as China's industry, livestock-raising, leather, pharmacy, the quantity of wastewater effluent of every profession and trade is consequently increased, and the organic wastewater that sewage great majority are high concentration that the similar industries such as industry, livestock-raising, leather, pharmacy produce, the treatment of Organic Wastewater of these high concentrations is improper or not qualified discharge, meeting polluted surface water and subsoil water, the pollution of surface water and groundwater, workers and peasants' fish production certainly will be affected, directly or indirectly give the life of the people and healthy bring harm.In view of the significant damage of high concentrated organic wastewater, China progressively strengthens and prevents from water pollution administering, and obtains a series of gratifying achievement.Activated sludge process is the effective sewage water treatment method of a kind of application, also it is the sewage disposal technology of a great development prospect, this is embodied in its extensive adaptability to water quality and quantity, the flexile method of operation, good controlling and the setting by anaerobism or anoxic zone are allowed to have biological denitrificaion, the aspects such as the usefulness of dephosphorization, Activated Sludge Process can remove dissolved gum body and biodegradable Organic substance from sewage, and can be by the suspended solid of activated sludge absorption and some other material, inorganic salts also can be partially removed, similar industrial wastewater also can use Wastewater Treated by Activated Sludge Process.Started so far from 1914, over the nearlyest 30 years, scientific and technical personnel have carried out experimental study extensively and profoundly to the reaction mechanism of activated sludge process, important breakthrough is achieved at Environmental Engineering Microbiology, biochemical reaction kinetics theoretical side, the blindness that before thoroughly overcoming, people cause because of employing experience or semi-empirical approach in the design and operation of sewage biological treatment system, the engineering design making activated sludge process is more scientific and reasonable, can preferably predict and instruct the operational management of system simultaneously.Plural serial stage activated sludge process improves hydraulic detention time and sludge retention time, coagulating basin and coagulating basin and is connected in series and substantially increases solid-liquid separation efficiency, it is possible to obtain high-quality process water.
Utility model content
In order to solve above-mentioned technical problem, this utility model provides a kind of integrated high-efficiency sewage treatment device, effluent quality is good, operating cost is low, system impact resistance is strong, sludge quantity is few, automaticity is high, process for higher concentration organic wastewater, industrial wastewater has remarkable result, have that floor space is little, it is integrated, easy to operate to be easy to, it is possible to achieve fully automatic operation manages.
In order to achieve the above object, the technical solution of the utility model is: a kind of integrated high-efficiency sewage treatment device, including integrated cabinet, regulating reservoir, equipment room, sludge-tank and sludge concentration tank, sludge-tank is connected in series with sludge concentration tank, being provided with anoxic pond, at least two Aerobic Pond, sedimentation tank, coagulating basin, flocculation basin, final deposition pool and clear water reserviors in described integrated cabinet, Aerobic Pond, sedimentation tank, coagulating basin, final deposition pool, clear water reserviors are all close to mutually with anoxic pond；Being provided with aerating system and nitrification liquid reflux pump in described Aerobic Pond, nitrification liquid reflux pump is connected with anoxic pond；It is provided with the first sludge pump in described sedimentation tank, is provided with the second sludge pump, the first sludge pump and the second sludge pump in final deposition pool and is all connected with sludge-tank；Being provided with submersible sewage pump in described regulating reservoir, submersible sewage pump is connected with anoxic pond；Being provided with aerator, ozonator, PAM dosing tank, PAC dosing tank in described equipment room, aerator is connected with aerating system, and ozonator is connected with clear water reserviors, and PAM dosing tank is connected with flocculation basin, and PAC dosing tank is connected with coagulating basin.
Described integrated cabinet is round box, and anoxic pond is arranged on the center of integrated cabinet and for circular, and the annular section between integrated cabinet and anoxic pond has been sequentially connected in series Aerobic Pond, sedimentation tank, coagulating basin, flocculation basin, final deposition pool and clear water reserviors counterclockwise.
It is provided with the 3rd latent dirty blender inside described anoxic pond, in coagulating basin, is provided with the first latent dirty blender, in flocculation basin, be provided with the second latent dirty blender.
Described sedimentation tank is vertical sedimentation basin, is provided with central tube, reflecting plate, bucket and the first sludge pump in sedimentation tank, and the first sludge pump is connected with anoxic pond, and sludge reflux to anoxic pond, the first sludge pump are arranged in the bucket of sedimentation tank by the first sludge pump；Described final deposition pool is vertical sedimentation basin, is provided with central tube, reflecting plate, bucket and the second sludge pump in final deposition pool, and the second sludge pump is arranged in the bucket of final deposition pool.
The quantity of described Aerobic Pond is provided with 4, includes Aerobic Pond I, Aerobic Pond II, Aerobic Pond III and Aerobic Pond IV, it is equipped with aerating system in Aerobic Pond I, Aerobic Pond II, Aerobic Pond III and Aerobic Pond IV, being interconnected between aerating system, nitrification liquid reflux pump is located at the bottom of Aerobic Pond IV.
Top between described anoxic pond and Aerobic Pond I is provided with water hole, bottom between Aerobic Pond I and Aerobic Pond II is provided with water hole, top between Aerobic Pond II and Aerobic Pond III is provided with water hole, between Aerobic Pond III and Aerobic Pond IV, bottom is provided with water hole, Aerobic Pond IV is connected with the central tube of sedimentation tank by pipeline, top between sedimentation tank and coagulating basin is provided with water hole, it is provided with water hole bottom coagulating basin and flocculation basin, flocculation basin is connected with the central tube of final deposition pool by pipeline, and the top between final deposition pool and clear water reserviors is provided with water hole.
Being provided with sludge pump in described sludge-tank, sludge pump is connected with sludge concentration tank.
Described aerating system includes the gas pipeline being interconnected, and aerating system is separately positioned on Aerobic Pond I, Aerobic Pond II, Aerobic Pond III, the bottom of Aerobic Pond IV.
The quantity of described aerator and submersible sewage pump is equipped with two, and two aerators are connected in parallel, and two submersible sewage pumps are connected in parallel.
Being provided with liquid level controller in described regulating reservoir, liquid level controller, submersible sewage pump, the 3rd latent dirty blender, nitrification liquid reflux pump, the first sludge pump, the first latent dirty blender, the second latent dirty blender, the second sludge pump, PAM dosing tank, PAC dosing tank, ozonator, aerator, sludge pump are all connected with electric control system.
This utility model is connected in series four Aerobic Ponds, improve the sewage time of staying at Aerobic Pond, make sewage be fully contacted with activated sludge, the Aerobic Pond in each stage can create the environment of suitable different microorganisms growth, form different functional sections, strengthen organic removal；Coagulating basin is connected in series with flocculation basin, appropriate coagulant is added in coagulating basin, through sufficiently mixing, the stability making colloid is destroyed, and the polymer phase absorption after being situated between with coagulant water, granule is made to have flocculating property, and the purpose flocculated creates suitable hydraulics exactly, this granule with flocculating property is made to assemble in contacting with each other, to form bigger floccule body, substantially increase the deposition efficiency of final deposition pool, thus obtain the water outlet of high-quality, solve Traditional Environmental-protection equipment to carry out the effluent quality of sewage disposal and do not reach the problem that Treated sewage reusing requires.Outward appearance of the present utility model is the round box of carbon steel material, there is floor space little, it is easy to integrated, easy to operate, fully automatic operation management can be realized, effluent quality is good, operating cost is low, system impact resistance is strong, sludge quantity is few, and automaticity is high, has in high concentrated organic wastewater process field and arrives more greatly development prospect.
Accompanying drawing explanation
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, the accompanying drawing used required in embodiment or description of the prior art will be briefly described below, apparently, accompanying drawing in describing below is only embodiments more of the present utility model, for those of ordinary skill in the art, on the premise of not paying creative work, it is also possible to obtain other accompanying drawing according to these accompanying drawings.
Fig. 1 is pipeline distribution plane Fig. 1 of the present utility model.
Fig. 2 is pipeline distribution plane Fig. 2 of the present utility model.
In figure, 1 is integrated cabinet, 2 is anoxic pond, 3 is Aerobic Pond I, 4 is Aerobic Pond II, 5 is Aerobic Pond III, 6 is Aerobic Pond IV, 7 is sedimentation tank, 8 is coagulating basin, 9 is flocculation basin, 10 is final deposition pool, 11 is clear water reserviors, 12 is the 3rd latent dirty blender, 13 is aerating system, 14 is the first sludge pump, 15 is the second sludge pump, 16 is the first latent dirty blender, 17 is the second latent dirty blender, 18 is nitrification liquid reflux pump, 19 is regulating reservoir, 20 is submersible sewage pump, 21 is equipment room, 22 is PAM dosing tank, 23 is PAC dosing tank, 24 is ozonator, 25 is aerator, 26 is sludge-tank, 27 is sludge pump, 28 is sludge concentration tank.
Detailed description of the invention
Below in conjunction with the accompanying drawing in this utility model embodiment, the technical scheme in this utility model embodiment is clearly and completely described, it is clear that described embodiment is only a part of embodiment of this utility model rather than whole embodiments.Based on the embodiment in this utility model, the every other embodiment that those of ordinary skill in the art are obtained under not paying creative work premise, broadly fall into the scope of this utility model protection.
A kind of integrated high-efficiency sewage treatment device, including integrated cabinet 1, regulating reservoir 19, equipment room 21, sludge-tank 26 and sludge concentration tank 28, sludge-tank 26 is connected in series with sludge concentration tank 28.Integrated cabinet 1 is made up of carbon steel or stainless steel.Being provided with anoxic pond 2, at least two Aerobic Pond, sedimentation tank 7, coagulating basin 8, flocculation basin 9, final deposition pool 10 and clear water reserviors 11 in integrated cabinet 1, Aerobic Pond, sedimentation tank 7, coagulating basin 8, final deposition pool 10, clear water reserviors 11 are all close to anoxic pond 2 phase.Being provided with aerating system 13 and nitrification liquid reflux pump 18 in Aerobic Pond, nitrification liquid reflux pump 18 is connected with anoxic pond 2；Being provided with the first sludge pump 14 in described sedimentation tank 7, be provided with the second sludge pump 15 in final deposition pool 10, the first sludge pump 14 is all connected with sludge-tank 26 with the second sludge pump 15；Being provided with submersible sewage pump 20 in described regulating reservoir 19, submersible sewage pump 20 is connected with anoxic pond 2；Aerator 25, ozonator 24, PAM dosing tank 22, PAC dosing tank 23 it is provided with in described equipment room 21, aerator 25 is connected with aerating system 13, ozonator 24 is connected with clear water reserviors 11, and PAM dosing tank 22 is connected with flocculation basin 9, and PAC dosing tank 23 is connected with coagulating basin 8.
Preferably, as depicted in figs. 1 and 2, being provided with sludge pump 27 in sludge-tank 26, sludge pump 27 is connected with sludge concentration tank 28, and sludge-tank 26 is connected with sludge concentration tank 28 by sludge pump 27.The quantity of Aerobic Pond is provided with 4, including Aerobic Pond I 3, Aerobic Pond II 4, Aerobic Pond III 5 and Aerobic Pond IV 6.Nitrification liquid reflux pump 18 is located at the bottom of Aerobic Pond IV 6.Integrated cabinet 1 is round box, and anoxic pond 2 is arranged on the center of integrated cabinet 1 and for circular.Integrated cabinet 1 can be located at and also can be embedded in underground on the ground, when being embedded in underground, can be used for greening or other lands used above, it is not necessary to build a house heating and insulation.Annular section between integrated cabinet 1 and anoxic pond 2 has been sequentially connected in series Aerobic Pond I 3, Aerobic Pond II 4, Aerobic Pond III 5, Aerobic Pond IV 6, sedimentation tank 7, coagulating basin 8, flocculation basin 9, final deposition pool 10 and clear water reserviors 11 counterclockwise.
Preferably, anoxic pond 2 is internal is provided with the 3rd latent dirty blender 12, for being stirred the sewage in anoxic pond, accelerates its response speed.It is provided with the first latent dirty blender 16 in coagulating basin 8, for the sewage in coagulating basin is stirred, accelerates its response speed.It is provided with the second latent dirty blender 17 in flocculation basin 9, for the sewage in flocculation basin is stirred, accelerates its response speed.
Preferably, sedimentation tank 7 is vertical sedimentation basin, is provided with central tube, reflecting plate, bucket and the first sludge pump 14 in final deposition pool 10, and the first sludge pump 14 is connected with anoxic pond 2, first sludge pump 14 by sludge reflux to anoxic pond 2, the first sludge pump 14 is arranged in the bucket of sedimentation tank 7；Described final deposition pool 10 is vertical sedimentation basin, is provided with central tube, reflecting plate, bucket and the second sludge pump 15 in final deposition pool 10, and the second sludge pump 15 is placed in the bucket of final deposition pool 10.
Preferably, top between anoxic pond 2 and Aerobic Pond I 3 is provided with water hole, bottom between Aerobic Pond I 3 and Aerobic Pond II 4 is provided with water hole, top between Aerobic Pond II 4 and Aerobic Pond III 5 is provided with water hole, between Aerobic Pond III 5 and Aerobic Pond IV 6, bottom is provided with water hole, Aerobic Pond IV 6 is connected by the central tube of pipeline with sedimentation tank 7, top between sedimentation tank 7 and coagulating basin 8 is provided with water hole, it is provided with water hole bottom coagulating basin 8 and flocculation basin 9, flocculation basin 9 is connected by the central tube of pipeline with final deposition pool 10, top between final deposition pool 10 and clear water reserviors 11 is provided with water hole.It is equipped with aerating system 13 in Aerobic Pond I 3, Aerobic Pond II 4, Aerobic Pond III 5 and Aerobic Pond IV 6, is interconnected between aerating system 13.Aerating system 13 includes the gas pipeline being interconnected, aerating system 13 is arranged on the bottom of Aerobic Pond I 3, aerating system 13 is arranged on the bottom of Aerobic Pond II 4, and aerating system 13 is arranged on the bottom of Aerobic Pond III 5, and aerating system 13 is arranged on the bottom of Aerobic Pond IV 6.
The outlet of submersible sewage pump 20 is connected with anoxic pond 2, and the sewage lifting in regulating reservoir 19 is entered anoxic pond 2 by submersible sewage pump 20, and the latent dirty blender 12 of the 3rd in anoxic pond 2 makes the sewage of anoxic pond 2 be sufficiently mixed uniformly.The microorganism of anoxic pond 2 can be reduced to nitrogen the material of the Nitrates in the sewage of Aerobic Pond backflow, thus reaches the purpose of sewage water denitrification.Microorganism in Aerobic Pond I 3, Aerobic Pond II 4, Aerobic Pond III 5 and Aerobic Pond IV 6 can be oxidized to carbon dioxide and water the organic pollution in sewage, and ammonia nitrogen pollutant is oxidized to nitrate, is then refluxed for can being removed to anoxic pond 2.
The aerobic microbiological being present in activated sludge just can must work in the presence of having oxygen, by activated sludge particles absorption, on zoogleic surface, this is due to its huge specific surface area and polysaccharide emplastic to dirty organic pollutants, some larger molecular organicses are decomposed into small organic molecule under antibacterial exoenzyme effect simultaneously, aerating system 13 makes Aerobic Pond I 3, Aerobic Pond II 4, the sewage of Aerobic Pond III 5 and Aerobic Pond IV 6 can obtain enough dissolved oxygen, and prevent the suspended substance in pond from sinking, strengthen contacting of Organic substance and microorganism and dissolved oxygen in pond, thus microorganism is under conditions of having sufficient dissolved oxygen in ensureing pond, to oxygenolysis organic in sewage.Microorganism is under conditions of oxygen abundance, adsorb these Organic substances, and oxidation Decomposition, form carbon dioxide and water, the procreation propagation of part supply self, the result that activated sludge reaction is carried out, the Organic substance in sewage is degraded and is removed, activated sludge itself is multiplied growth, and sewage is then purified process.The outlet of the nitrification liquid reflux pump 18 in Aerobic Pond IV 6 is connected with anoxic pond 2, makes backflow nitrification liquid that nitration reaction to occur in anoxic pond 2, makes the nitrogen in water escape in a gaseous form, reach the purpose of denitrogenation, and denitrification can consume part COD simultaneously.
PAC dosing tank 23 adds appropriate PAC in coagulating basin 8, passes through sufficiently mixing, makes the stability of colloid be destroyed, and adsorbs with the polymer phase after coagulant water Jie, makes granule have flocculating property.PAM dosing tank 22 adds appropriate PAM in flocculation basin 9, makes this granule with flocculating property assemble in contacting with each other, and to form bigger floccule body, substantially increases the deposition efficiency of final deposition pool.
Preferably, the quantity of aerator 25 and submersible sewage pump 20 is equipped with two, and two aerators 25 are connected in parallel, and two submersible sewage pumps 20 are connected in parallel, and one of them use one is standby, improves its reliability.Aerator 25, ozonator 24, PAM dosing tank 22, PAC dosing tank 23 can adjust to optimum position according to practical situation in putting of equipment room 21.Ozonator 24 is connected with clear water reserviors 11, and the ozone that ozonator 24 produces has higher germicidal efficiency, plays an important role in wastewater disinfection, can kill virus and the spore of chlorine resistance, increases the dissolved oxygen in water and improves water quality.
Preferably, being provided with liquid level controller in regulating reservoir 19, the latent dirty blender 12 of liquid level controller, submersible sewage pump the 20, the 3rd, nitrification liquid reflux pump the 18, first sludge pump 14, first latent dirty blender the 17, second sludge pump 15 of latent dirty blender 16, second, PAM dosing tank 22, PAC dosing tank 23, ozonator 24, aerator 25, sludge pump 27 are all connected with electric control system.Electric control system can be realized by PLC, makes whole device Automatic Control, simple to operate, safe and reliable to operation, daily need not professional's management, only needs in real time equipment is carried out care and maintenance, and noise is low, free from extraneous odour, and service life is long.
The above; it is only this utility model preferably detailed description of the invention; but protection domain of the present utility model is not limited thereto; any those familiar with the art is in the technical scope that this utility model discloses; the change that can readily occur in or replacement, all should contain within protection domain of the present utility model.
Claims (10)
1. an integrated high-efficiency sewage treatment device, including integrated cabinet (1), regulating reservoir (19), equipment room (21), sludge-tank (26) and sludge concentration tank (28), sludge-tank (26) is connected in series with sludge concentration tank (28), it is characterized in that: in described integrated cabinet (1), be provided with anoxic pond (2), at least two Aerobic Pond, sedimentation tank (7), coagulating basin (8), flocculation basin (9), final deposition pool (10) and clear water reserviors (11), Aerobic Pond, sedimentation tank (7), coagulating basin (8), final deposition pool (10), clear water reserviors (11) are all close to mutually with anoxic pond (2)；Being provided with aerating system (13) and nitrification liquid reflux pump (18) in described Aerobic Pond, nitrification liquid reflux pump (18) is connected with anoxic pond (2)；Being provided with the first sludge pump (14) in described sedimentation tank (7), be provided with the second sludge pump (15) in final deposition pool (10), the first sludge pump (14) is all connected with sludge-tank (26) with the second sludge pump (15)；Being provided with submersible sewage pump (20) in described regulating reservoir (19), submersible sewage pump (20) is connected with anoxic pond (2)；Aerator (25), ozonator (24), PAM dosing tank (22), PAC dosing tank (23) it is provided with in described equipment room (21), aerator (25) is connected with aerating system (13), ozonator (24) is connected with clear water reserviors (11), PAM dosing tank (22) is connected with flocculation basin (9), and PAC dosing tank (23) is connected with coagulating basin (8).
2. according to the integrated high-efficiency sewage treatment device described in claims 1, it is characterized in that, described integrated cabinet (1) is round box, anoxic pond (2) is arranged on the center of integrated cabinet (1) and for circular, and the annular section between integrated cabinet (1) and anoxic pond (2) has been sequentially connected in series Aerobic Pond, sedimentation tank (7), coagulating basin (8), flocculation basin (9), final deposition pool (10) and clear water reserviors (11) counterclockwise.
3. according to the integrated high-efficiency sewage treatment device described in claims 1, it is characterized in that, described anoxic pond (2) is internal is provided with the 3rd latent dirty blender (12), is provided with the first latent dirty blender (16), is provided with the second latent dirty blender (17) in flocculation basin (9) in coagulating basin (8).
4. according to the integrated high-efficiency sewage treatment device described in claims 1, it is characterized in that, described sedimentation tank (7) is vertical sedimentation basin, central tube, reflecting plate, bucket and the first sludge pump (14) it is provided with in sedimentation tank (7), first sludge pump (14) is connected with anoxic pond (2), sludge reflux to anoxic pond (2), the first sludge pump (14) are arranged in the bucket of sedimentation tank (7) by the first sludge pump (14)；Described final deposition pool (10) is vertical sedimentation basin, is provided with central tube, reflecting plate, bucket and the second sludge pump (15) in final deposition pool (10), and the second sludge pump (15) is arranged in the bucket of final deposition pool (10).
5. according to the integrated high-efficiency sewage treatment device described in claims 1, it is characterized in that, the quantity of described Aerobic Pond is provided with 4, includes Aerobic Pond I (3), Aerobic Pond II (4), Aerobic Pond III (5) and Aerobic Pond IV (6), it is equipped with aerating system (13) in Aerobic Pond I (3), Aerobic Pond II (4), Aerobic Pond III (5) and Aerobic Pond IV (6), aerating system is interconnected between (13), and nitrification liquid reflux pump (18) is located at the bottom of Aerobic Pond IV (6).
null6. according to the integrated high-efficiency sewage treatment device described in claims 5，It is characterized in that，Top between described anoxic pond (2) and Aerobic Pond I (3) is provided with water hole，Bottom between Aerobic Pond I (3) and Aerobic Pond II (4) is provided with water hole，Top between Aerobic Pond II (4) and Aerobic Pond III (5) is provided with water hole，Between Aerobic Pond III (5) and Aerobic Pond IV (6), bottom is provided with water hole，Aerobic Pond IV (6) is connected by the central tube of pipeline with sedimentation tank (7)，Top between sedimentation tank (7) and coagulating basin (8) is provided with water hole，Coagulating basin (8) is provided with water hole with flocculation basin (9) bottom，Flocculation basin (9) is connected by the central tube of pipeline with final deposition pool (10)，Top between final deposition pool (10) and clear water reserviors (11) is provided with water hole.
7., according to the integrated high-efficiency sewage treatment device described in claims 1, it is characterised in that be provided with sludge pump (27) in described sludge-tank (26), sludge pump (27) is connected with sludge concentration tank (28).
8. according to the integrated high-efficiency sewage treatment device described in claims 1 or 5, it is characterized in that, described aerating system (13) includes that the gas pipeline being interconnected, aerating system (13) are separately positioned on Aerobic Pond I (3), Aerobic Pond II (4), Aerobic Pond III (5), the bottom of Aerobic Pond IV (6).
9. according to the integrated high-efficiency sewage treatment device described in claims 1, it is characterised in that the quantity of described aerator (25) and submersible sewage pump (20) is equipped with two, two aerators (25) are connected in parallel, and two submersible sewage pumps (20) are connected in parallel.
10. according to claims 1, 3, 7, integrated high-efficiency sewage treatment device described in any one in 9, it is characterized in that, described regulating reservoir is provided with liquid level controller in (19), liquid level controller, submersible sewage pump (20), 3rd latent dirty blender (12), nitrification liquid reflux pump (18), first sludge pump (14), first latent dirty blender (16), second latent dirty blender (17), second sludge pump (15), PAM dosing tank (22), PAC dosing tank (23), ozonator (24), aerator (25), sludge pump (27) is all connected with electric control system.
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| CN201620477227.XU CN205635285U (en) | 2016-05-24 | 2016-05-24 | High -efficient sewage treatment device of integration |
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| CN201620477227.XU CN205635285U (en) | 2016-05-24 | 2016-05-24 | High -efficient sewage treatment device of integration |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106430847A (en) * | 2016-11-22 | 2017-02-22 | 河南鸿昇环保设备制造有限公司 | Intensive swine wastewater treating equipment |
| CN110240349A (en) * | 2018-03-10 | 2019-09-17 | 北控水务(中国)投资有限公司 | One kind is with A2Integrated sewage treating apparatus based on/O technique |
| CN110845078A (en) * | 2019-11-14 | 2020-02-28 | 广东威特雅环境科技有限公司 | Adjustable integrated garbage transfer station leachate treatment system and process |
| CN111513023A (en) * | 2020-05-24 | 2020-08-11 | 镇江大成渔业发展有限公司 | Greenhouse soft-shelled turtle breeding method |
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2016
- 2016-05-24 CN CN201620477227.XU patent/CN205635285U/en active Active
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106430847A (en) * | 2016-11-22 | 2017-02-22 | 河南鸿昇环保设备制造有限公司 | Intensive swine wastewater treating equipment |
| CN106430847B (en) * | 2016-11-22 | 2023-04-07 | 河南鸿昇环保设备制造有限公司 | Intensive pig raising wastewater treatment equipment |
| CN110240349A (en) * | 2018-03-10 | 2019-09-17 | 北控水务(中国)投资有限公司 | One kind is with A2Integrated sewage treating apparatus based on/O technique |
| CN110845078A (en) * | 2019-11-14 | 2020-02-28 | 广东威特雅环境科技有限公司 | Adjustable integrated garbage transfer station leachate treatment system and process |
| CN110845078B (en) * | 2019-11-14 | 2021-10-29 | 广东威特雅环境科技有限公司 | Adjustable integrated garbage transfer station leachate treatment system and process |
| CN111513023A (en) * | 2020-05-24 | 2020-08-11 | 镇江大成渔业发展有限公司 | Greenhouse soft-shelled turtle breeding method |
| CN111513023B (en) * | 2020-05-24 | 2021-12-03 | 镇江大成渔业发展有限公司 | Greenhouse soft-shelled turtle breeding method |
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