CN207468287U - Integral anaerobic and scarce aerobic transformation combination wastewater treatment equipment - Google Patents

Integral anaerobic and scarce aerobic transformation combination wastewater treatment equipment Download PDF

Info

Publication number
CN207468287U
CN207468287U CN201721457164.2U CN201721457164U CN207468287U CN 207468287 U CN207468287 U CN 207468287U CN 201721457164 U CN201721457164 U CN 201721457164U CN 207468287 U CN207468287 U CN 207468287U
Authority
CN
China
Prior art keywords
aerobic
anoxic
zone
anaerobism
water inlet
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.)
Active
Application number
CN201721457164.2U
Other languages
Chinese (zh)
Inventor
李玄
赵友恒
史会剑
王占金
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shandong Institute of ecological environment planning
Original Assignee
Shandong Institute Of Environmental Planning
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Shandong Institute Of Environmental Planning filed Critical Shandong Institute Of Environmental Planning
Priority to CN201721457164.2U priority Critical patent/CN207468287U/en
Application granted granted Critical
Publication of CN207468287U publication Critical patent/CN207468287U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

A kind of integral anaerobic and aerobic transformation combination wastewater treatment equipment is lacked, including pond body, anaerobic zone spaced apart from each other, aerobic zone and anoxic zone are divided into pond body;Anaerobism water inlet pipe, aerobic water inlet pipe and anoxic water inlet pipe are respectively arranged in each area, anaerobism inlet valve is both provided on each water inlet pipe;Each area top is provided with filter layer, downflow weir is provided with above filter layer, drainpipe is provided on the outside of downflow weir, anaerobic zone drainpipe is connected with anoxic water inlet pipe, it is connected between anaerobic zone downflow weir and aerobic zone and detests aerobic communicating pipe, anoxic zone drainpipe is connected with anaerobism water inlet pipe, and scarce aerobic communicating pipe is connected between anoxic zone downflow weir and aerobic zone.The device sets anaerobic zone, aerobic zone and anoxic zone in a pond body, by combination and the use in conjunction in each area, it can be achieved that the individually combination of anaerobism, aerobic and hypoxia response and a variety of reaction formations, to adapt to the needs of different quality, stable effluent quality.

Description

Integral anaerobic and scarce aerobic transformation combination wastewater treatment equipment
Technical field
The utility model is related to a kind of devices for being used to carry out waste water anaerobism or scarce Aerobic Process for Treatment, belong to Wastewater Treatment Technology Art field.
Background technology
In the prior art, anaerobism, anoxic and aerobic reaction are generally used to the processing of waste water.Anaerobism refers in a kind of non- The biodegradability of sewage can be changed for releasing phosphorus bacterium in oxidation state, anaerobic reaction.Anoxic is the state of oxidation of hypodactylia oxygen, is lacked Oxygen reaction is for NO3-N and NO2-N denitrification denitrogenation.It is aerobic to refer to oxygen abundance, it is utilized for aerobic microbiological, it is aerobic Reaction removes BOD for nitrifying with aerobic activated sludge.It is useless to reach purification for generally use anaerobism, anoxic and aerobic association response The purpose of water.
Following various combinations can be carried out to the anaerobism, anoxic and aerobic reaction of sewage:
1. traditional anaerobism, anoxic and aerobic process (A2/O techniques) are carried out with anaerobism, anoxic and aerobic order. During A2/O process waste water, need in water containing more organic matter to ensure carbon source, it is less in content of organics In the case of, which can make denitrification denitrogenation undesirable, and the nitrate nitrogen that returned sludge brings anaerobic zone into makes polyP bacteria release phosphorus not Fully, the polyP bacteria then influenced in aerobic zone inhales phosphorus, causes effluent quality unstable, is extremely difficult to good simultaneous denitrification and removes Phosphorus effect.
2. anaerobism and aerobic combined process (A/O techniques), major function is biological phosphate-eliminating.Anaerobic stages, polyP bacteria release Phosphorus;Aerobic stage absorbs phosphorus, and when discharging excess sludge, phosphorus is excluded together.
3. anoxic and aerobic combined process, major function is biological denitrificaion.Anoxic phases, nitrate, nitrite, nitric acid Nitrogen and cultured water are converted into nitrogen.If ammonia nitrogen in sewage is very high, then by the sewage backflow of aerobic stage to anoxic pond.
In existing sewage disposal device, there are individual anaerobic reactor, aerobic reactor, anaerobism with it is aerobic compound anti- Answer device and scarce aerobic reactor.And the structure of reaction tank is generally adopted in anaerobism, anoxic and aerobic process (A2/O techniques), takes up an area Area is big, and treatment effeciency is low.
But currently without can to waste water carry out multiple combinations processing equipment so that it can according to required technique The arbitrary combination of Anaerobic Treatment, anoxic treatment and Aerobic Process for Treatment is realized, to improve treatment effeciency and effect.
Utility model content
The utility model provides a kind of achievable a variety of processing mode groups for deficiency existing for existing wastewater processing technology It closes, the integral anaerobic that treatment effeciency is high, effluent quality is good and scarce aerobic transformation combine wastewater treatment equipment.
The integral anaerobic of the utility model and scarce aerobic transformation combination wastewater treatment equipment, using following technical proposals:
The device including pond body, is divided into anaerobic zone spaced apart from each other, aerobic zone and anoxic zone in pond body;Aerobic zone is with lacking Water valve was provided between oxygen area, be respectively arranged in anaerobic zone, aerobic zone and anoxic zone anaerobism water inlet pipe, aerobic water inlet pipe and Anoxic water inlet pipe is both provided with anaerobism inlet valve on each water inlet pipe;The top of anaerobic zone is provided with gas-solid-liquid Disengagement zone, gas-solid-liquid Anaerobism filter layer is provided with above Disengagement zone, is provided with anaerobism downflow weir above anaerobism filter layer, anaerobism downflow weir it is outer Side is provided with anaerobism drainpipe, is provided on anaerobism drainpipe and detests anoxic reversal valve, detest anoxic reversal valve and anoxic water inlet pipe it Between be connected with and detest anoxic communicating pipe, be connected between anaerobism downflow weir and aerobic zone and detest aerobic communicating pipe, detested on aerobic communicating pipe It is provided with and detests aerobic communicating valve;The top of aerobic zone is provided with aerobic filter layer, and aerobic overflow is provided with above aerobic filter layer Weir is flowed, aerobic drainpipe is provided on the outside of aerobic downflow weir, drain valve is provided on aerobic drainpipe, is provided in aerobic zone Aerator;Anoxic air inlet pipe is provided in anoxic zone, the top of anoxic zone is provided with anoxic filter layer, anoxic filter layer top Anoxic downflow weir is provided with, anoxic drainpipe is provided on the outside of anoxic downflow weir, scarce anaerobism is provided on anoxic drainpipe and is changed To valve, lack and scarce anaerobism communicating pipe is connected between anaerobism reversal valve and anaerobism water inlet pipe, connect between anoxic downflow weir and aerobic zone Scarce aerobic communicating pipe is connected to, lacks and is provided with scarce aerobic communicating valve on aerobic communicating pipe.
The bottom end of the anaerobism water inlet pipe, aerobic water inlet pipe and anoxic water inlet pipe is respectively provided with water distributor.
The bottom of the anaerobic zone, aerobic zone and anoxic zone is both provided with blow-off pipe, and blowdown valve is connected on blow-off pipe.
Flow valve is connected in the anoxic air inlet pipe, to control aeration quantity, anoxic zone is made to be in anaerobic condition.
During above-mentioned wastewater treatment equipment operation, can individually it be reacted accordingly in anaerobic zone, aerobic zone and anoxic zone, But carry out anaerobism and aerobic, anoxic with it is aerobic, aerobic with anoxic, anaerobism, anoxic and aerobic and anoxic, anaerobism with it is aerobic etc. The combination of diversified forms, to adapt to the needs of different quality.
The utility model is adaptable, and anaerobic zone, aerobic zone and anoxic zone are set in a pond body, passes through the group in each area It closes and use in conjunction is, it can be achieved that individually anaerobism, aerobic and hypoxia response and two kinds of reaction formations or three kinds of reaction formations Combination, to adapt to the needs of different quality, improves treatment effeciency, effluent quality is greatly improved and stablizes.
Description of the drawings
Fig. 1 is the utility model integral anaerobic and the structure diagram for lacking aerobic transformation combination wastewater treatment equipment.
In figure:1st, pond body, 2, anaerobism blow-off pipe, 3, first partition, 4, aerobic blow-off pipe, 5, cross water valve, 6, second partition, 7th, anoxic blow-off pipe, 8, anoxic air inlet pipe, 9, flow valve, 10, lack aerobic communicating pipe, 11, anoxic zone, 12, anoxic water inlet pipe, 13rd, aerobic filter layer, 14, anoxic filter layer, 15, anoxic drainpipe, 16, lack anaerobism reversal valve, 17, lack anaerobism communicating pipe, 18, Anoxic inlet valve, 19, exhaust pipe, 20, aerobic water inlet pipe, 21, aerobic inlet valve, 22, aeration tube, 23, anaerobism inlet valve, 24, Water inlet manifold, 25, anaerobism water inlet pipe, 26, biogas pipe, 27, anaerobism downflow weir, 28, anaerobism drainpipe, 29, anaerobism filter layer, 30th, gas-solid-liquid Disengagement zone, 31, aerobic downflow weir, 32, detest aerobic communicating pipe, 33, blender, 34, aerobic drainpipe, 35, lack Oxygen communicating valve, 36, detest aerobic communicating valve, 37, anaerobic zone, 38, aerobic zone, 39, anoxic downflow weir, 40, detest anoxic reversal valve, 41st, anaerobism communicating pipe is lacked.
Specific embodiment
As shown in Figure 1, the integral anaerobic of the utility model and scarce aerobic transformation combination wastewater treatment equipment, including pond body 1.Divided in pond body 1 by vertical first partition 3 and second partition 6 for anaerobic zone 37 arranged side by side, aerobic zone 38 and anoxic zone 11. 6 lower part of second partition between aerobic zone 38 and anoxic zone 11 was provided with water valve 5.Anaerobic zone 37, aerobic zone 38 and anoxic zone Be respectively arranged with anaerobism water inlet pipe 23, aerobic water inlet pipe 20 and anoxic water inlet pipe 12 in 11, anaerobism water inlet pipe 25 by anaerobism into Water valve 23 is connect with water inlet manifold 24, and aerobic water inlet pipe 20 is connect by aerobic inlet valve 21 with water inlet manifold 24, anoxic water inlet Pipe 12 is connect by anoxic inlet valve 18 with water inlet manifold 24.It can intake in anaerobism water inlet pipe 23, aerobic water inlet pipe 20 and anoxic The bottom end setting water distributor of pipe 12.
The bottom of anaerobic zone 37 is provided with anaerobism blow-off pipe 2, and blowdown valve is connected on anaerobism blow-off pipe 2.Anaerobic zone 37 Top is provided with gas-solid-liquid Disengagement zone 30, and the top of gas-solid-liquid Disengagement zone 30 is provided with anaerobism filter layer 29, anaerobism filter layer 29 Top be provided with anaerobism downflow weir 27, the outside of anaerobism downflow weir 27 is provided with anaerobism drainpipe 28.On anaerobism drainpipe 28 It is provided with and detests anoxic reversal valve 40, detest to be connected between anoxic reversal valve 40 and anoxic water inlet pipe 12 and detest anoxic communicating pipe 41.Detest It is connected between oxygen downflow weir 27 and aerobic zone 38 and detests aerobic communicating pipe 32, detested to be provided on aerobic communicating pipe 32 and detest aerobic connection Valve 36.Blender 33 is additionally provided in anaerobic zone 37 and stretches into the biogas pipe 26 of gas-solid-liquid Disengagement zone 30.Waste water is by always intaking Pipe 24 (opening anaerobism inlet valve 25) (changes and commutates into anaerobic zone 37 or by anoxic zone 11 by lacking anaerobism communicating pipe 17 Valve 16) into anaerobic zone 37.After waste water enters anaerobic zone 37, anaerobic reaction is carried out by the stirring of blender 33, then by gas Solid-liquid displacement zone 30 carries out gas-solid-liquid separation, and the biogas of generation is discharged by biogas pipe 26, and sludge is trapped, and purified water body leads to It crosses after anaerobism filter layer 29 filters and enters anaerobism downflow weir 27, water in anaerobism downflow weir 27 or directly pass through anaerobism drainpipe 28 discharges (detesting anoxic reversal valve 40 to connect with anaerobism drainpipe 28) enter aerobic zone 38 by detesting aerobic communicating pipe 32 (opening detests aerobic communicating valve 36), then carry out aerobic reaction processing.Other forms can also be used in structure in anaerobic zone 37.
The bottom of aerobic zone 38 is provided with aerobic blow-off pipe 4, and blowdown valve is connected on aerobic blow-off pipe 4.Aerobic zone 38 Top is provided with aerobic filter layer 13, and the top of aerobic filter layer 13 is provided with aerobic downflow weir 31, aerobic downflow weir 31 it is outer Side is provided with aerobic drainpipe 34, and drain valve is provided on aerobic drainpipe 34.It is additionally provided in aerobic zone 38 and stretches into its bottom Aeration tube 22,22 bottom of aeration tube setting aeration head.Compressed air is passed through into aerobic zone 38 by aeration tube 22, is exposed Gas.Waste water enters by water inlet manifold 24 (opening aerobic inlet valve 21) into aerobic zone 38 or by detesting aerobic communicating pipe 32 Oxygen area 38 (opening detests aerobic communicating valve 36) lacks aerobic communicating pipe 10 into (the scarce aerobic communicating valve of opening of aerobic zone 38 35).Purified water body enters aerobic downflow weir 31 after being filtered by aerobic filter layer 13, and the water in aerobic downflow weir 31 passes through Aerobic drainpipe 34 discharges and (opens the drain valve on aerobic drainpipe 34), is utilized.Structure in aerobic zone 38 can also adopt Use other forms.
The bottom of anoxic zone 11 is provided with anoxic blow-off pipe 7, and blowdown valve is connected on anoxic blow-off pipe 7.Anoxic zone 11 Lower part is provided with anoxic air inlet pipe 8, and flow valve 9 is connected in anoxic air inlet pipe 8, to control aeration quantity, is in anoxic zone 11 Anaerobic condition.The top of anoxic zone 11 is provided with anoxic filter layer 14, and 14 top of anoxic filter layer is provided with anoxic downflow weir 39, The outside of anoxic downflow weir 39 is provided with anoxic drainpipe 15, and scarce anaerobism reversal valve 16 is provided on anoxic drainpipe 15, lacks and detests Scarce anaerobism communicating pipe 17 is connected between oxygen reversal valve 16 and anaerobism water inlet pipe 23.Connect between anoxic downflow weir 39 and aerobic zone 38 Scarce aerobic communicating pipe 10 is connected to, lacks and is provided with scarce aerobic communicating valve 35 on aerobic communicating pipe 10.The row of being additionally provided in anoxic zone 11 Tracheae 19, the exhaust gas of generation are discharged by exhaust pipe 19.Waste water is by water inlet manifold 24 (open anoxic inlet valve 18) into anoxic zone 11 either enter anoxic zone 11 or by anaerobic zone 37 through detesting anoxic communicating pipe 41 into anoxic by aerobic zone 38 by water valve 5 Area 11.Waste water enters anoxic zone 11 and carries out hypoxia response, and purified water body enters anoxic after being filtered by anoxic filter layer 14 Downflow weir 39, water in anoxic downflow weir 39 or directly discharged by anoxic drainpipe 15 (are opened on anoxic drainpipe 15 Drain valve) or by lacking aerobic communicating pipe 10 into aerobic zone 38 (opening scarce aerobic communicating valve 35), then carry out aerobic reaction Processing lacks anaerobism reversal valve 16 by lacking anaerobism communicating pipe 17 into anaerobic zone 37 by change.Structure in anoxic zone 11 Other forms can also be used.
Above-mentioned wastewater treatment equipment can carry out the transformation combination of following diversified forms, to adapt to the needs of different quality.
1. independent anaerobic reaction device
Anaerobism inlet valve 23 is opened, detests anoxic reversal valve 40 and be converted to communicating with anaerobism drainpipe 28, and closes other valves Door, waste water only enter anaerobic zone 37, are reacted in anaerobic zone 37, and be expelled directly out.
2. independent aerobic reaction device
The drain valve on aerobic inlet valve 21 and aerobic drainpipe 34 is opened, and closes other valves, waste water only enters It reacts, and is expelled directly out in aerobic zone 38 in oxygen area 38.
3. independent hypoxia response device
Anoxic inlet valve 18 is opened, scarce anaerobism reversal valve 16 is converted to be communicated with anoxic drainpipe 15, closes other valves, Waste water only enters anoxic zone 11, is reacted in anoxic zone 11, and be expelled directly out.
4. anaerobism and aerobic reaction device
It opens anaerobism inlet valve 25, detest drain valve on aerobic communicating valve 36 and aerobic drainpipe 34, and close other valves Door.Waste water enters after anaerobic zone 37 is reacted and enters aerobic zone 38 by detesting aerobic communicating pipe 32 again, and be expelled directly out by aerobic zone 38.
5. anoxic and aerobic reaction device
Drain valve on unlatching anoxic inlet valve 18, scarce aerobic communicating valve 35 and aerobic drainpipe 34, and close other valves Door.Waste water enters after anoxic zone 11 is reacted and enters aerobic zone 38 by lacking aerobic communicating pipe 10 again, and be expelled directly out by aerobic zone 38.
6. aerobic and hypoxia response device
It opens aerobic inlet valve 21 and crosses water valve 5, scarce anaerobism reversal valve 16 is converted to be communicated with anoxic drainpipe 15, and is closed Close other valves.Waste water enters after aerobic zone 38 is reacted and enters anoxic zone 11, and directly arranged by anoxic zone 11 using water valve 5 Go out.
7. anaerobism, anoxic and aerobic reaction device
Drain valve on unlatching anaerobism inlet valve 23, scarce aerobic communicating valve 35 and aerobic drainpipe 34, detests anoxic reversal valve 40 are converted to and are communicated with detesting anoxic communicating pipe 41, and close other valves.Waste water enters anaerobic zone by anaerobism water inlet pipe 25 first 37, enter anoxic zone 11 anoxic communicating pipe 41 by detesting again after anaerobic reaction, entered aerobic communicating pipe 10 by lacking again after hypoxia response Aerobic zone 38, and be expelled directly out by aerobic zone 38.
8. anoxic, anaerobism and aerobic reaction device
It opens anoxic inlet valve 18, detest drain valve on aerobic communicating valve 36 and aerobic drainpipe 34, lack anaerobism reversal valve 16 communicate with scarce anaerobism communicating pipe 17, and close other valves.Waste water enters anoxic zone 11, anoxic by anoxic water inlet pipe 12 first Enter anaerobic zone 37 anaerobism communicating pipe 17 by lacking again after reaction, again by detesting aerobic communicating pipe 32 into aerobic zone after anaerobic reaction 38, and be expelled directly out by aerobic zone 38.
The combination of other forms can also be carried out as needed.

Claims (4)

1. a kind of integral anaerobic and scarce aerobic transformation combination wastewater treatment equipment, including pond body, it is characterized in that:It is divided into pond body Anaerobic zone spaced apart from each other, aerobic zone and anoxic zone;Water valve, anaerobic zone, aerobic zone were provided between aerobic zone and anoxic zone With anaerobism water inlet pipe, aerobic water inlet pipe and anoxic water inlet pipe are respectively arranged in anoxic zone, be both provided with anaerobism on each water inlet pipe Inlet valve;The top of anaerobic zone is provided with gas-solid-liquid Disengagement zone, and anaerobism filter layer, anaerobism are provided with above gas-solid-liquid Disengagement zone Anaerobism downflow weir is provided with above filter layer, anaerobism drainpipe is provided on the outside of anaerobism downflow weir, is set on anaerobism drainpipe Be equipped with and detest anoxic reversal valve, detest to be connected between anoxic reversal valve and anoxic water inlet pipe and detest anoxic communicating pipe, anaerobism downflow weir with It is connected between aerobic zone and detests aerobic communicating pipe, detested to be provided on aerobic communicating pipe and detest aerobic communicating valve;The top of aerobic zone is set Aerobic filter layer is equipped with, aerobic downflow weir is provided with above aerobic filter layer, aerobic row is provided on the outside of aerobic downflow weir Water pipe is provided with drain valve on aerobic drainpipe, aerator is provided in aerobic zone;Anoxic air inlet is provided in anoxic zone Pipe, the top of anoxic zone are provided with anoxic filter layer, are provided with anoxic downflow weir above anoxic filter layer, anoxic downflow weir it is outer Side is provided with anoxic drainpipe, and scarce anaerobism reversal valve is provided on anoxic drainpipe, lack anaerobism reversal valve and anaerobism water inlet pipe it Between be connected with scarce anaerobism communicating pipe, scarce aerobic communicating pipe is connected between anoxic downflow weir and aerobic zone, lack aerobic communicating pipe on It is provided with scarce aerobic communicating valve.
2. integral anaerobic according to claim 1 and scarce aerobic transformation combination wastewater treatment equipment, it is characterized in that:It is described The bottom end of anaerobism water inlet pipe, aerobic water inlet pipe and anoxic water inlet pipe is respectively provided with water distributor.
3. integral anaerobic according to claim 1 and scarce aerobic transformation combination wastewater treatment equipment, it is characterized in that:It is described The bottom of anaerobic zone, aerobic zone and anoxic zone is both provided with blow-off pipe, and blowdown valve is connected on blow-off pipe.
4. integral anaerobic according to claim 1 and scarce aerobic transformation combination wastewater treatment equipment, it is characterized in that:It is described Flow valve is connected in anoxic air inlet pipe.
CN201721457164.2U 2017-11-03 2017-11-03 Integral anaerobic and scarce aerobic transformation combination wastewater treatment equipment Active CN207468287U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721457164.2U CN207468287U (en) 2017-11-03 2017-11-03 Integral anaerobic and scarce aerobic transformation combination wastewater treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721457164.2U CN207468287U (en) 2017-11-03 2017-11-03 Integral anaerobic and scarce aerobic transformation combination wastewater treatment equipment

Publications (1)

Publication Number Publication Date
CN207468287U true CN207468287U (en) 2018-06-08

Family

ID=62262938

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201721457164.2U Active CN207468287U (en) 2017-11-03 2017-11-03 Integral anaerobic and scarce aerobic transformation combination wastewater treatment equipment

Country Status (1)

Country Link
CN (1) CN207468287U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107619110A (en) * 2017-11-03 2018-01-23 山东省环境规划研究院 Integral anaerobic and scarce aerobic conversion combination wastewater treatment equipment

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107619110A (en) * 2017-11-03 2018-01-23 山东省环境规划研究院 Integral anaerobic and scarce aerobic conversion combination wastewater treatment equipment

Similar Documents

Publication Publication Date Title
CN105481093B (en) The system and method for continuous stream segmental influent short distance nitration/Anammox Treating Municipal Sewage
CN106830324A (en) A kind of subsection water inflow A2The apparatus and method of/O process strengthening biological carbon and phosphorous removals
CN104350012A (en) Internal-circulation aeration anammox-membrane bioreactor
CN103241903A (en) Device and method for treating low-carbon nitrogen sewage in synchronous anaerobic ammonia oxidation and anaerobic methane oxidation mode
CN105217786B (en) Based on DEAMOX reinforcing improvement subsection water inflow As2The apparatus and method of/O technique biological carbon and phosphorous removals
CN102101746A (en) Low-carbon urban sewage biological phosphorus removal and autotrophic biological nitrogen removal device and method
CN109160606A (en) A kind of method of municipal sewage methane phase and efficient advanced nitrogen
CN107574117A (en) A kind of preparation facilities and its method of penicillin resistant class amonifying bacteria microbial inoculum
CN110683654B (en) High-efficient whole autotrophic nitrogen removal device
CN206666226U (en) A kind of integrated biochemical reaction tower
CN108545887A (en) The method of sulfide type DEAMOX postposition anoxics filter tank denitrification and desulfurization hydrogen based on AAO-BAF Process for Effluent
CN216549815U (en) Internal circulation short-cut denitrification filter tank
CN201923926U (en) Low carbon biological phosphorus removal and autotroph denitrogenation device for municipal sewage
CN110078213A (en) The apparatus and method of SBR/ anaerobic baffled reactor strengthened anaerobic ammoxidation Treating Municipal Sewage stable operation
CN207468287U (en) Integral anaerobic and scarce aerobic transformation combination wastewater treatment equipment
CN106045030B (en) A2The apparatus and method of/O-UASB continuous flow city domestic sewage advanced nitrogen dephosphorization
CN210683343U (en) Rural domestic sewage MBR integration processing apparatus
CN113023882B (en) Method and reactor for treating sewage with low carbon-nitrogen ratio
CN213357071U (en) System for realizing short-cut nitrification-anaerobic ammonia oxidation denitrification stable operation of low-ammonia-nitrogen wastewater
CN101638270B (en) System for biochemically treating wastewater with high ammonia nitrogen concentration
CN210340622U (en) Sewage treatment device with multi-point backflow
CN107487841A (en) A kind of denitrification integrates coupling dephosphorization and the waste water treatment process of Anammox
CN209619000U (en) A kind of high strength domestic sewage processing unit
CN107619110A (en) Integral anaerobic and scarce aerobic conversion combination wastewater treatment equipment
CN111233151A (en) Efficient synchronous nitrogen and phosphorus removal system and method for high-nitrogen and phosphorus wastewater

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CP01 Change in the name or title of a patent holder

Address after: 250101, No. ten, No. 3377, Ji'nan, Shandong

Patentee after: Shandong Institute of ecological environment planning

Address before: 250101, No. ten, No. 3377, Ji'nan, Shandong

Patentee before: SHANDONG ACADEMY FOR ENVIRONMENTAL PLANNING

CP01 Change in the name or title of a patent holder