CN216141327U - One-section type EGSB anaerobic ammonia oxidation device based on MABR - Google Patents

One-section type EGSB anaerobic ammonia oxidation device based on MABR Download PDF

Info

Publication number
CN216141327U
CN216141327U CN202120496092.2U CN202120496092U CN216141327U CN 216141327 U CN216141327 U CN 216141327U CN 202120496092 U CN202120496092 U CN 202120496092U CN 216141327 U CN216141327 U CN 216141327U
Authority
CN
China
Prior art keywords
mabr
internal reflux
valve
internal
flow meter
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
CN202120496092.2U
Other languages
Chinese (zh)
Inventor
穆永杰
张丽丽
薛晓飞
李凌云
于弢
曹天宇
郑琬琳
曹之淇
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.)
Beijing Enterprises Water China Investment Co Ltd
Original Assignee
Beijing Enterprises Water China Investment Co Ltd
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 Beijing Enterprises Water China Investment Co Ltd filed Critical Beijing Enterprises Water China Investment Co Ltd
Priority to CN202120496092.2U priority Critical patent/CN216141327U/en
Application granted granted Critical
Publication of CN216141327U publication Critical patent/CN216141327U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00—Technologies for wastewater treatment
    • Y02W10/10—Biological treatment of water, waste water, or sewage

Landscapes

  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

A one-stage EGSB anaerobic ammonia oxidation device based on MABR belongs to the field of sewage treatment equipment. The device couples the MABR and the EGSB, realizes the effective enrichment of AOB and the elimination of NOB through the regulation and control operation of oxygen supply, and provides substrate guarantee for the effective implementation of the anaerobic ammonia oxidation reaction; the MABR membrane component can meet the requirement of accurate oxygen supply and also serves as a biological carrier, so that the biomass of the biological membrane is large, the food chain length is long, and AOB is not easy to lose; the AOB reaction zone and the anaerobic ammonia oxidation reaction zone of the granular sludge of the MABR are separated, and an online monitoring feedback system and a backflow regulation and control system are respectively arranged, so that the running efficiency of the EGSB system is maximized while the optimized regulation and control of the two reaction zones are respectively met; the aeration energy consumption of the MABR membrane component is low, and the overall operation cost of the system is reduced; the EGSB internal reflux system is flexible and changeable, the operation requirements of the two reaction zones are met, and the flushing regulation and control of the biofilm thickness of the MABR membrane component can be realized.

Description

One-section type EGSB anaerobic ammonia oxidation device based on MABR
Technical Field
The utility model belongs to the field of sewage treatment equipment, and particularly relates to a one-stage EGSB anaerobic ammonia oxidation device based on MABR.
Background
The one-stage shortcut nitrification-anaerobic ammonia oxidation process couples shortcut nitrification and anaerobic ammonia oxidation to realize NH in one reactor4 +The nitrosation and the anaerobic ammoxidation are carried out synchronously, and the method is suitable for higher NH4 +The treatment of wastewater with N concentration (such as industrial wastewater, garbage leachate, culture wastewater, sludge digestive fluid and the like) has high denitrification efficiency and low aeration energy consumption compared with the traditional denitrification process. In addition, the denitrification process is based on the unique physiological metabolic pathway of the anaerobic ammonium oxidation bacteria, and organic matters are not needed to participate in the denitrification process, so that the denitrification effect is not influenced by insufficient organic matters in the inlet water.
NH4 ++1.5O2→NO2 -+2H++H2O(1-1)
NH4 ++1.32NO2 -+0.066HCO3 -+0.13H+→1.02N2+0.26NO3 -+0.066CH2O0.5N0.15+2.03H2O (1-2)
The reaction principles (1-1) and (1-2) show that the limitation of the reaction process of the one-stage type short-cut nitrification-anaerobic ammonia oxidation processThe fast step is shortcut nitrification, which is the reaction of NH by Ammonia Oxidizing Bacteria (AOB)4 +Conversion of-N to NO2 -N, which provides a reaction substrate for the smooth proceeding of the subsequent anaerobic ammonium oxidation reaction. Under the condition of excessive aeration, nitrite-oxidizing bacteria (NOB) can convert NO2 -Further oxidation of-N to NO3 -N, which is detrimental to the anammox reaction. How to realize the effective enrichment of AOB and the elimination of NOB through the accurate and effective aeration control is the main technical bottleneck of the current one-stage type short-cut nitrification-anaerobic ammonia oxidation system.
The Membrane Aeration Bioreactor (MABR) uses a permeable Membrane material to perform aeration and oxygen supply, oxygen is transferred in a dissolved diffusion or micro-bubble/bubble-free mode, and meanwhile, the permeable Membrane has a large specific surface area and is easy for the attachment and growth of microorganisms to form a biological Membrane. According to the pollutant load and the activity of the biological membrane, the aeration membrane supplies oxygen to the biological membrane in real time according to the requirement, the oxygen concentration gradient in the biological membrane forms dynamic distribution, the oxygen concentration and the pollutant concentration are reversely transferred, and accurate oxygen supply is realized to the maximum extent.
The Expanded Granular Sludge Bed (EGSB) reactor provides reasonable and stable ascending flow velocity and flow state for a biochemical reaction zone through the optimized regulation and control of an internal reflux system, has remarkable advantages in the aspects of culturing anaerobic ammonia oxidation granular sludge, forming a biological membrane, controlling the thickness and the like, simultaneously increases the contact of a substrate and microorganisms in waste water through the flexible regulation and control of internal reflux parameters, effectively strengthens the mass transfer effect among reactants, and improves the biochemical reaction speed and the impact resistance of the reactor.
In conclusion, the advantages of flow state regulation and control of the internal reflux system of the EGSB reactor and substrate contact are utilized, the MABR capable of accurately supplying oxygen is coupled with the MABR, effective enrichment of AOB and elimination of NOB are realized through flexible regulation and control of the internal reflux system and accurate supply of oxygen, and technical reference is provided for efficient and stable operation of the one-stage EGSB anaerobic ammonia oxidation reactor.
Disclosure of Invention
The utility model aims to solveHigh NH treatment of one-stage EGSB anaerobic ammonia oxidation reactor4 +And in the case of N wastewater, the AOB is difficult to effectively enrich.
A one-stage EGSB anaerobic ammonia oxidation device based on MABR is shown in figure 1 and is characterized in that:
a one-stage EGSB anaerobic ammonia oxidation device based on MABR comprises: a device main body (1); an anammox granular sludge zone (1-1); a screen plate flange (1-2); an MABR reaction zone (1-3); a three-phase separator (2); an internal reflux main valve (3); a first internal return valve (4); a second internal return valve (5); a first internal reflux flow meter (6); a second internal reflux flow meter (7); a second internal reflux pump (8); a third internal return valve (9); a third internal reflux flow meter (10); a third internal reflux pump (11); a first internal reflux pump (12); a first perforated water distributor (13); a second perforated water distributor (14); a water inlet tank (15); a water inflow meter (16); a water inlet valve (17); a water inlet pump (18); an air filter (19); an intake valve (20); an aeration fan (21); an intake air flow meter (22); a MABR membrane module (23); an exhaust gas oxygen concentration measuring instrument (24); an exhaust valve (25); an exhaust gas flow meter (26); a first in-line monitoring electrode (27); a second on-line monitoring electrode (28); an autonomous system (29); an effluent overflow weir (30); a U-shaped water outlet (31); a gas production valve (32); a reactor vent valve (33);
the device main body (1) is divided into an anaerobic ammonia oxidation granular sludge area (1-1) and an MABR reaction area (1-3) by a sieve plate flange (1-2);
the volume ratio of the anaerobic ammonia oxidation granular sludge area (1-1) to the MABR reaction area (1-3) is maintained between 1:1 and 3: 1;
the sieve plate flange (1-2) has the aperture range of 1-3mm and is used for intercepting a biological membrane dropped from the surface of the MABR membrane component (23) to enter an anaerobic ammonia oxidation granular sludge area (1-1);
the internal reflux system of the device body (1) comprises: an internal reflux main valve (3); a first internal return valve (4); a second internal return valve (5); a first internal reflux flow meter (6); a second internal reflux flow meter (7); a second internal reflux pump (8); a third internal return valve (9); a third internal reflux flow meter (10); a third internal reflux pump (11); a first internal reflux pump (12); a first perforated water distributor (13); a second perforated water distributor (14);
the internal reflux main valve (3) is sequentially connected with a first internal reflux valve (4); a first internal reflux flow meter (6); a first internal reflux pump (12) and a first perforated water distributor (13); the internal reflux main valve (3) is sequentially connected with a second internal reflux valve (5); a second internal reflux flow meter (7); a second internal reflux pump (8) and a second perforated water distributor (14); the first perforated water distributor (13) is arranged in the MABR reaction zone (1-3); the second perforated water distributor (14) is arranged in the anaerobic ammonia oxidation granular sludge area (1-1);
a third internal return valve (9); a third internal reflux flow meter (10); the third internal reflux pump (11) and the MABR reaction zone (1-3) form a cycle;
the MABR membrane module (23) tail gas system comprises: a tail gas oxygen concentration measuring instrument (24), a tail gas valve (25) and a tail gas flowmeter (26) which are used for calculating the utilization efficiency of oxygen and regulating and controlling aeration parameters;
the MABR membrane component (23) is a hollow fiber membrane, the pore size range of the membrane is 0.01-0.5 mu m, the porosity of the membrane is 30-90%, and a biological membrane is attached to the surface of the membrane component for growth;
said air filter (19); an intake valve (20); an aeration fan (21); the air inlet flow meter (22) jointly forms an aeration system, wherein the air filter (19) is used for dehumidifying, dedusting and pressure regulation of air, and the air inlet pressure is 300-350 mbar;
the first online monitoring electrode (27); the second online monitoring electrode (28) and the automatic control system (29) jointly form an online feedback control system for monitoring and controlling NH at the tail ends of the MABR reaction area (1-3) and the anammox granular sludge area (1-1) in real time4 +-N、NO2 --N、NO3 --a value of N.
A one-stage EGSB anaerobic ammonia oxidation device based on MABR comprises the following specific operation steps:
water inlet operation: opening a water inlet valve (17), starting a water inlet pump (18), setting the flow through a water inlet flow meter (16), and enabling raw water in a water inlet tank (15) to enter a device main body (1) through a first perforated water distributor (13);
(II) air inlet operation: opening an air inlet valve (20), starting an aeration fan (21), setting air volume through an air inlet flow meter (22), dedusting and dehumidifying air through an air filter (19), controlling pressure and then entering an MABR membrane assembly (23);
(III) tail gas monitoring: opening a tail gas valve (25), discharging tail gas of the MABR membrane component (23), and recording values of a tail gas oxygen concentration determinator (24) and a tail gas flowmeter (26) for calculating oxygen utilization efficiency and regulating aeration parameters;
(IV) refluxing operation: the MABR reaction zone (1-3) and the anammox granular sludge zone (1-1) are respectively provided with an independent reflux system, and reflux regulation and control are carried out according to monitoring values of a first online monitoring electrode (27) and a second online monitoring electrode (28):
MABR reaction zone (1-3): opening a third internal reflux valve (9), starting a third internal reflux pump (11), adjusting a third internal reflux flowmeter (10) according to a monitoring value of the first online monitoring electrode (27), and maintaining NH4 +-N and NO2 --the mass concentration ratio of N is between 1:1 and 1: 1.5;
anammox granular sludge zone (1-1): opening the main internal reflux valve (3), opening the second internal reflux valve (5), starting the second internal reflux pump (8), adjusting the second internal reflux flowmeter (7) according to the monitoring value of the second online monitoring electrode (28), and maintaining NH4 +-N and NO2 --no N concentration is higher than 10 mg/L;
(V) MABR flushing operation: the surface biological membrane of the MABR membrane component (23) is not too thick, and is required to be washed regularly, an aged biological layer is eliminated, the first internal reflux valve (4) is opened, the first internal reflux pump (12) is started, the first internal reflux flowmeter (6) is adjusted, and the biological membrane of the MABR membrane component (23) is washed for 10min/48 h;
in the steps (II) and (III), the air flow is set through the air inlet flow meter (22), the air filter (19) removes dust and moisture, controls the pressure, monitors the values of the tail gas oxygen concentration determinator (24) and the tail gas flow meter (26), calculates the oxygen utilization efficiency, and realizes the accurate oxygen supply regulation and control;
the step (IV) is to monitor the electrode (27) and the second electrode on lineThe monitoring feedback of the two on-line monitoring electrodes (28) flexibly regulates and controls the backflow of the MABR reaction area (1-3) and the anammox granular sludge area (1-1) so that the water quality at the tail end of the MABR reaction area (1-3) meets the NH requirement of the inflow water of the anammox granular sludge area (1-1)4 +-N and NO2 -The mass concentration ratio of N is between 1:1 and 1:1.5, and the water quality of the effluent of the anaerobic ammonia oxidation granular sludge area (1-1) is regulated and controlled in real time;
and (V) under the working condition of operation of the backflow operation (IV), the regular flushing of the biomembrane on the surface of the MABR membrane assembly (23) is completed through the opening and closing of the first internal backflow valve (4), the starting and stopping of the first internal backflow pump (12) and the adjustment of the first internal backflow flowmeter (6).
The utility model has the advantages of
Compared with the existing one-section type EGSB anaerobic ammonia oxidation device, the utility model has the following advantages:
(1) MABR and EGSB are coupled, and effective enrichment of AOB and elimination of NOB are realized through the regulation and control operation of accurate oxygen supply, so that substrate guarantee is provided for the effective implementation of the anaerobic ammonia oxidation reaction;
(2) the MABR membrane component can meet the requirement of accurate oxygen supply and also serves as a biological carrier, so that the biomass of the biological membrane is large, the food chain length is long, and AOB is not easy to lose;
(3) the AOB reaction zone and the anaerobic ammonia oxidation reaction zone of the granular sludge of the MABR are separated, and an online monitoring feedback system and a backflow regulation and control system are respectively arranged, so that the running efficiency of the EGSB system is maximized while the optimized regulation and control of the two reaction zones are respectively met;
(4) the aeration energy consumption of the MABR membrane component is low, and the overall operation cost of the system is reduced;
(5) the EGSB internal reflux system is flexible and changeable, the operation requirements of the two reaction zones are met, and the flushing regulation and control of the biofilm thickness of the MABR membrane component can be realized.
Drawings
FIG. 1 is a schematic view of the apparatus of the present invention.
A device main body (1); an anammox granular sludge zone (1-1); a screen plate flange (1-2); an MABR reaction zone (1-3); a three-phase separator (2); an internal reflux main valve (3); a first internal return valve (4); a second internal return valve (5); a first internal reflux flow meter (6); a second internal reflux flow meter (7); a second internal reflux pump (8); a third internal return valve (9); a third internal reflux flow meter (10); a third internal reflux pump (11); a first internal reflux pump (12); a first perforated water distributor (13); a second perforated water distributor (14); a water inlet tank (15); a water inflow meter (16); a water inlet valve (17); a water inlet pump (18); an air filter (19); an intake valve (20); an aeration fan (21); an intake air flow meter (22); a MABR membrane module (23); an exhaust gas oxygen concentration measuring instrument (24); an exhaust valve (25); an exhaust gas flow meter (26); a first in-line monitoring electrode (27); a second on-line monitoring electrode (28); an autonomous system (29); an effluent overflow weir (30); a U-shaped water outlet (31); a gas production valve (32); a reactor vent valve (33);
Detailed Description
An embodiment of the present invention will be described below with reference to fig. 1.
The volume ratio of the anaerobic ammonia oxidation granular sludge area (1-1) to the MABR reaction area (1-3) is maintained between 1: 1;
the sieve plate flange (1-2) has the aperture range of 1.5mm and is used for intercepting a biological membrane dropped from the surface of the MABR membrane component (23) to enter an anaerobic ammonia oxidation granular sludge area (1-1);
the MABR membrane component (23) is a hollow fiber membrane, the membrane aperture is 0.01 mu m, the membrane porosity is 75%, and a biological membrane is attached to the surface of the membrane component for growth; the membrane module tail gas system comprises: an exhaust gas oxygen concentration measuring instrument (24); an exhaust valve (25); the tail gas flowmeter (26) is used for calculating the utilization efficiency of oxygen and regulating and controlling aeration parameters;
said air filter (19); an intake valve (20); an aeration fan (21); the air intake flow meter (22) jointly forms an aeration system, wherein an air filter (19) is used for dehumidifying, dedusting and pressure regulation of air, and the air intake pressure is 300 mbar.
A one-stage EGSB anaerobic ammonia oxidation device based on MABR comprises the following implementation operation steps:
water inlet operation: opening a water inlet valve (17), starting a water inlet pump (18), setting the flow through a water inlet flow meter (16), and enabling raw water in a water inlet tank (15) to enter a device main body (1) through a first perforated water distributor (13);
(II) air inlet operation: opening an air inlet valve (20), starting an aeration fan (21), setting air volume through an air inlet flow meter (22), dedusting and dehumidifying air through an air filter (19), controlling pressure and then entering an MABR membrane assembly (23);
(III) tail gas monitoring: opening a tail gas valve (25), discharging tail gas of the MABR membrane component (23), and recording values of a tail gas oxygen concentration determinator (24) and a tail gas flowmeter (26) for calculating oxygen utilization efficiency and regulating aeration parameters;
(IV) refluxing operation: the MABR reaction zone (1-3) and the anammox granular sludge zone (1-1) are respectively provided with an independent reflux system, and reflux regulation and control are carried out according to monitoring values of a first online monitoring electrode (27) and a second online monitoring electrode (28):
MABR reaction zone (1-3): opening a third internal reflux valve (9), starting a third internal reflux pump (11), adjusting a third internal reflux flowmeter (10) according to a monitoring value of the first online monitoring electrode (27), and maintaining NH4 +-N and NO2 --the mass concentration ratio of N is between 1:1 and 1: 1.5;
anammox granular sludge zone (1-1): opening the main internal reflux valve (3), opening the second internal reflux valve (5), starting the second internal reflux pump (8), adjusting the second internal reflux flowmeter (7) according to the monitoring value of the second online monitoring electrode (28), and maintaining NH4 +-N and NO2 --no N concentration is higher than 5 mg/L;
(V) MABR flushing operation: the surface biological membrane of the MABR membrane component (23) is not too thick, and is required to be washed regularly, an aged biological layer is eliminated, the first internal reflux valve (4) is opened, the first internal reflux pump (12) is started, the first internal reflux flowmeter (6) is adjusted, and the biological membrane of the MABR membrane component (23) is washed for 10min/48 h;
example 1
(1) Starting and domesticating an EGSB reactor:
inoculating floc AOB sludge into an MABR reaction zone (1-3) with the inoculation concentration of 4 g/L;
inoculating anaerobic ammonia oxidation granular sludge with the grain diameter of about 2mm and the inoculation concentration of 8g/L into the anaerobic ammonia oxidation granular sludge area (1-1);
feed water NH4 +Controlling the N concentration at 50-100mg/L, controlling the pH of inlet water at 7.5-7.8, and simultaneously adding trace elements and nutrient salts, wherein the specific formula is as follows:
TABLE 1 formulation of trace elements and nutrient salts
Figure DEST_PATH_GDA0003430470670000071
Starting a domestication stage, namely an MABR reaction area (1-3), opening a third internal reflux valve (9), starting a third internal reflux pump (11), adjusting a third internal reflux flowmeter (10) according to a monitoring value of a first online monitoring electrode (27), and maintaining NH4 +-N and NO2 --the mass concentration ratio of N is between 1:1 and 1: 1.5;
anammox granular sludge zone (1-1): opening the main internal reflux valve (3), opening the second internal reflux valve (5), starting the second internal reflux pump (8), adjusting the second internal reflux flowmeter (7) according to the monitoring value of the second online monitoring electrode (28), and maintaining NH4 +-N and NO2 --N concentrations are all below 5 mg/L;
NH after 120d operation under the acclimatization working condition4 +The removal rate of-N reaches more than 95 percent, and the effluent NO3 -The concentration of N is about 15mg/L, the theoretical yield is met, a biological membrane is formed on the surface of the MABR membrane component, and the concentration of the anaerobic ammonia oxidation sludge is increased to 10 g/L.
(2) The EGSB reactor operates stably: on the basis of successful acclimatization starting, feeding water NH4 +Controlling the N concentration at 150mg/L, controlling the pH of inlet water at 7.5-7.8, and keeping the adding concentration of trace elements and nutrient salts unchanged;
the MABR reaction zone (1-3) is opened, a third internal reflux valve (9) is opened, a third internal reflux pump (11) is started, a third internal reflux flowmeter (10) is adjusted according to the monitoring value of the first online monitoring electrode (27), and NH is maintained4 +-N and NO2 -A mass concentration ratio of-N in the range of 1:1 to 1:1.5A (c) is added;
opening an internal reflux main valve (3) in an anaerobic ammonia oxidation granular sludge area (1-1), opening a second internal reflux valve (5), starting a second internal reflux pump (8), adjusting a second internal reflux flowmeter (7) according to a monitoring value of a second online monitoring electrode (28), and maintaining NH4 +-N and NO2 --N concentrations are all below 5mg/L, NH4 +The removal rate of-N is maintained to be more than 95 percent, and NO is discharged3 -The concentration of N is about 20mg/L, corresponding to the theoretical yield.
(3) MABR flushing operation: and during the stable operation of the EGSB reactor, the MABR membrane module is periodically flushed, the first internal reflux valve (4) is opened, the first internal reflux pump (12) is started, the first internal reflux flowmeter (6) is adjusted, and the biological membrane of the MABR membrane module (23) is flushed for 10min/48 h.
(4) Compared with the traditional EGSB, the one-stage EGSB anaerobic ammonia oxidation device based on the MABR has better operation stability and saves about 35% of aeration energy consumption under the conditions of the same operation scale and water quality.
The above description is only a preferred embodiment of the present invention, and is not intended to limit the present invention, and it will be apparent to those skilled in the art that other modifications and variations can be made without departing from the main structure and principle of the utility model, and these modifications and variations are considered to be within the scope of the present invention.

Claims (4)

1. A one-stage type EGSB anaerobic ammonia oxidation device based on MABR is characterized in that: comprises a device body (1); an anammox granular sludge zone (1-1); a screen plate flange (1-2); an MABR reaction zone (1-3); a three-phase separator (2); an internal reflux main valve (3); a first internal return valve (4); a second internal return valve (5); a first internal reflux flow meter (6); a second internal reflux flow meter (7); a second internal reflux pump (8); a third internal return valve (9); a third internal reflux flow meter (10); a third internal reflux pump (11); a first internal reflux pump (12); a first perforated water distributor (13); a second perforated water distributor (14); a water inlet tank (15); a water inflow meter (16); a water inlet valve (17); a water inlet pump (18); an air filter (19); an intake valve (20); an aeration fan (21); an intake air flow meter (22); a MABR membrane module (23); an exhaust gas oxygen concentration measuring instrument (24); an exhaust valve (25); an exhaust gas flow meter (26); a first in-line monitoring electrode (27); a second on-line monitoring electrode (28); an autonomous system (29); an effluent overflow weir (30); a U-shaped water outlet (31); a gas production valve (32); a reactor vent valve (33);
the device main body (1) is divided into an anaerobic ammonia oxidation granular sludge area (1-1) and an MABR reaction area (1-3) by a sieve plate flange (1-2);
the internal reflux system of the device body (1) comprises: an internal reflux main valve (3); a first internal return valve (4); a second internal return valve (5); a first internal reflux flow meter (6); a second internal reflux flow meter (7); a second internal reflux pump (8); a third internal return valve (9); a third internal reflux flow meter (10); a third internal reflux pump (11); a first internal reflux pump (12); a first perforated water distributor (13); a second perforated water distributor (14);
the internal reflux main valve (3) is sequentially connected with a first internal reflux valve (4); a first internal reflux flow meter (6); a first internal reflux pump (12) and a first perforated water distributor (13); the internal reflux main valve (3) is sequentially connected with a second internal reflux valve (5); a second internal reflux flow meter (7);
a second internal reflux pump (8) and a second perforated water distributor (14); the first perforated water distributor (13) is arranged in the MABR reaction zone (1-3); the second perforated water distributor (14) is arranged in the anaerobic ammonia oxidation granular sludge area (1-1);
a third internal return valve (9); a third internal reflux flow meter (10); the third internal reflux pump (11) and the MABR reaction zone (1-3) form a cycle;
the MABR membrane module (23) tail gas system comprises: an exhaust gas oxygen concentration measuring instrument (24); an exhaust gas valve (25) and an exhaust gas flowmeter (26);
said air filter (19); an intake valve (20); an aeration fan (21); the air inlet flow meters (22) jointly form an aeration system;
the first online monitoring electrode (27); the second online monitoring electrode (28) and the automatic control system (29) jointly form an online feedback regulation and control system.
2. The MABR-based one-stage EGSB anammox apparatus of claim 1, wherein: the volume ratio of the anaerobic ammonia oxidation granular sludge area (1-1) to the MABR reaction area (1-3) is maintained between 1:1 and 3: 1.
3. The MABR-based one-stage EGSB anammox apparatus of claim 1, wherein: the aperture range of the sieve plate flange (1-2) is 1-3 mm.
4. The MABR-based one-stage EGSB anammox apparatus of claim 1, wherein: the MABR membrane component (23) is a hollow fiber membrane, the pore diameter range of the membrane is 0.01-0.5 mu m, the porosity of the membrane is 30-90%, and a biological membrane is attached to the surface of the membrane component for growth.
CN202120496092.2U 2021-03-09 2021-03-09 One-section type EGSB anaerobic ammonia oxidation device based on MABR Active CN216141327U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202120496092.2U CN216141327U (en) 2021-03-09 2021-03-09 One-section type EGSB anaerobic ammonia oxidation device based on MABR

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202120496092.2U CN216141327U (en) 2021-03-09 2021-03-09 One-section type EGSB anaerobic ammonia oxidation device based on MABR

Publications (1)

Publication Number Publication Date
CN216141327U true CN216141327U (en) 2022-03-29

Family

ID=80798108

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202120496092.2U Active CN216141327U (en) 2021-03-09 2021-03-09 One-section type EGSB anaerobic ammonia oxidation device based on MABR

Country Status (1)

Country Link
CN (1) CN216141327U (en)

Similar Documents

Publication Publication Date Title
CN108178302B (en) Device and method for integrating rapid start and stable maintenance of shortcut nitrification/anaerobic ammonia oxidation based on hydroxylamine
CN107162193B (en) Device and method for treating domestic sewage by low-oxygen nitrification coupled with short-range denitrification anaerobic ammonia oxidation
CN113023881B (en) Aeration quantity and internal reflux quantity optimal control system and method based on MABR (moving average aeration ratio) process
CN110240260B (en) Sewage treatment equipment and method based on biomembrane thickness in-situ control
CN105541021B (en) A kind of quick start method of the continuous stream improvement UCT autotrophic denitrification dephosphorization process based on Anammox
CN105776539B (en) The application process of the autotrophic denitrification device of low carbon source urban sewage segmental influent multistage A/O techniques based on short-cut denitrification
CN110217889B (en) Device and method for treating urban domestic sewage by two-stage reinforced semi-shortcut nitrification coupled anaerobic ammonia oxidation based on biomembrane
CN111422993B (en) Method for rapidly starting autotrophic ammonia oxidation by using heterotrophic denitrification granular sludge
CN106115915A (en) Low C/N is than the apparatus and method of city domestic sewage short-cut denitrification/short distance nitration Anammox biomembrane process
CN107162186A (en) A kind of apparatus and method of the municipal sewage Anammox autotrophic denitrification based on granule sludge
CN109264850A (en) Integral anaerobic ammoxidation film bioelectrochemical system and sewage water denitrification remove the treatment process of carbon
CN106830302A (en) The MBR complete nitrifications bacterium concentrating device and its method of dissolved oxygen Automated condtrol
CN112479370A (en) Sewage autotrophic nitrogen removal device and method
CN114229995B (en) System and process for synchronous denitrification and decarbonization of pig raising wastewater
CN216712108U (en) Device for rapidly enriching and culturing anaerobic ammonium oxidation bacteria
CN103601294B (en) Method and system for realization of autotrophic nitrogen removal of micro polluted water
CN101851022B (en) Short-distance nitration membrane biological reactor process and processing device thereof
CN114455782A (en) Embedded short-cut nitrification coupling denitrification device for inorganic ammonia nitrogen wastewater
CN208166668U (en) A kind of device fast implementing high ammonia-nitrogen wastewater BAF integration autotrophic denitrification
CN106542636A (en) A kind of method of quick startup whole process autotrophic denitrification
CN112830577A (en) One-section type EGSB anaerobic ammonia oxidation device based on MABR
CN113087321A (en) Container formula electro-Fenton biochemical pond MBR membrane allies oneself with uses water treatment system
CN112340843A (en) Device and method for realizing integrated decarbonization and denitrification of methanogenesis anaerobic ammonium oxidation
CN216141327U (en) One-section type EGSB anaerobic ammonia oxidation device based on MABR
CN106754483A (en) A kind of ammonia nitrogen stream adds the ammonia oxidizing bacteria bacterium screening and Enrichment culture method of periodic running

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant