CN205115228U - Municipal sewage regeneration treatment device - Google Patents

Municipal sewage regeneration treatment device Download PDF

Info

Publication number
CN205115228U
CN205115228U CN201520872745.7U CN201520872745U CN205115228U CN 205115228 U CN205115228 U CN 205115228U CN 201520872745 U CN201520872745 U CN 201520872745U CN 205115228 U CN205115228 U CN 205115228U
Authority
CN
China
Prior art keywords
oxygen
tank
aeration
sewage treatment
pond
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
CN201520872745.7U
Other languages
Chinese (zh)
Inventor
张树军
张亮
蒋勇
马淑勍
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 Drainage Group Co Ltd
Original Assignee
Beijing Drainage Group 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 Drainage Group Co Ltd filed Critical Beijing Drainage Group Co Ltd
Priority to CN201520872745.7U priority Critical patent/CN205115228U/en
Application granted granted Critical
Publication of CN205115228U publication Critical patent/CN205115228U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Treatment Of Water By Oxidation Or Reduction (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The utility model relates to a municipal sewage regeneration treatment device, including blast aeration system and sewage treatment system, the blast aeration system includes embrane method air separation machine, oxygen compression jar and nitrogen gas compression jar, sewage treatment system includes oxygen purifier, ozone generator, aeration tank, sedimentation tank, from oxygen denitrogenation pond, two sink ponds, ozone contact chamber, municipal sewage through the inlet tube in proper order through the aeration tank connected according to the preface, sedimentation tank, from oxygen denitrogenation pond, two sink ponds, ozone contact chamber and handle the back and obtain the recycled water through the outlet pipe, ozone generator is connected through the ozone aeration dish of valve with oxygen purifier and ozone contact chamber bottom respectively. This processing apparatus and processing method have: simple structure, reasonable in design, manipulate nimble convenience, treatment effeciency high, go out that water quality of water is high, the device operation is stable and advantage such as safe and reliable.

Description

A kind of regeneration of urban sewage treatment unit
Technical field
The utility model relates to urban sewage treatment technology field, particularly relate to a kind of regeneration of urban sewage treatment unit, this device comprises high loading organics removal reactor, short distance nitration-anaerobic ammoxidation denitrification reactor and ozone oxidation reaction device, realized oxygenation and the mixing requirement of different reactor by air separation, can be applicable to municipal sewage treatment, technical process is simple, red-tape operati is flexible, and effluent quality is high.
Background technology
The most general technique of municipal sewage treatment is activated sludge process.Traditional activated sludge process, by active sludge alternate run under the environment of anaerobic-aerobic, can realize multiple pollutant simultaneously and remove.In aerobic environment, microorganism carries out nitration reaction and utilizes organism to carry out anti-nitration reaction under removing partial organic substances, anoxia condition realizing denitrogenation.The denitrification effect of conventional nitration denitrification process affects significantly by organic, and under low ratio of carbon to ammonium condition, nitric efficiency is general not high.The municipal effluent carbon-nitrogen ratio of China is generally on the low side, and the organism in water inlet fails efficiency utilization, causes water outlet nitrogen element to be difficult to stably reaching standard, does not meet the basic demand of reclaimed water reuse.
Anaerobic ammonia oxidation process appear as municipal sewage treatment and regeneration provides new thinking.Ammonia nitrogen and nitrite directly can be converted to nitrogen by anaerobic ammonia oxidation process.And anaerobic ammonia oxidizing bacteria is chemosynthetic autotroph, be electron donor without the need for machine carbon source in denitrification process, the corresponding minimizing of sludge yield.Denitrification process based on Anammox technology can save aeration energy consumption compared to the nitration denitrification technique of routine, does not need extra organism as carbon source, has advantage significantly.What anaerobic ammonia oxidation process realized that carbon removes with nitrogen pollutant is separated, and changes sewage treatment process.
Technical process based on Anammox technology it is also proposed new requirement to aeration mode.The appropriate design of aerating system and steady running are the essential condition that activated sludge process realizes pollutant removal.Aeration can provide oxygen for the microorganism of active sludge, in order to oxidation of organic compounds and ammonia nitrogen; In addition, aeration can realize good gas-liquid-solid three-phase mixing, and reinforcing mass transfer, improves contaminant removal efficiency.In traditional activated sludge process, oxygen mass transfer efficiency is generally limited, and therefore general passing through increases aeration rate and improve the oxygen supply that oxygen-transfer efficiency realizes abundance, and under this condition, the mixture strength of system does not belong to restricted condition.Therefore conventional aeration mode can realize good oxygenation and mixing effect simultaneously, the effective pollutent removed in sewage.Based on the urban sewage treatment process flow process of Anammox technology, the reactive system bearing organic matter removal needs enough dissolved oxygens, and aeration rate increases.Organic removal reactor carries out pure oxygen aeration, can improve reaction efficiency, reduces aeration energy consumption.And short distance nitration-anaerobic ammoxidation reactor mainly realizes the removal process of polluted by nitrogen, oxygen requirement significantly reduces, under whole system needs to maintain low DO condition.Traditional aeration mode is adopted to be difficult to meet denitrogenation requirement.Under higher aeration rate, although good oxidation effect can be realized, uncontrollable rational dissolved oxygen concentration.When after reduction aeration rate, under low DO condition, the mixed effect of system weakens, and causes the elimination capacity of system to reduce.For Anammox technology Problems existing in sewage disposal application, should consider how to optimize aeration mode, for the removal of organism and nitrogen pollutant provides rational aeration rate and mixture strength, and further optimize its control strategy, by the synthetic operation with advanced treatment system, realize the reuse water water outlet requirement of high-quality.Therefore, study a kind of regeneration of urban sewage treatment unit and there is important Research Significance.
Utility model content
For the deficiency of regeneration of urban sewage treatment unit in prior art, the purpose of this utility model is: provide a kind of regeneration of urban sewage treatment unit and treatment process thereof, this treatment unit and treatment process have: structure is simple, reasonable in design, it is flexible and convenient to use to operate, processing efficiency is high, effluent quality is high, plant running is stable and the advantage such as safe and reliable.
To achieve these goals, the utility model adopts following technical scheme to realize:
A kind of regeneration of urban sewage treatment unit, this regenerating treater comprises blast aeration system and Sewage treatment systems; Described blast aeration system comprises membrane based air separation machine, oxygen compression tank and nitrogen compressed tanks; Described membrane based air separation machine is also provided with oxygen outlet valve and nitrogen outlet valve, described oxygen outlet valve is connected with nitrogen compressed tanks with described oxygen compression tank respectively by penstock with nitrogen outlet valve; Described Sewage treatment systems comprise oxygen purifier, ozonizer, aeration tank, settling tank, from oxygen denitrification tank, second pond, ozone contact tank; Described oxygen compression tank to be connected the aeration plate bottom described oxygen purifier and described aeration tank respectively by penstock with valve; Described nitrogen compressed tanks is connected by the microporous aeration disc of valve with described bottom in oxygen denitrification tank; Municipal effluent by water inlet pipe successively through sequentially connect described aeration tank, settling tank, after oxygen denitrification tank, second pond, ozone contact tank process, obtain reuse water by rising pipe; Described settling tank is connected with described water inlet pipe by settling tank reflux sludge tube; Described second pond is connected with the described water-in from oxygen denitrification tank by second pond reflux sludge tube; Described ozonizer is connected with the ozonation aerated dish bottom described ozone contact tank with described oxygen purifier respectively by valve.
As the further improvement of technique scheme, described membrane based air separation machine, oxygen compression tank, nitrogen compressed tanks, oxygen purifier and ozonizer are provided with gas manometer and gas meter, come adjustable pressure value and gas flow values by valve.
As the further improvement of technique scheme, described regenerating treater also comprises automatic control system, is also provided with gas concentration detector in described oxygen compression tank, nitrogen compressed tanks; Described rising pipe is also provided with COD concentration detector; Described automatic control system and described gas concentration detector, COD concentration detector, NH 4 +concentration detector, gaseous tension machine are connected with gas meter Data Control.
As the further improvement of technique scheme, described regenerating treater comprises secondary treatment yielding water device, and described ozone contact tank is communicated with described secondary treatment yielding water device with online liquid meter pipeline by controlled variable frequency pump.
As the further improvement of technique scheme, described regenerating treater also comprises mud recycling system, and described mud recycling system comprises mire preprocess system and drying sludge disinfection system; Wherein said mire preprocess system is used for that the mud in described settling tank and described second pond is added straw and stirs; Described sludge dry system is used for the mud obtained through mire preprocess system process to carry out oven dry and sterilization.
Compared with regeneration of urban sewage treatment unit in prior art, regenerating treater of the present utility model and treatment process tool thereof is adopted to have the following advantages:
(1) high loading Sludge System utilizes pure oxygen aeration, improves the removal efficiency of COD, reduces pond and holds.
(2) autotrophic denitrification system utilizes the gas being rich in nitrogen to carry out recurrence mixing, the dissolved oxygen of reduction can be maintained when ensureing mixed effect, be conducive to the growth of NOB in suppression system, thus ensure the steady running of anaerobic ammonia oxidation process.
(3) source of oxygen after air separation is prepared into ozone further, carries out advanced oxidation process to sewage, effectively can reduce the microbiology risk of water outlet, reduces effluent color dilution, increases the feasibility of reuse.
Accompanying drawing explanation
Accompanying drawing 1 is the structural representation of the utility model regeneration of urban sewage treatment unit.
In above-mentioned accompanying drawing, the concrete meaning of each Reference numeral is as follows:
1 membrane based air separation machine; 2 oxygen outlet valves; 3 nitrogen outlet valves; 4 penstocks; 5 oxygen compression tanks; 6 nitrogen compressed tanks, 7 oxygen purifiers; 8 ozonizers; 9 valves; 10 settling tank reflux sludge tubes; 11 second pond reflux sludge tubes; 12 aeration plates; 13 microporous aeration discs; 14 ozonation aerated dishes; 15 water inlet pipes; 16 aeration tanks; 17 settling tanks; 18 autotrophic denitrification ponds; 19 second ponds; 20 ozone contact tanks; 21 rising pipes; 22 ozone accumulator tanks.
Embodiment
Structure below in conjunction with accompanying drawing 1 pair of the utility model regeneration of urban sewage treatment unit is described in detail.
A kind of regeneration of urban sewage treatment unit, this regenerating treater comprises blast aeration system and Sewage treatment systems; Described blast aeration system comprises membrane based air separation machine 1, oxygen compression tank 5 and nitrogen compressed tanks 6; Described membrane based air separation machine 1 is also provided with oxygen outlet valve 2 and nitrogen outlet valve 3, described oxygen outlet valve 2 is connected with nitrogen compressed tanks 6 with described oxygen compression tank 5 respectively by penstock 4 with nitrogen outlet valve 3; Described Sewage treatment systems comprise oxygen purifier 7, ozonizer 8, aeration tank 16, settling tank 17, from oxygen denitrification tank 18, second pond 19, ozone contact tank 20; Described oxygen compression tank 5 to be connected the aeration plate 12 bottom described oxygen purifier and described aeration tank respectively by penstock 4 with valve 9; Described nitrogen compressed tanks is connected by the microporous aeration disc 13 of valve 9 with described bottom in oxygen denitrification tank; Municipal effluent by water inlet pipe 15 successively through sequentially connect described aeration tank, settling tank, after oxygen denitrification tank, second pond, ozone contact tank process, obtain reuse water by rising pipe 21; Described settling tank is connected with described water inlet pipe by settling tank reflux sludge tube 10; Described second pond is connected with the described water-in from oxygen denitrification tank by second pond reflux sludge tube 11; Described ozonizer is connected with the ozonation aerated dish 14 bottom described ozone contact tank with described oxygen purifier respectively by valve.Described membrane based air separation machine, oxygen compression tank, nitrogen compressed tanks, oxygen purifier and ozonizer are provided with gas manometer and gas meter, come adjustable pressure value and gas flow values by valve.Described regenerating treater also comprises automatic control system, is also provided with gas concentration detector in described oxygen compression tank, nitrogen compressed tanks; Described rising pipe is also provided with COD concentration detector and NH 4 +concentration detector; Described automatic control system and described gas concentration detector, COD concentration detector, NH 4 +concentration detector, gaseous tension machine are connected with gas meter Data Control.Described regenerating treater comprises secondary treatment yielding water device, and described ozone contact tank is communicated with described secondary treatment yielding water device with online liquid meter pipeline by controlled variable frequency pump.Described regenerating treater also comprises mud recycling system, and described mud recycling system comprises mire preprocess system and drying sludge disinfection system; Wherein said mire preprocess system is used for that the mud in described settling tank and described second pond is added straw and stirs; Described sludge dry system is used for the mud obtained through mire preprocess system process to carry out oven dry and sterilization.
Above-mentioned is can understand for ease of those skilled in the art and apply the utility model to the description of embodiment.Person skilled in the art obviously easily can make various amendment to these embodiments, and General Principle described herein is applied in other embodiments and need not through performing creative labour.Therefore, the utility model is not limited to embodiment here, and those skilled in the art, according to announcement of the present utility model, do not depart from improvement that the utility model category makes and amendment all should within protection domain of the present utility model.

Claims (5)

1. a regeneration of urban sewage treatment unit, is characterized in that: this regenerating treater comprises blast aeration system and Sewage treatment systems; Described blast aeration system comprises membrane based air separation machine (1), oxygen compression tank (5) and nitrogen compressed tanks (6); Described membrane based air separation machine (1) is also provided with oxygen outlet valve (2) and nitrogen outlet valve (3), described oxygen outlet valve (2) is connected with nitrogen compressed tanks (6) with described oxygen compression tank (5) respectively by penstock (4) with nitrogen outlet valve (3); Described Sewage treatment systems comprise oxygen purifier (7), ozonizer (8), aeration tank (16), settling tank (17), from oxygen denitrification tank (18), second pond (19), ozone contact tank (20); Described oxygen compression tank (5) to be connected the aeration plate (12) bottom described oxygen purifier and described aeration tank respectively by penstock (4) with valve (9); Described nitrogen compressed tanks is connected by the microporous aeration disc (13) of valve (9) with described bottom in oxygen denitrification tank; Municipal effluent by water inlet pipe (15) successively through sequentially connect described aeration tank, settling tank, after oxygen denitrification tank, second pond, ozone contact tank process, obtain reuse water by rising pipe (21); Described settling tank is connected with described water inlet pipe by settling tank reflux sludge tube (10); Described second pond is connected with the described water-in from oxygen denitrification tank by second pond reflux sludge tube (11); Described ozonizer is connected with the ozonation aerated dish (14) bottom described ozone contact tank with described oxygen purifier respectively by valve.
2. a kind of regeneration of urban sewage treatment unit according to claim 1, it is characterized in that: described membrane based air separation machine, oxygen compression tank, nitrogen compressed tanks, oxygen purifier and ozonizer are provided with gas manometer and gas meter, come adjustable pressure value and gas flow values by valve.
3. a kind of regeneration of urban sewage treatment unit according to claim 1, is characterized in that: described regenerating treater also comprises automatic control system, is also provided with gas concentration detector in described oxygen compression tank, nitrogen compressed tanks; Described rising pipe is also provided with COD concentration detector; Described automatic control system and described gas concentration detector, COD concentration detector, NH 4 +concentration detector, gaseous tension machine are connected with gas meter Data Control.
4. a kind of regeneration of urban sewage treatment unit according to claim 1, it is characterized in that: described regenerating treater comprises secondary treatment yielding water device, described ozone contact tank is communicated with described secondary treatment yielding water device with online liquid meter pipeline by controlled variable frequency pump.
5. a kind of regeneration of urban sewage treatment unit according to claim 1, is characterized in that: described regenerating treater also comprises mud recycling system, and described mud recycling system comprises mire preprocess system and drying sludge disinfection system; Wherein said mire preprocess system is used for that the mud in described settling tank and described second pond is added straw and stirs; Described sludge dry system is used for the mud obtained through mire preprocess system process to carry out oven dry and sterilization.
CN201520872745.7U 2015-11-04 2015-11-04 Municipal sewage regeneration treatment device Active CN205115228U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201520872745.7U CN205115228U (en) 2015-11-04 2015-11-04 Municipal sewage regeneration treatment device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201520872745.7U CN205115228U (en) 2015-11-04 2015-11-04 Municipal sewage regeneration treatment device

Publications (1)

Publication Number Publication Date
CN205115228U true CN205115228U (en) 2016-03-30

Family

ID=55570852

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201520872745.7U Active CN205115228U (en) 2015-11-04 2015-11-04 Municipal sewage regeneration treatment device

Country Status (1)

Country Link
CN (1) CN205115228U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105254129A (en) * 2015-11-04 2016-01-20 北京城市排水集团有限责任公司 Municipal sewage reclamation treatment device and treatment method adopting same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105254129A (en) * 2015-11-04 2016-01-20 北京城市排水集团有限责任公司 Municipal sewage reclamation treatment device and treatment method adopting same

Similar Documents

Publication Publication Date Title
CN105384247B (en) It is a kind of that the method that part denitrification couples Anammox denitrogenation is realized by A/O biomembrane process
CN104591473B (en) Advanced nitrogen and phosphorus removal technology
CN203419825U (en) Landfill leachate advanced treatment device
CN105174622A (en) System and method suitable for treating high concentration organic wastewater
CN201932988U (en) Anaerobic/aerobic contact oxidation membrane bioreactor
CN109912145B (en) Aerobic granular sludge power generation device
CN111252889A (en) High-salinity wastewater treatment device and method combining bacteria-algae symbiosis method and membrane biofilm reactor
CN103641268B (en) Two-stage biological reactor for treatment percolate instrument and supplies
CN107935300B (en) Process device and method for treating landfill leachate by non-membrane method
CN104556550A (en) High-efficiency and low-energy MBR device and method capable of delaying membrane pollution
CN101200331B (en) Method for producing reclaimed water by membrane bioreactor-ozone combination technique
CN204111537U (en) The device of internal carbon source denitrification coupling Anammox Treating Municipal Sewage
CN205115228U (en) Municipal sewage regeneration treatment device
CN208562049U (en) A kind of three-dimensional rural sewage treatment equipment
CN203269735U (en) Equipment for treating rubbish leachate by utilizing two-stage bioreactors
CN102887613A (en) Treatment method for high-concentration industrial wastewater
CN105984991A (en) Process for advanced treatment of sewage
CN104743751A (en) A/O (anaerobic/aerobiotic) sewage treatment process device and technique thereof
CN105110582B (en) A kind of sewage disposal system based on biofilm reactor and bioreactor
CN105174606B (en) A kind of membrane technology medical waste water with disinfection by ultraviolet light processes device
CN113998846A (en) Efficient carbon adsorption coupled biological nitrogen and phosphorus removal sewage treatment device and method
CN105254129B (en) A kind of regeneration of urban sewage processing unit and its processing method
CN209853942U (en) Distributed domestic sewage treatment system
CN107879471B (en) Whole-process autotrophic nitrogen removal process and device
CN106587484A (en) Reaction system for removal of nitrogen and phosphorus in domestic sewage by use of microalgae

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant