CN206359390U - A kind of high ammonia nitrogen micro-polluted raw processing system of high algae - Google Patents

A kind of high ammonia nitrogen micro-polluted raw processing system of high algae Download PDF

Info

Publication number
CN206359390U
CN206359390U CN201621357760.9U CN201621357760U CN206359390U CN 206359390 U CN206359390 U CN 206359390U CN 201621357760 U CN201621357760 U CN 201621357760U CN 206359390 U CN206359390 U CN 206359390U
Authority
CN
China
Prior art keywords
unit
algae
tank body
ammonia nitrogen
film process
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.)
Expired - Fee Related
Application number
CN201621357760.9U
Other languages
Chinese (zh)
Inventor
孔赟
邹培
邹桐
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.)
Yixing City Product Quality Supervision And Testing Institute
Wuxi City Bywater Environmental Technology Co Ltd
Original Assignee
Yixing City Product Quality Supervision And Testing Institute
Wuxi City Bywater Environmental Technology 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 Yixing City Product Quality Supervision And Testing Institute, Wuxi City Bywater Environmental Technology Co Ltd filed Critical Yixing City Product Quality Supervision And Testing Institute
Priority to CN201621357760.9U priority Critical patent/CN206359390U/en
Application granted granted Critical
Publication of CN206359390U publication Critical patent/CN206359390U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

A kind of high ammonia nitrogen micro-polluted raw processing system of high algae, can especially remove four major parts such as the high high algae-laden water treatment technology of ammonia nitrogen concentration, including coagulating sedimentation unit, absorbing unit, film process unit and disinfection unit.The handling process comprises the following steps:The high high ammonia nitrogen micro-polluted raw of algae enters coagulating sedimentation unit, and algae removes after flocculation sediment;Water outlet enters absorbing unit, and Algae toxins and organic matter are adsorbed using mode from bottom to top;Absorbing unit water outlet enters film process unit, and unit installing membrane module, film surface attachment growth biomembrane, membrane module bottom device aerator effectively removes ammonia nitrogen;Up to drinking water standard after the sterilized unit of water outlet.The utility model removes algae by chemical coagulation and physical absorption, with reference to the effect such as UF membrane and biological denitrificaion, algae and ammonia nitrogen is effectively removed.The technique floor space is small, and operating cost is low, and effluent quality is good, and with good Social benefit and economic benefit, application prospect is extensive.

Description

A kind of high ammonia nitrogen micro-polluted raw processing system of high algae
Technical field
The utility model is related to eutrophication lake storehouse micro pollution drinking water source processing technology field, more particularly to high algae height Ammonia nitrogen micro-polluted raw handling process.
Background technology
With the fast development of Chinese society economy, town and country drinking water source area is generally polluted in various degree, Hu Ku Water body eutrophication degree constantly aggravates.The Algae toxins of algae reproduction secretion cause drinking water source water quality deterioration, add water The intractability and processing cost of factory;In addition, the algae organic matter produced in algae metabolic processes is stagnant in water body environment Time length, difficult for biological degradation are stayed, causes to generate DBPs in conventional water treatment process chlorination link, very big journey Degree threatens drinking water quality safety.
The source such as chemical oxidation, bio-contact oxidation water is researched and developed on the basis of drinking water conventional treatment process both at home and abroad Preconditioning technique and charcoal absorption, ozone oxidation, ozone and activated carbon, biological activated carbon, film process even depth treatment technology, but Conventional water treatment process has been difficult to meet the algae organic matter risk triggered by water source algae pollution and disinfection by-product of drinking water It is required that.The problems such as constantly being aggravated by the situation of micro- Organic Pollutants and algae pollution for drinking water source, seeks safe efficient The high ammonia nitrogen micro-polluted water treatment technology of high algae it is extremely urgent.
Traditional micro-polluted raw handling process is generally Biological Contact Oxidation Process, is enriched with by the use of filler as bio-carrier Microorganism simultaneously forms biomembrane on filler surface, and ammonia nitrogen is converted into nitrate nitrogen under the conditions of aeration aerating by nitrobacteria, dissolves Property organic matter then by occurring absorption with biofilm contact process, decompose and the effect such as oxidation is removed, but the technique is to algae Removal effect is not good enough.Existing denitrogenation technology and algae removal technology are carried out efficient combination by the utility model, while setting up absorbing unit Algae organic matter and Algae toxins etc. are carried out effectively to remove in favor of reaching drinking water standard, algae and ammonia nitrogen is not only realized It is efficiently quick to remove, and operating cost is low, and effluent quality is good, with good Social benefit and economic benefit, application prospect Extensively.
Utility model content
The utility model purpose is to overcome existing eutrophication lake storehouse micro-polluted raw handling process is not enough to be tied there is provided one kind Structure is simple, floor space is small, and operating cost is low, and effluent quality is good, at the extensive high high ammonia nitrogen micro-polluted raw of algae of application prospect Science and engineering skill.
To realize the utility model purpose, there is provided following technical scheme:A kind of high ammonia nitrogen micro-polluted raw processing of high algae System, it is characterised in that including the coagulating sedimentation unit being sequentially connected with, absorbing unit, film process unit and disinfection unit, coagulation Precipitation unit includes tank body, is opened in the mud discharging mouth of tank base, the agitating device being arranged in tank body and the nearly top of tank body Delivery port;Absorbing unit includes being filled with tank body, the delivery port on the nearly top of water inlet, tank body of the nearly bottom of tank body, tank body Adsorbent;Film process unit includes tank body, the membrane module set in tank body, the mud discharging mouth of tank body bottom, is arranged at tank body inner membrance The water inlet of the nearly bottom of aerator and tank body below component, aerator connects air blower by aeration tube;Coagulation sinks Shallow lake unit delivery port is connected by conveyance conduit one with absorbing unit inlet seal, and absorbing unit delivery port passes through conveyance conduit Two are connected with film process unit inlet seal, and elevator pump is provided with conveyance conduit two, and membrane module top passes through conveyance conduit Three are tightly connected on disinfection unit, conveyance conduit three and are provided with pressure gauge and elevator pump, disinfection unit connection outlet terminal.
Preferably, film process unit is Nets impregnated, membrane module is tubular membrane, curtain type membrane or flat board Film.
Preferably, described disinfection unit is ultraviolet disinfection.
The utility model beneficial effect:There is advantages below compared with the prior art:1)At integrated physics, chemistry and biology Reason technology;2)Coagulation unit can rapidly and efficiently remove algae;3)Absorbing unit can suitably be adjusted according to processing water and contamination index's concentration Adsorbent amount is saved, and can effectively remove Algae toxins and algae organic matter;4)Film process unit can a large amount of biomembranes of apposition growth, Strengthened denitrification is conducive to remove algae effect;Membrane module is by algae and rejection to organics, good separating effect;5)Film process unit possesses instead Pre-washing function, membrane module is repeatable to be utilized;6)Floor space is small, and operating cost is low, and effluent quality is good, and application prospect is extensive.
Brief description of the drawings
Fig. 1 is system schematic of the present utility model.
Embodiment
Embodiment 1:A kind of high ammonia nitrogen micro-polluted raw processing system of high algae, including be sequentially connected with coagulating sedimentation unit 1, Absorbing unit 2, film process unit 3 and disinfection unit 4, coagulating sedimentation unit 1 include tank body 1.1, are opened in the bottom of tank body 1.1 The delivery port 1.4 of mud discharging mouth 1.2, the agitating device 1.3 being arranged in tank body 1.1 and the nearly top of tank body 1.1;Absorbing unit 2 Including tank body 2.1, the water inlet 2.2 of the nearly bottom of tank body 2.1, the nearly top of tank body 2.1 delivery port 2.3, be filled with tank body 2.1 Adsorbent 2.4;Film process unit 3 includes tank body 3.1, the membrane module 3.2, the mud discharging mouth of the bottom of tank body 3.1 that set in tank body 3.1 3.3rd, the aerator 3.4 of the lower section of 3.1 inner membrane member of tank body 3.2 and the water inlet 3.5 of the nearly bottom of tank body 3.1 are arranged at, is exposed Device of air 3.4 connects air blower 5 by aeration tube;The delivery port 1.4 of coagulating sedimentation unit 1 is single with absorption by conveyance conduit 1 First 2 water inlets 2.2 are tightly connected, and the delivery port 2.3 of absorbing unit 2 passes through conveyance conduit 27 and the water inlet 3.5 of film process unit 3 It is tightly connected, elevator pump 8 is provided with conveyance conduit 27, the top of membrane module 3.2 is tightly connected sterilization by conveyance conduit 39 Pressure gauge 10 and elevator pump 8, the connection outlet terminal of disinfection unit 4 are provided with unit 4, conveyance conduit 39.Film process unit 3 For Nets impregnated, membrane module 3.2 is tubular membrane, curtain type membrane or Flat Membrane.Described disinfection unit 4 disappears to be ultraviolet Poison.
A kind of high ammonia nitrogen micro-polluted raw processing system of high algae, is connected using seal for pipe joints, absorbing unit 2 and film process list Discharge pressure is improved by elevator pump between member 2 and film process unit 3 and disinfection unit 4.Its course of work is as follows:Containing the high ammonia of high algae Nitrogen micro-polluted raw is entered in coagulating sedimentation unit 1 by water inlet, and agitating device 1.3 carries out abundant in coagulating sedimentation unit 1 Stirring, algae discharged after coagulating sedimentation by mud discharging mouth 1.2, and upper strata clear water then enters the bottom of absorbing unit 2 and using from lower Upper reflux type is fully contacted with adsorbent 2.4, and Algae toxins and algae organic matter etc. are efficiently removed after absorption, absorbing unit The boosted pump 8 of 2 water outlets enters film process unit 3 after being pressurized, air blower 5 is that aerator 3.4 provides ammonia in sufficient oxygen, water body Nitrogen continues through aerator 3.4 or intermittent aerating is removed, and algae and organic matter etc. are retained and pass through mud discharging mouth by membrane module 3.2 3.3 discharges, at the same a large amount of biomembranes of the surface attachment of membrane module 3.2 growth and microorganism can strengthened denitrification remove algae effect, at film Manage after the sterilized ultraviolet disinfection of unit 4 of the water outlet of unit 3 up to drinking water standard.The pressure registration of pressure gauge 9 is recoiled when larger Wash to ensure effluent quality.

Claims (3)

1. a kind of high ammonia nitrogen micro-polluted raw processing system of high algae, it is characterised in that including be sequentially connected with coagulating sedimentation unit, Absorbing unit, film process unit and disinfection unit, coagulating sedimentation unit include tank body, are opened in the mud discharging mouth of tank base, set The delivery port on the nearly top of agitating device and tank body being placed in tank body;Absorbing unit includes tank body, the water inlet of the nearly bottom of tank body Adsorbent is filled with mouth, the delivery port on the nearly top of tank body, tank body;Film process unit includes tank body, the film group set in tank body Part, the mud discharging mouth of tank body bottom, the aerator being arranged at below tank body inner membrane member and the water inlet of the nearly bottom of tank body, expose Device of air connects air blower by aeration tube;Coagulating sedimentation unit delivery port is close by conveyance conduit one and absorbing unit water inlet Envelope connection, absorbing unit delivery port is connected with film process unit inlet seal by conveyance conduit two, set on conveyance conduit two Elevator pump is equipped with, membrane module top is tightly connected on disinfection unit, conveyance conduit three by conveyance conduit three and is provided with pressure gauge And elevator pump, disinfection unit connection outlet terminal.
2. a kind of high high ammonia nitrogen micro-polluted raw processing system of algae according to claim 1, it is characterised in that film process list Member is Nets impregnated, and membrane module is tubular membrane, curtain type membrane or Flat Membrane.
3. a kind of high high ammonia nitrogen micro-polluted raw processing system of algae according to claim 1, it is characterised in that described disappears Malicious unit is ultraviolet disinfection.
CN201621357760.9U 2016-12-12 2016-12-12 A kind of high ammonia nitrogen micro-polluted raw processing system of high algae Expired - Fee Related CN206359390U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621357760.9U CN206359390U (en) 2016-12-12 2016-12-12 A kind of high ammonia nitrogen micro-polluted raw processing system of high algae

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201621357760.9U CN206359390U (en) 2016-12-12 2016-12-12 A kind of high ammonia nitrogen micro-polluted raw processing system of high algae

Publications (1)

Publication Number Publication Date
CN206359390U true CN206359390U (en) 2017-07-28

Family

ID=59374600

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201621357760.9U Expired - Fee Related CN206359390U (en) 2016-12-12 2016-12-12 A kind of high ammonia nitrogen micro-polluted raw processing system of high algae

Country Status (1)

Country Link
CN (1) CN206359390U (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107055931A (en) * 2016-12-12 2017-08-18 无锡市拜沃特环保科技有限公司 A kind of high ammonia nitrogen micro-polluted raw processing system of high algae
CN108031470A (en) * 2017-12-18 2018-05-15 广州增晔科技有限公司 A kind of method for removing removing heavy metals and harmful chemical in water
CN108569822A (en) * 2018-03-30 2018-09-25 叶柳竹 A kind of algae and water pollution purifying treatment method
CN111039461A (en) * 2019-12-30 2020-04-21 武汉理工大学 A denitrogenation removes algae repair system for aquaculture water

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107055931A (en) * 2016-12-12 2017-08-18 无锡市拜沃特环保科技有限公司 A kind of high ammonia nitrogen micro-polluted raw processing system of high algae
CN108031470A (en) * 2017-12-18 2018-05-15 广州增晔科技有限公司 A kind of method for removing removing heavy metals and harmful chemical in water
CN108569822A (en) * 2018-03-30 2018-09-25 叶柳竹 A kind of algae and water pollution purifying treatment method
CN111039461A (en) * 2019-12-30 2020-04-21 武汉理工大学 A denitrogenation removes algae repair system for aquaculture water

Similar Documents

Publication Publication Date Title
CN206359390U (en) A kind of high ammonia nitrogen micro-polluted raw processing system of high algae
CN106794428A (en) The cleaning method and cleaning device and water treatment system of filter membrane
CN102351380A (en) Method and device for treating caprolactam-containing waste water
CN208814710U (en) Photochemical catalytic oxidation sewage-treatment plant
CN107055931A (en) A kind of high ammonia nitrogen micro-polluted raw processing system of high algae
CN105481154A (en) Ultrafiltration membrane reclaimed water treatment device integrating catalytic oxidation and supported catalyst
CN105461045A (en) Ultrafiltration membrane assembly integrating catalytic oxidation and carrying catalyst
CN205635209U (en) Laboratory wastewater treatment equipment
CN205603429U (en) Micro -polluted water source water purification system
CN205773629U (en) A kind of high ammonia nitrogen sewage treatment unit
CN201301254Y (en) Buried type oligodynamic sewage treatment device
CN202156978U (en) High salinity effluent treatment plant
CN206457377U (en) A kind of sewage-treatment plant
CN205575873U (en) Sewage treatment device for hospitals
CN204342609U (en) A kind of refractory organic industrial sewage treatment system
CN105850866A (en) Self-cleaning fish tank with external MBR (membrane biological reactor)
CN206255962U (en) One kind strengthens denitrogenation dephosphorizing sewage-treatment plant
CN212924695U (en) Drinking water filtering and purifying equipment
JP2002192184A (en) Powdery activated carbon-adding membrane separation activated sludge method
CN204224384U (en) Integral type high-concentration hardly-degradable organic industrial sewage treatment unit
WO2013172241A1 (en) Water treatment device and method
CN203144235U (en) Integrated automatic treatment equipment of medical wastewater
CN208747895U (en) By sewage treatment at the equipment of earth's surface water quality standard recycle-water
CN203683315U (en) Membrane technology and inclined plate sedimentation integrated medical waste treatment system
CN209259894U (en) Integrated MBR sewage disposal device

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20170728

Termination date: 20201212

CF01 Termination of patent right due to non-payment of annual fee