CN108059214A - Algae water boat-carrying processing system - Google Patents

Algae water boat-carrying processing system Download PDF

Info

Publication number
CN108059214A
CN108059214A CN201711306256.5A CN201711306256A CN108059214A CN 108059214 A CN108059214 A CN 108059214A CN 201711306256 A CN201711306256 A CN 201711306256A CN 108059214 A CN108059214 A CN 108059214A
Authority
CN
China
Prior art keywords
water
algae
algae water
ultrafiltration membrane
processing system
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.)
Pending
Application number
CN201711306256.5A
Other languages
Chinese (zh)
Inventor
林超
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.)
Wuxi Lanwan Recycling Technology Co Ltd
Original Assignee
Wuxi Lanwan Recycling 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 Wuxi Lanwan Recycling Technology Co Ltd filed Critical Wuxi Lanwan Recycling Technology Co Ltd
Priority to CN201711306256.5A priority Critical patent/CN108059214A/en
Publication of CN108059214A publication Critical patent/CN108059214A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/444Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B30PRESSES
    • B30BPRESSES IN GENERAL
    • B30B9/00Presses specially adapted for particular purposes
    • B30B9/02Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/007Contaminated open waterways, rivers, lakes or ponds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/008Mobile apparatus and plants, e.g. mounted on a vehicle
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/16Regeneration of sorbents, filters

Landscapes

  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The invention discloses algae water boat-carrying processing system, including:Hull is installed on the in vivo ultrafiltration apparatus algae water concentrating part of ship, squeezer algal gel compression section, and ultrafiltration apparatus algae water concentrating part entrance salvages entrance with cyanobacteria and is connected the concentration of realization algae water, outlet and squeezer algal gel compression section;For boat-carrying processing system, it can be according to the Blue-green Algae Fast Growth degree in polluted-water region, flexibly mobile processing, processing system is integrated with the systems such as film concentration, mechanically decoupled, the cyanobacteria of polluted-water can be efficiently separated, as a result of film pre-concentration technology, processing system separative efficiency is higher than traditional coagulation air-float separation, the separated algal gel moisture content of algae hydraulic pressure crusher, far below centrifugal dehydrator, convenient for subsequent processing, integrated treatment cost is also below conventional treatment systems.

Description

Algae water boat-carrying processing system
Technical field
The present invention relates to waters cyanobacteria process fields, further relate to algae water boat-carrying processing system.
Background technology
As the mankind increasingly increase the utilization activity of environmental resource, rivers and lakes water body be subject to agricultural, industry and The pollution of domestic pollution source, particularly nitrogen and phosphorus pollution, body eutrophication with temperature and the influence of illumination, easily trigger water body The amount reproduction of algae, water quality deterioration, main contamination control index have been more than water environmental function requirement.Algae, especially cyanobacteria Control technology receive a large amount of concerns and research, have the application of algae water boat-carrying treatment technology, but most of technical matters mistakes Journey is complicated, investment is big, and operating cost is high, and application limitation is big.
The content of the invention
Present invention aims at algae water boat-carrying processing system is provided, using chemical reaction cohesion cyanobacteria, with reference to physical squeezing, The separation of algae water is realized, in order to achieve the above object, using following technical scheme:Including:Hull is installed on the in vivo ultrafiltration dress of ship Algae water concentrating part, squeezer algal gel compression section are put, ultrafiltration apparatus algae water concentrating part entrance is salvaged entrance with cyanobacteria and is connected Realize the concentration of algae water, outlet and squeezer algal gel compression section;Wherein, ultrafiltration apparatus algae water concentrating part includes:Algae water is collected Pond, ultrafiltration membrane group, ultra filtration drainage water tank, concentration algae water collecting pit, the water inlet of algae water collecting pit are connected with raw water pump, go out The mouth of a river connects ultrafiltration membrane group by pipeline, and the discharge outlet of ultrafiltration membrane group connects concentration algae water collecting pit, and the concentration algae water collecting pit leads to It crosses overflow pipe and connects algae water collecting pit, realize the cycling of water body;Squeezer algal gel compression section includes:Coagulation stirrer, squeezing Machine, coagulation stirrer entrance, outlet are connected respectively with concentration algae water collecting pit squeezer.
Preferably, circulating pump is equipped at ultrafiltration membrane group both ends, is connected at the both ends of ultrafiltration membrane by pipeline using circulating pump, Form the structure with circulatory function.
Preferably, ultrafiltration membrane group also accessed drainage water tank by pipeline, crossed drainage water tank water outlet by anti- It washes pump and connects ultrafiltration membrane group, for backwashing ultrafiltration film group.
Preferably, ultrafiltration membrane group is connected by air inlet pipe with air compressor machine, there is intake valve in air inlet pipe, and intake valve is opened, high Pressure air enters ultrafiltration membrane group, and air is controlled by film dump valve and passes through discharge duct and discharged.
Preferably, squeezer algal gel compression section has further included dosing unit, and the dosing unit passes through pipeline and coagulation Mixer connects, and flocculant is added in into mixing flocculation tank.
Advantageous effect of the present invention:
The system is boat-carrying processing system, can be according to the Blue-green Algae Fast Growth degree in polluted-water region, flexibly mobile processing, processing The system integration systems such as film concentration, mechanically decoupled can efficiently separate the cyanobacteria of polluted-water, as a result of film pre-concentration skill Art, processing system separative efficiency are higher than traditional coagulation air-float separation, the separated algal gel moisture content of algae hydraulic pressure crusher, far below from Heart dewaterer, convenient for subsequent processing, integrated treatment cost is also below conventional treatment systems.
Description of the drawings
Below with reference to figure, the present invention is described in further detail.The attached drawing for forming the part of the application is used for A further understanding of the present invention is provided, schematic description and description of the invention is not formed for explaining the present invention Inappropriate limitation of the present invention.In the accompanying drawings:
Fig. 1 is the frame diagram of present patent application;
Fig. 2 is block schematic illustration of the present patent application on ultrafiltration apparatus algae water concentrating part;
In figure, 1, hull;2nd, algae water collecting pit;3rd, water pump is produced;4th, ultrafiltration membrane group;5th, algae water collecting pit is concentrated;6th, ultra-filtration filters Water water tank;7th, backwashing pump;8th, circulating pump;9th, coagulation stirrer;10th, squeezer;11st, solar panel;12nd, liquid level gauge; 13rd, solenoid valve;14th, influent turbidity meter;15th, membrane module flow of inlet water transmitter;16th, y-type filter;17th, filter partition hand Dynamic valve;18th, air compressor machine;19th, intake pressure transmitter;20th, intake valve;21st, water producing tank water inlet pneumatic operated valve;22nd, solenoid valve II; 23rd, delivery turbidity meter;24th, backwash water supply pneumatic operated valve;25th, film dump valve.
Specific embodiment
The embodiment of the present invention is described in detail below in conjunction with attached drawing.
As shown in Figure 1, including:Hull is installed on the in vivo ultrafiltration apparatus algae water concentrating part of ship, the compression of squeezer algal gel Part, ultrafiltration apparatus algae water concentrating part entrance salvage entrance with cyanobacteria and are connected the concentration of realization algae water, outlet and squeezer algal gel The separation of algae water is realized in compression section connection.
Shown in Fig. 1, Fig. 2, ultrafiltration apparatus algae water concentrating part is installed on hull tail position, ultrafiltration apparatus algae water concentrating part Dividing includes algae water collecting pit, ultrafiltration membrane group, ultra filtration drainage water tank, concentration algae water collecting pit, the water inlet of algae water collecting pit It is connected with raw water pump, salvaging entrance with algae water by raw water pump is connected, and receives the water body containing frond salvaged, and algae water is received The water outlet of Ji Chi is practiced midwifery water pump by pipeline, is produced the outlet of water pump and is connect ultrafiltration membrane group by pipeline, the algae in algae water collecting pit Water is thrown algae water into ultrafiltration membrane group by producing water pump and is concentrated, and the discharge outlet of ultrafiltration membrane group connects concentration algae water collecting pit, passes through Concentrated water after ultrafiltration membrane concentration is discharged to concentration algae water collecting pit, and the concentration algae water collecting pit connects algae water by overflow pipe and receives Ji Chi realizes the cycling of water body, and the concentration for concentrating the algae water purification in algae water collecting pit only can be higher and higher.
Shown in Fig. 1, Fig. 2, squeezer algal gel compression section is located at hull center section, squeezer algal gel compression unit subpackage It includes:Coagulation stirrer, dosing unit and squeezer, coagulation stirrer is by mixing flocculation tank, screw rod(Band stirring motor), concentration Algae water collecting pit water outlet is connected with coagulation stirrer entrance, is thrown the algae water for concentrating algae water collecting pit by pump by pumping Mixing flocculation tank, dosing unit are connected by pipeline with coagulation stirrer, and flocculant, screw rod are added in into mixing flocculation tank(Band Stirring motor)Mixing part be installed in tank diameter, for the stirring to algae water, into squeezer, squeezing after the stirring of algae water Machine is broadly divided into two parts, enriching section and squeeze section, and the algae water of the agitated reaction of mixing flocculation tank flows into the pre-concentration of squeezer Duan Jinhang is concentrated again, into squeeze section after concentration, is squeezed into algal gel, is realized the separated effect of algae water, pass through dehydration electric motor Mud extraction after dehydration, the mud of exclusion are deposited in algal gel acquisition heap.
Preferably, circulating pump is equipped at ultrafiltration membrane group both ends, is connected at the both ends of ultrafiltration membrane by pipeline using circulating pump, The structure with circulatory function is formed, reducing the impurity in water body using the mobility of water body attaches on film, avoids causing film Blocking, film wire is allowed to freely swing in membrane component, the film wire of ultrafiltration membrane group is single-ended fixed, so circulating pump installation When need it is more solid and be not easy to plug along structure as film wire installation.
Preferably, ultrafiltration membrane group also accessed drainage water tank by pipeline, crossed drainage water tank water outlet by anti- It washes pump and connects ultrafiltration membrane group, for backwashing ultrafiltration film group, ultrafiltration membrane group is rinsed by the pure water body for introducing filtering, this is opened It puts the scouring of structure permit air the solid of retention is released through film wire beam and during air bump rinse operation and carried out by pressure switch The action of flushing is voluntarily automatically controlled, realizes that automatic cleaning avoids the blocking of film, due to such ultrafiltration membrane sole mass preferably not It easily blocks, and per se with the backwashing system and circulator of automation, similar common ultrafiltration membrane is obtained with the problem of blocking long To solve.
Shown in Fig. 2, produce also be disposed on the tube body between water pump and ultrafiltration membrane group membrane module flow of inlet water transmitter, Y-type filter, intake pressure transmitter, y-type filter are provided at least in parallel two, the inlet and outlet of each y-type filter Section is both provided with a filter partition hand-operated valve, forms two groups of parallel pipelines.
Preferably, need to be first aerated when ultrafiltration membrane backwash, ultrafiltration membrane group is connected by air inlet pipe with air compressor machine, into There is intake valve on tracheae, intake valve is opened, and pressure-air enters ultrafiltration membrane group, and air is controlled by film dump valve and passes through exhaust Pipeline discharges.
Preferably, algae water collecting pit, ultra filtration drainage water tank, concentration algae water collecting pit in have liquid level gauge respectively, be used for Its internal liquid height is measured in real time.
Preferably, produce and set a lateral on the pipeline between water pump and membrane module flow of inlet water transmitter, the branched pipe The end in road is influent turbidity meter, there is solenoid valve on the lateral, and solenoid valve is opened, influent turbidity measurement volume production water pump output Water turbidity.
Preferably, it is specifically for exporting water to drainage water tank excessively between ultrafiltration membrane group and mistake drainage water tank Tube body on be provided with water producing tank water inlet pneumatic operated valve, go out water speed for control ultrafiltration membrane group;Pneumatic operated valve intake with crossing drainage Solenoid valve II, the delivery turbidity meter concatenated with solenoid valve II, delivery turbidity when solenoid valve II is opened are additionally provided between water tank Measurement measures water turbidity.
Preferably, backwash water supply pneumatic operated valve is additionally provided between backwashing pump and ultrafiltration membrane group, for controlling backwash water outlet Flow.
Entire production water backwash flow is controlled by plc realizes automation with this, and above-mentioned liquid level gauge, influent turbidity meter go out Water turbidity meter is electrically connected, for receiving the real time information of its feedback;Above-mentioned valve class, pump class also realize between PLC and be electrically connected, Using PLC controls pump, the switch on and off of valve class, automation control is used to implement.
Preferably, present patent application is additionally provided with solar panel on hull, is used to implement the conversion of photoelectricity, especially It is the hull for moving at any time, the powerup issue for solving equipment on hull so that mobile algae water separating system uses It is more convenient.
The foregoing is only a preferred embodiment of the present invention, is not intended to limit the invention;For the skill of this field For art personnel, the invention may be variously modified and varied.Within the spirit and principles of the invention, that is made any repaiies Change, equivalent substitution, improvement etc., should all be included in the protection scope of the present invention.

Claims (5)

1. algae water boat-carrying processing system, it is characterised in that:Including:Hull is installed on the in vivo ultrafiltration apparatus algae water concentrating part of ship Point, squeezer algal gel compression section, ultrafiltration apparatus algae water concentrating part entrance and cyanobacteria salvage entrance be connected realization algae water concentrate, Outlet and squeezer algal gel compression section;Wherein, ultrafiltration apparatus algae water concentrating part includes:Algae water collecting pit, ultrafiltration membrane group surpass Filter drainage water tank, concentration algae water collecting pit, the water inlet of algae water collecting pit is connected with raw water pump, water outlet is connect by pipeline Ultrafiltration membrane group, the discharge outlet of ultrafiltration membrane group connect concentration algae water collecting pit, and the concentration algae water collecting pit connects algae by overflow pipe Water collecting pit realizes the cycling of water body;Squeezer algal gel compression section includes:Coagulation stirrer, squeezer, coagulation stirrer enter Mouth, outlet are connected respectively with concentration algae water collecting pit squeezer.
2. algae water boat-carrying processing system according to claim 1, it is characterised in that:Xun Huan is equipped at ultrafiltration membrane group both ends Pump, is connected at the both ends of ultrafiltration membrane by pipeline using circulating pump, forms the structure with circulatory function.
3. algae water boat-carrying processing system according to claim 1, it is characterised in that:Ultrafiltration membrane group is also accessed by pipeline Drainage water tank is crossed, drainage water tank water outlet is crossed and connects ultrafiltration membrane group by backwashing pump, for backwashing ultrafiltration film group.
4. algae water boat-carrying processing system according to claim 1, it is characterised in that:Ultrafiltration membrane group passes through air inlet pipe and pneumatics Machine connects, and has intake valve in air inlet pipe, and intake valve is opened, and pressure-air enters ultrafiltration membrane group, and air is controlled by film dump valve And pass through discharge duct and discharge.
5. algae water boat-carrying processing system according to claim 1, it is characterised in that:Squeezer algal gel compression section further includes There is dosing unit, the dosing unit is connected by pipeline with coagulation stirrer, and flocculant is added in into mixing flocculation tank.
CN201711306256.5A 2017-12-11 2017-12-11 Algae water boat-carrying processing system Pending CN108059214A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711306256.5A CN108059214A (en) 2017-12-11 2017-12-11 Algae water boat-carrying processing system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711306256.5A CN108059214A (en) 2017-12-11 2017-12-11 Algae water boat-carrying processing system

Publications (1)

Publication Number Publication Date
CN108059214A true CN108059214A (en) 2018-05-22

Family

ID=62136444

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201711306256.5A Pending CN108059214A (en) 2017-12-11 2017-12-11 Algae water boat-carrying processing system

Country Status (1)

Country Link
CN (1) CN108059214A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113684800A (en) * 2020-05-19 2021-11-23 伟泰科技(无锡)有限公司 Concentrated integral type testing arrangement is salvaged to on-board formula blue alga

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN202046952U (en) * 2011-04-08 2011-11-23 中国船舶重工集团公司第七○二研究所 Rapid treatment device for algae-containing sewage
CN202072555U (en) * 2011-05-20 2011-12-14 厦门理工学院 Bent flat membrane (BFM) separating and algae removing system
KR101455025B1 (en) * 2014-02-14 2014-10-27 주식회사 한화건설 a water treatment system effective for treating both high turbity and high algal raw water
CN205275336U (en) * 2015-12-29 2016-06-01 上海华励振环保科技有限公司 Portable recycled water treatment facility
CN208617428U (en) * 2017-12-11 2019-03-19 无锡蓝湾资源再生科技有限公司 Algae water boat-carrying processing system

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN202046952U (en) * 2011-04-08 2011-11-23 中国船舶重工集团公司第七○二研究所 Rapid treatment device for algae-containing sewage
CN202072555U (en) * 2011-05-20 2011-12-14 厦门理工学院 Bent flat membrane (BFM) separating and algae removing system
KR101455025B1 (en) * 2014-02-14 2014-10-27 주식회사 한화건설 a water treatment system effective for treating both high turbity and high algal raw water
CN205275336U (en) * 2015-12-29 2016-06-01 上海华励振环保科技有限公司 Portable recycled water treatment facility
CN208617428U (en) * 2017-12-11 2019-03-19 无锡蓝湾资源再生科技有限公司 Algae water boat-carrying processing system

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
水工业市场杂志: "《‘十一五’水处理关键技术与工程应用 案例大全》", 中国环境科学出版社, pages: 80 - 89 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113684800A (en) * 2020-05-19 2021-11-23 伟泰科技(无锡)有限公司 Concentrated integral type testing arrangement is salvaged to on-board formula blue alga

Similar Documents

Publication Publication Date Title
CN101921050B (en) Device and method for dewatering and drying mud under water
CN104609605B (en) Device and method for realizing printing and dyeing dyed wastewater reuse and dye recovery
CN103693711B (en) Utilize weak acidic ion-exchange fiber process nickeliferous/method of copper-contained electroplating waste water
CN101921008B (en) Water treatment device integrating functions of clarification, air flotation and ultrafiltration
CN109179955A (en) A kind of sludge dewatering treatment system and its processing method
CN208617428U (en) Algae water boat-carrying processing system
CN202046952U (en) Rapid treatment device for algae-containing sewage
CN113003913A (en) Method and equipment for two-stage integrated deep dehydration of municipal sludge
CN204310940U (en) A kind of centrifugal sludge concentrator
CN108059214A (en) Algae water boat-carrying processing system
CN101870639A (en) Method for producing kelp mannitol with low energy consumption
CN203904107U (en) Treatment system for industrial wastewater of water supply plant
CN201125201Y (en) Combined type intermediate water treating eqiupment
CN111875211A (en) Muddy water concentration and separation device and separation method
CN216997800U (en) High-efficiency mechanical clarification solid-liquid separation device integrating coagulation and precipitation
CN215250222U (en) Multistage purification and magnetic separation heavy metal wastewater treatment system
CN215249767U (en) Flocculation inclined tube sedimentation tank
CN201620084U (en) Waste water treating device for trichlorosilane production
CN207760214U (en) Sewage collecting processing unit in a kind of sludge
CN209098430U (en) A kind of pretreatment unit of high calcium desulfurization wastewater
CN102874804B (en) Cleaning method in activated carbon for super capacitors production
CN203545852U (en) Sludge dewatering and drying integrated testing device for dredging of rivers and lakes
CN110467328B (en) Method for conditioning and concentrating sludge by utilizing filter pressing
CN106861257A (en) Continuous raw streaming active sand filtration treatment device and filter method
CN112062238A (en) Comprehensive utilization system for blue algae treatment

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination