CN108059214A - Algae water boat-carrying processing system - Google Patents
Algae water boat-carrying processing system Download PDFInfo
- 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.)
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/02—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/007—Contaminated open waterways, rivers, lakes or ponds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/008—Mobile apparatus and plants, e.g. mounted on a vehicle
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/16—Regeneration 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
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.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201711306256.5A CN108059214A (en) | 2017-12-11 | 2017-12-11 | Algae water boat-carrying processing system |
Applications Claiming Priority (1)
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CN201711306256.5A CN108059214A (en) | 2017-12-11 | 2017-12-11 | Algae water boat-carrying processing system |
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CN108059214A true CN108059214A (en) | 2018-05-22 |
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CN201711306256.5A Pending CN108059214A (en) | 2017-12-11 | 2017-12-11 | Algae water boat-carrying processing system |
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Cited By (1)
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)
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 |
-
2017
- 2017-12-11 CN CN201711306256.5A patent/CN108059214A/en active Pending
Patent Citations (5)
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)
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)
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 |
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