CN208104087U - The separation of algae water and tail water treatment system - Google Patents
The separation of algae water and tail water treatment system Download PDFInfo
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- CN208104087U CN208104087U CN201820296024.XU CN201820296024U CN208104087U CN 208104087 U CN208104087 U CN 208104087U CN 201820296024 U CN201820296024 U CN 201820296024U CN 208104087 U CN208104087 U CN 208104087U
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Abstract
The utility model provides the separation of algae water and tail water treatment system, including：Algal gel squeezing unit, tail water processing unit, organic fertilizer cache unit and dosing unit, algal gel squeezing unit is connect by pipeline with tail water processing unit, organic fertilizer cache unit, dosing unit is connect by drug feeding pipeline with algal gel squeezing unit, tail water processing unit, organic fertilizer cache unit, for conveying pharmacy response to algal gel squeezing unit, tail water processing unit, organic fertilizer cache unit, the utility model is squeezed algae hydraulic pressure by modularization squeezer, cost is saved, treatment effeciency and ability are improved；The algal gel concentration of squeezing is made into organic fertilizer, rationally utilizes resource, avoids bring a series of problems after concentration landfill；After the tail water of discharge passes through tail water processing unit, water quality reaching standard discharge.
Description
Technical field
The utility model relates to waters algae process fields, further relate to the separation of algae water and tail water treatment system.
Background technique
Nowadays with the attention for increasingly obtaining people of cyanobacteria problem, domestic and foreign scholars have studied a variety of improvement sides at present
Method handles the cyanobacteria of lake surface, including physical method, chemical method and bioanalysis.Chemical method is harmful to aqueous bio, and large area
Implementation acquires a certain degree of difficulty, although bioanalysis effect is also most lasting very well, cost is big, and slow effect, and mechanical removal is a kind of
A kind of physical method for being removed cyanobacteria from lake using mechanical equipment, is generally used for cyanobacteria rich region（As Taihu Lake is flowed
Domain）, using fixed except algae facility or mobile alga removing ship carry out the separation of algae water to the cyanobacteria to salvaging of cyanobacteria rich region.Now such as
The present is taken up a large area based on the treatment process with precipitation-air-flotation mostly, and operating cost is higher, and to subsequent tail water lack into
The treatment measures of one step.
Utility model content
The utility model aim is to provide the separation of algae water and tail water treatment system, realizes that the processing of algae water tail water, realization reach
Mark discharge, in order to achieve the above object, using following technical scheme：Including：It is algal gel squeezing unit, tail water processing unit, organic
Fertile cache unit and dosing unit, algal gel squeezing unit are connect by pipeline with tail water processing unit, organic fertilizer cache unit,
Dosing unit is connect by drug feeding pipeline with algal gel squeezing unit, tail water processing unit, organic fertilizer cache unit, anti-for conveying
Answer medicament to algal gel squeezing unit, tail water processing unit, organic fertilizer cache unit.
Preferably, the dosing unit includes：PAC storage tank 10, MgCl2 storage tank 12, NaOH storage tank 14, NaH2PO4 storage tank
16, PAM storage tank 18, PGa21Ca storage tank 20,2 storage tank 22 of Ca (ClO).
Preferably, the algal gel squeezing unit includes：Algae water buffer pool 1, modularization squeezer 2, algae water buffer pool 1 are used for
Algae water is stored, algae water buffer pool 1 is connect by conveyance conduit with the water inlet of modularization squeezer 2, and modularization squeezer 2 goes out
Mouth is connect with tail water processing unit, organic fertilizer cache unit.
Preferably, organic fertilizer cache unit includes：Organic fertilizer fermentation area 7, organic fertilizer buffer area 8, through modularization squeezer 2
Isolated algal gel is sent directly into organic fertilizer fermentation area 7 by auger conveyor, and organic fertilizer fermentation area 7 and organic fertilizer buffer area 8 are managed
Road connection.
Preferably, the tail water processing unit includes：Tail water buffer pool 3, sedimentation basin I 4, sedimentation basin II 5 and clear water reserviors
6, the water outlet of modularization squeezer 2 is connect by outlet conduit with tail water buffer pool 3, and tail water buffer pool 3 is by pipeline and sinks
Shallow lake pond I 4 connects, and carries out preliminary sedimentation separation, and the sedimentation basin I 4 is connect with II 5 pipeline of sedimentation basin, carries out secondary precipitation separation,
The sedimentation basin II 5 is connect by pipeline with clear water reserviors 6.
Preferably, there are liquidometer, the conveying between algae water buffer pool 1 and modularization squeezer 2 in the algae water buffer pool 1
There are elevator pump and flowmeter on pipeline.
Preferably, the modularization squeezer 2 passes through drug feeding pipeline with PAC storage tank 10, MgCl2 storage tank 12, PAM storage tank 18
Connection.
Preferably, the upper left side of sedimentation basin I 4 is dosing area 9, dosing area 9 and MgCl2 storage tank 12, NaOH storage tank 14,
NaH2PO4 storage tank 16 is connected by drug feeding pipeline, there is screw rod and PH instrument in dosing area 9, and sedimentation basin I 4 passes through top overflow port
It is connect with II 5 pipeline of sedimentation basin, I 4 bottom overflow port of sedimentation basin is connect by pipeline with algae water buffer pool 1.
Preferably, the upper left side of sedimentation basin II 5 is dosing area 9, dosing area 9 and PGa21Ca storage tank 20,2 storage tank of Ca (ClO)
22 are connected by drug feeding pipeline, there is screw rod and PH instrument in dosing area 9, and sedimentation basin II 5 is connect by pipeline with clear water reserviors 6, are precipitated
II 5 bottom overflow port of pond is connect by pipeline with algae water buffer pool 1.
Preferably, the top overflow port connecting pipe of clear water reserviors 6 realizes clear water outlet；The bottom overflow port of clear water reserviors 6 is logical
Piping is connect with algae water buffer pool 1.
The utility model beneficial effect：
The utility model is squeezed algae hydraulic pressure by modularization squeezer, saves cost, improves treatment effeciency and ability；Pressure
The algal gel concentration of squeezing is made into organic fertilizer, rationally utilizes resource, avoids bring a series of problems after concentration landfill；The tail of discharge
After water passes through tail water processing unit, water quality reaching standard discharge.
Detailed description of the invention
Below with reference to figure, the utility model is described in further detail.The attached drawing constituted part of this application
It is used to provide a further understanding of the present invention, the illustrative embodiments and their description of the utility model are for explaining this reality
With novel, do not constitute improper limits to the present invention.In the accompanying drawings：
Fig. 1 is the structural schematic diagram of present patent application.
Specific embodiment
The embodiments of the present invention are described in detail below in conjunction with attached drawing.
As shown in Figure 1, this patent includes：Algal gel squeezing unit, tail water processing unit, organic fertilizer cache unit and dosing
Unit, algal gel squeezing unit are connect by pipeline with tail water processing unit, organic fertilizer cache unit, and dosing unit passes through chemical feed pipe
Road is connect with algal gel squeezing unit, tail water processing unit, organic fertilizer cache unit, squeezes list to algal gel for conveying pharmacy response
Member, tail water processing unit, organic fertilizer cache unit.
The algal gel squeezing unit includes：Algae water buffer pool 1, modularization squeezer 2, algae water buffer pool 1 are for storing algae
Water, algae water buffer pool 1 is connect by conveyance conduit with the water inlet of modularization squeezer 2, for algae water to be delivered to squeezer
Interior progress algae water expression separation generates algal gel and squeezing tail water that moisture content is about 80%, it is slow to have respectively entered organic fertilizer after separation
Rush unit and tail water processing unit.
The organic fertilizer cache unit includes：Organic fertilizer fermentation area 7, organic fertilizer buffer area 8, divide through modularization squeezer 2
From algal gel be sent directly into organic fertilizer fermentation area 7 by auger conveyor, shape after carrying out hot fermentation 30 hours is added after ingredient
At Slow release organic fertilizer, the algal gel after everfermentation deposits in organic fertilizer buffer area 8 and waits outward transport.
Preferably, organic fertilizer fermentation area 7 is fermented using mobile hot fermentation device.
The tail water processing unit includes：Tail water buffer pool 3, sedimentation basin I 4, sedimentation basin II 5 and clear water reserviors 6, module
The water outlet for changing squeezer 2 is connect by outlet conduit with tail water buffer pool 3, the tail water row after the squeezing of modularization squeezer 2
To tail water buffer pool 3, tail water buffer pool 3 is connect by pipeline with sedimentation basin I 4, and dosing carries out tentatively heavy in sedimentation basin I 4
Form sediment separation, the sedimentation basin I 4 connect with II 5 pipeline of sedimentation basin, preliminary sedimentation separate after water body in sedimentation basin II 5 again
Precipitation and separation is carried out, the sedimentation basin II 5 is connect by pipeline with clear water reserviors 6, and water body after precipitation drains into clear water reserviors 6,
It can be discharged outward by clear water reserviors 6.
The dosing unit includes：PAC medicine dissolving tank 9, PAC storage tank 10, MgCl2 medicine dissolving tank 11, MgCl2 storage tank 12, NaOH
Medicine dissolving tank 13, NaOH storage tank 14, NaH2PO4 medicine dissolving tank 15, NaH2PO4 storage tank 16, PAM medicine dissolving tank 17, PAM storage tank 18,
PGa21Ca medicine dissolving tank 19, PGa21Ca storage tank 20,2 medicine dissolving tank 21 of Ca (ClO), 2 storage tank 22 of Ca (ClO), PAC medicine dissolving tank 9 pass through
Pipeline is connect with PAC storage tank 10, and PAC storage tank 10 is connect by pipeline with 2 feeding opening of modularization squeezer；MgCl2 medicine dissolving tank 11
It is connect by pipeline with MgCl2 storage tank 12, MgCl2 storage tank 12 is connected by pipeline and 2 feeding opening of modularization squeezer, sedimentation basin I 4
It connects；NaOH medicine dissolving tank 13 is connect by pipeline with NaOH storage tank 14, and NaOH storage tank 14 is connect by pipeline with sedimentation basin I 4；
NaH2PO4 medicine dissolving tank 15 is connect by pipeline with NaH2PO4 storage tank 16, and NaH2PO4 storage tank 16 is connected by pipeline and sedimentation basin I 4
It connects；PAM medicine dissolving tank 17 is connected by pipeline PAM storage tank 18, and PAM storage tank 18 is connected by pipeline and 2 feeding opening of modularization squeezer
It connects；PGa21Ca medicine dissolving tank 19 is connect by pipeline with PGa21Ca storage tank 20, and PGa21Ca storage tank 20 passes through pipeline and sedimentation basin II
5 connections；2 medicine dissolving tank 21 of Ca (ClO) is connect by pipeline with 2 storage tank 22 of Ca (ClO), and 2 storage tank 22 of Ca (ClO) is by pipeline and sinks
Shallow lake pond II 5 connects.
Preferably, there is liquidometer in algae water buffer pool 1, for height of water level in Real-time Feedback algae water buffer pool 1, algae water is slow
There are elevator pump and flowmeter on the conveyance conduit rushed between pond 1 and modularization squeezer 2, carries out the defeated of algae water using elevator pump
It send, and utilizes the fluid velocity on flowmeter real-time detection conveyance conduit.
Preferably, it is 4 modularization squeezers 2 that the modularization squeezer 2, which is provided with provide at least two, Fig. 1,
The water inlet of all modularization squeezers 2 is connect with algae water buffer pool 1, the water outlet and tail of one of modularization squeezer 2
Water buffer pool 3 connects, and the water outlet of other modularization squeezers 2 is connect with sedimentation basin I 4, as shown in the figure, a modularization squeezing
The water outlet of machine 2 is connect with algae water buffer pool, and excess-three modularization squeezer 2 is connect by pipeline with sedimentation basin I 4.
Preferably, there is liquidometer inside tail water buffer pool 3, for tail water height in Real-time Feedback tail water buffer pool 3, tail water
Elevator pump and flowmeter are provided on pipeline between buffer pool 3 and sedimentation basin I 4, it will be in tail water buffer pool 3 using elevator pump
Tail water mention to sedimentation basin I 4, and tail water flow velocity on pipeline is monitored in real time using flowmeter.
Preferably, the upper left side of sedimentation basin I 4 is dosing area 9, dosing area 9 and MgCl2 storage tank 12, NaOH storage tank 14,
NaH2PO4 storage tank 16 is connected by drug feeding pipeline, is had screw rod and PH instrument in dosing area 9, is stirred using screw rod, is improved anti-
Speed and reaction sufficient degree are answered, and carries out PH inside dosing area using PH instrument and detects；Sedimentation basin I 4 by top overflow port with
The connection of II 5 pipeline of sedimentation basin, I 4 bottom overflow port of sedimentation basin are connect by pipeline with algae water buffer pool 1, sedimentation basin I 4 and algae water
There are multiple elevator pumps in connecting pipe between buffer pool 1.
Preferably, the upper left side of sedimentation basin II 5 is dosing area 9, dosing area 9 and PGa21Ca storage tank 20,2 storage tank of Ca (ClO)
22 are connected by drug feeding pipeline, are had screw rod and PH instrument in dosing area 9, are stirred using screw rod, and reaction speed and anti-is improved
Sufficient degree is answered, and carries out the real-time detection of pH value in dosing area 9 using PH instrument；II 5 top overflow port connecting pipe of sedimentation basin, and
It is connect by pipeline with clear water reserviors 6, II 5 bottom overflow port of sedimentation basin is connect by pipeline with algae water buffer pool 1, sedimentation basin II 5
There are multiple elevator pumps in connecting pipe between algae water buffer pool 1.
Preferably, the top overflow port connecting pipe of clear water reserviors 6 realizes clear water outlet；The bottom overflow port of clear water reserviors 6 is logical
Piping is connect with algae water buffer pool 1, has multiple elevator pumps in the connecting pipe between clear water reserviors 6 and algae water buffer pool 1.
Preferably, it is additionally provided with elevator pump in above-mentioned medicine dissolving tank and storage tank connecting pipe, for by the medicine inside medicine dissolving tank
Agent is evacuated in corresponding storage tank.
Preferably, PAC medicine dissolving tank 9, MgCl2 medicine dissolving tank 11, NaOH medicine dissolving tank 13, NaH2PO4 medicine dissolving tank 15, the molten medicine of PAM
Pond 17, PGa21Ca medicine dissolving tank 19,2 medicine dissolving tank 21 of Ca (ClO) inside have agitating device, be convenient for medicament uniform dissolution, and each
There is tank gage inside a medicine dissolving tank, for monitoring the liquid level inside each medicine dissolving tank in real time.
Preferably, it is additionally provided with elevator pump in above-mentioned medicine dissolving tank and storage tank connecting pipe, for by the medicine inside medicine dissolving tank
Agent is evacuated in corresponding storage tank.
Present patent application is additionally provided with middle control machine, and PLC, input terminal and tank gage, PH tester, the stream of signal can be used
Meter connection, output end is connect with elevator pump, for controlling fluid conveying.
The processing of algal gel squeezing, organic fertilizer caching and tail water is carried out using above system, step is：
S1：Algae water is first pumped into the algae water buffer pool 1 in algae water squeezing unit by storage pool, into modularization squeezer 2
Three sections of dosing reactions are carried out, sequentially adding Mgcl2, PAC, PAM and being stirred makes it sufficiently react direct current after formation flocculation group
Expression separation is carried out into screw rod, algal gel and squeezing tail water that moisture content is about 80% are generated after separation；
S2：Algal gel is sent directly into organic fertilizer fermentation area 7 by auger conveyor, and progress hot fermentation 30 is small after ingredient is added
When after form Slow release organic fertilizer, the algal gel after everfermentation deposit in organic fertilizer buffer area wait outward transport；
S3：Squeezing tail water gravity flow is successively pumped into sedimentation basin I 4 and II 5 two-stage reaction of sedimentation basin after entering tail water buffer pool 3
Device sequentially adds MgCl2, NaH2PO4, NaOH in sedimentation basin I 4, and the PH for controlling reactor enters sedimentation basin I 4 after being 8.5, sinks
The sludge in shallow lake pond I 4 is periodically discharged into squeezer buffer pool 1 and carries out circular treatment；Gravity flow is anti-into second level again for the water outlet of sedimentation basin I 4
Device is answered, Ca (ClO) 2 and PGA is sequentially added, enters the progress secondary precipitation of sedimentation basin II 5, precipitating after being kept for 15 minutes reaction time
II 5 sludge of pond periodically sucks squeezer buffer pool 1 and carries out circular treatment, and the water outlet of sedimentation basin II 5 is discharged into after monitoring system is up to standard
Clear water storage pool 6.
The above descriptions are merely preferred embodiments of the present invention, is not intended to limit the utility model；For this
For the technical staff in field, various modifications and changes may be made to the present invention.It is all in the spirit and principles of the utility model
Within, any modification, equivalent replacement, improvement and so on should be included within the scope of protection of this utility model.
Claims (10)
1. the separation of algae water and tail water treatment system, including：Algal gel squeezing unit, tail water processing unit, organic fertilizer cache unit with
And dosing unit, it is characterised in that：Algal gel squeezing unit is connect by pipeline with tail water processing unit, organic fertilizer cache unit,
Dosing unit is connect by drug feeding pipeline with algal gel squeezing unit, tail water processing unit, organic fertilizer cache unit, anti-for conveying
Answer medicament to algal gel squeezing unit, tail water processing unit, organic fertilizer cache unit.
2. algae water separation according to claim 1 and tail water treatment system, it is characterised in that：The dosing unit includes：
PAC storage tank（10), MgCl2 storage tank (12), NaOH storage tank (14), NaH2PO4 storage tank（16）, PAM storage tank（18）, PGa21Ca storage
Slot（20）, 2 storage tank of Ca (ClO)（22）.
3. algae water separation according to claim 2 and tail water treatment system, it is characterised in that：The algal gel squeezing unit packet
It includes：Algae water buffer pool（1）, modularization squeezer（2）, algae water buffer pool（1）For storing algae water, algae water buffer pool（1）Pass through
Conveyance conduit and modularization squeezer（2）Water inlet connection, modularization squeezer（2）Outlet and tail water processing unit, have
The connection of machine fertilizer cache unit.
4. algae water separation according to claim 3 and tail water treatment system, it is characterised in that：Organic fertilizer cache unit packet
It includes：Organic fertilizer fermentation area（7）, organic fertilizer buffer area（8）, through modularization squeezer（2）Isolated algal gel passes through auger conveyor
It is sent directly into organic fertilizer fermentation area（7）, organic fertilizer fermentation area（7）With organic fertilizer buffer area（8）Pipeline connection.
5. algae water separation according to claim 3 and tail water treatment system, it is characterised in that：The tail water processing unit packet
It includes：Tail water buffer pool（3）, sedimentation basin I（4）, sedimentation basin II（5）And clear water reserviors（6）, modularization squeezer（2）Water outlet
Pass through outlet conduit and tail water buffer pool（3）Connection, tail water buffer pool (3) are connect by pipeline with sedimentation basin I (4), are carried out just
Precipitation and separation is walked, the sedimentation basin I (4) connect with sedimentation basin II (5) pipeline, carries out secondary precipitation separation, the sedimentation basin II
(5）It is connect by pipeline with clear water reserviors (6).
6. algae water separation according to claim 3 and tail water treatment system, it is characterised in that：The algae water buffer pool（1）
Inside there are liquidometer, algae water buffer pool（1）With modularization squeezer（2）Between conveyance conduit on have elevator pump and flowmeter.
7. algae water separation according to claim 3 and tail water treatment system, it is characterised in that：The modularization squeezer
（2）With PAC storage tank（10), MgCl2 storage tank (12), PAM storage tank（18）It is connected by drug feeding pipeline.
8. algae water separation according to claim 5 and tail water treatment system, it is characterised in that：Sedimentation basin I（4）Upper left side
For dosing area（9）, dosing area（9）With MgCl2 storage tank（12）, NaOH storage tank（14）, NaH2PO4 storage tank（16）Pass through drug feeding pipeline
Connection, dosing area（9）Inside there are screw rod and PH instrument, sedimentation basin I（4）Pass through top overflow port and sedimentation basin II（5）Pipeline connection,
Sedimentation basin I（4）Bottom overflow port passes through pipeline and algae water buffer pool（1）Connection.
9. algae water separation according to claim 5 and tail water treatment system, it is characterised in that：The upper left of sedimentation basin II (5)
Side is dosing area (9), dosing area (9) and PGa21Ca storage tank（20）, 2 storage tank of Ca (ClO)（22）It is connected, is added by drug feeding pipeline
There are screw rod and PH instrument in medicine area (9), sedimentation basin II (5) is connect by pipeline with clear water reserviors (6), sedimentation basin II (5）Bottom overflow
Mouth passes through pipeline and algae water buffer pool（1）Connection.
10. algae water separation according to claim 5 and tail water treatment system, it is characterised in that：Clear water reserviors（6）Top overflow
Head piece connecting pipe realizes clear water outlet；Clear water reserviors（6）Bottom overflow port pass through pipeline and algae water buffer pool（1）Connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820296024.XU CN208104087U (en) | 2018-03-04 | 2018-03-04 | The separation of algae water and tail water treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820296024.XU CN208104087U (en) | 2018-03-04 | 2018-03-04 | The separation of algae water and tail water treatment system |
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| Publication Number | Publication Date |
|---|---|
| CN208104087U true CN208104087U (en) | 2018-11-16 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201820296024.XU Active CN208104087U (en) | 2018-03-04 | 2018-03-04 | The separation of algae water and tail water treatment system |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110240378A (en) * | 2018-03-04 | 2019-09-17 | 无锡蓝湾资源再生科技有限公司 | The separation of algae water and tail water treatment system |
| CN112062238A (en) * | 2019-06-11 | 2020-12-11 | 伟泰科技（无锡）有限公司 | Comprehensive utilization system for blue algae treatment |
-
2018
- 2018-03-04 CN CN201820296024.XU patent/CN208104087U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110240378A (en) * | 2018-03-04 | 2019-09-17 | 无锡蓝湾资源再生科技有限公司 | The separation of algae water and tail water treatment system |
| CN112062238A (en) * | 2019-06-11 | 2020-12-11 | 伟泰科技（无锡）有限公司 | Comprehensive utilization system for blue algae treatment |
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