CN106915854A - A kind of water body processing method - Google Patents
A kind of water body processing method Download PDFInfo
- Publication number
- CN106915854A CN106915854A CN201710124854.4A CN201710124854A CN106915854A CN 106915854 A CN106915854 A CN 106915854A CN 201710124854 A CN201710124854 A CN 201710124854A CN 106915854 A CN106915854 A CN 106915854A
- Authority
- CN
- China
- Prior art keywords
- water body
- flocculant
- processing method
- water
- processing unit
- 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
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- 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
- C02F1/34—Treatment of water, waste water, or sewage with mechanical oscillations
- C02F1/36—Treatment of water, waste water, or sewage with mechanical oscillations ultrasonic vibrations
-
- 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
-
- 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
- C02F1/56—Macromolecular compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F7/00—Aeration of stretches of water
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The invention discloses a kind of water body processing method, by each position for swimming in the continuous moving of the processing unit on the water surface to reach waters, purified treatment is carried out come the water body to each position, described purified treatment includes being aerated and added flocculant to the water body of the position.During processing unit continuous moving of the invention, often reach a position just can carry out dosing and Air Exposure to the waters of the position such that it is able to sufficiently uniformly all of water body in processing pond.Present invention can apply to water body process field.
Description
Technical field
The present invention relates to water treatment field, more particularly to a kind of water body processing method.
Background technology
Water process usually stream-handling is carried out in water factory, i.e., by pinpoint dosing, fixed point aeration after by water body from
One pond is extracted into another pond., due to being fixed point dosing, no matter loading position is at which for the processing mode and processing equipment
In the problem that cannot be dispersed evenly in water body of the appearance medicine that is all difficult to avoid that.
Also there are some processing methods, be the floating equipment that a certain position is fixed in water surface placement, floating equipment is built-in to be added
The part of medicine, aeration, inside is pumped into when using by water body, is emitted into the external world after the completion for the treatment of again.These processing methods and treatment
Equipment, can not sufficiently uniformly process all water bodys very much in large pool or large-scale container.
The content of the invention
In order to solve the above problems, it is an object of the invention to provide a kind of water body processing method, can be sufficiently uniformly
Purification, treatment water body.
The technical solution adopted in the present invention is：
A kind of water body processing method, by swim in the continuous moving of the processing unit on the water surface with reach waters each
Put, purified treatment carried out come the water body to each position, described purified treatment include carrying out the water body of the position aeration and
Add flocculant.
As a further improvement on the present invention, the aeration from bottom to top, the dispensing depth of flocculant are carried out to water body
Depth substantially is delivered below water body liquid level but higher than aeration position depth in same depth, or flocculant with aeration position,
Or flocculant is thrown to water body liquid level.
As a further improvement on the present invention, after the water quality of processing unit monitoring water body, by automatically controlling or manually
The mode of control adjusts aeration rate and flocculant dosage.
As a further improvement on the present invention, the process cycle of the water quality situation control process device according to water body.
As a further improvement on the present invention, flocculant is polymeric flocculant, aluminum sulfate, one kind of organic flocculant or many
Kind, the dosage of flocculant is 10-50ppm.
As a further improvement on the present invention, processing unit voluntarily prepares flocculant, and flocculant is thrown into water automatically
Body.
As a further improvement on the present invention, polymeric flocculant is prepared using electrolysis, the polymeric flocculant elder generation after preparation
Buffered is thrown to water body again.
As a further improvement on the present invention, the part in the flocculant after buffered is thrown to water body, another portion
It is electrolysed repeatedly after dividing backflow.
As a further improvement on the present invention, ultrasound wave alga-killing is used during processing unit continuous moving.
As a further improvement on the present invention, processing unit sequentially reaches each water surface site according to the route of planning.
The beneficial effects of the invention are as follows：During processing unit continuous moving of the invention, often a position is reached just
Dosing and Air Exposure can be carried out to the waters of the position such that it is able to sufficiently uniformly all of water body in processing pond.
Brief description of the drawings
The present invention is further described with implementation method below in conjunction with the accompanying drawings.
Fig. 1 is the schematic diagram of water body processing method first embodiment；
Fig. 2 is the schematic diagram of water body processing method embodiment；
Fig. 3 is the schematic diagram of water body processing method embodiment；
Fig. 4 is 3rd embodiment dosing, aeration principle schematic；
Fig. 5 is the schematic diagram of water body processing method fourth embodiment；
Fig. 6 is the schematic diagram of dosing part；
Fig. 7 is the floor plan of dosing part；
Fig. 8 is a kind of mobile route figure of processing unit；
Fig. 9 is processing unit another kind mobile route figure.
Specific embodiment
As shown in figure 8, having processing unit in a clarifier-tank 100, the processing unit includes moveable raft
1, raft 1 is furnished with moving parts, and moving parts can drive the translational motion on the water surface of clarifier-tank 100 of raft 1,
And by modes such as outside wireless telecommunications, raft 1 can reach any one position of the water surface of clarifier-tank 100.
Referring to figs. 1 to Fig. 3, aeration devices 2 and dosing part 3 are additionally provided with described raft 1.Aeration devices 2 to
Include a Fans less, the outlet of blower fan is connected to the pipeline of aeration, and the pipeline of the aeration described in one or more has exposure respectively
Gas is exported, and these pipelines have certain length, can extend the bottom of pond of clarifier-tank 100, are aerated upwards from bottom of pond.Described dosing
Part 3 is mainly used in adding flocculant to clarifier-tank 100.
Above-mentioned its continuous moving of the processing unit swum on the water surface can reach each position in waters, so as to every
The water body of one position carries out purified treatment, and the purified treatment includes the water body of the position is aerated and is used using aeration devices 2
Dosing part 3 adds flocculant.
First embodiment with reference to shown in Fig. 1, medicine outlet 31 and the aeration of dosing part 3 are exported substantially in same depth,
So as to flocculant dispensing depth is roughly the same with aeration position.Directly mix with bubble and rise after flocculant outflow.
Second embodiment with reference to shown in Fig. 2, medicine outlet 31 is substantially in the half position of aeration outlet depth, i.e. flocculant
Depth is delivered below water body liquid level but higher than aeration position depth, the process that the position bubble rises can spread to surrounding, wad a quilt with cotton
Solidifying agent can rise together with the bubble of diffusion, so that the uniformity and adequacy of water body dosing are increased.
3rd embodiment with reference to shown in Fig. 3, more than the liquid level of clarifier-tank 100, flocculant is thrown to water body to medicine outlet 31
Liquid level.Either first embodiment or second embodiment, flocculator drug are directly inside water body, however, in water body
There is certain resistance between portion, due to the presence of resistance after flocculant addition, it is difficult to spread to surrounding in water body, and only
Can rise as bubble rises, then in same vertical position, the flocculant for adding can not sufficiently with the water body on periphery
Reaction, and needing raft to be moved to another location could directly process the water body of the position, undoubtedly be unfavorable for purified treatment
Efficiency.As shown in figure 4, the flocculant dosing of 3rd embodiment is more than liquid level, the bubble produced by aeration rises, while current
It is fully contacted with flocculant after rolling upwards, the flowing shape that the diffusion of current direction surrounding and formation rolled afterwards are stirred up and down
State, flocculant is brought into the water body of bottom, surrounding, so that bottom, the water body of surrounding can contact with flocculant, then flocculant
Can obtain sufficiently being reacted very much with water body, substantially increase the utilization rate of flocculant and the efficiency of water process.This place
The mode of reason is better when the treatment of the water body with algae is carried out.
Hereinafter only it is described further on the basis of 3rd embodiment, meanwhile, following examples can also be applied simultaneously
In the first embodiment and the second embodiment.
With reference to Fig. 4, medicine outlet 31 is provided with and even medicine device (not shown).The even medicine device can be by sprinkling or flow by gravity
Or other modes are to the surrounding drug of medicine outlet 31 so that flocculant is fallen among a region for annular of liquid level, without
Can only be gathered in one with the equal-sized region of medicine outlet 31 in so that flocculant combined with water body it is more abundant.
It is further preferred that referring to figs. 1 to Fig. 3, water quality monitoring module 4 and control module 5 are additionally provided with raft 1,
Water quality monitoring module 4, aeration devices 2, dosing part 3 are connected with the signal of control module 5.Described water quality monitoring module 4 can
To be the instrument and equipment for including COD detectors, Turbidity measurement instrument or other detection water quality, by the way that after the analysis of water quality number will be analyzed
According to control module 5 is uploaded to, data of the control module 5 according to more than carry out aeration devices aeration rate, dosing part flocculant and throw
The control of dosage realizing Automatic Dosing, be aerated and automatically adjust；Certain user can manually be controlled according to the parameter of water quality
System.
Control module 5 can be including host computer etc., and the mode of its control and the connection circuitry of control are abilities
The relatively common control in domain and the mode of connection, therefore embodiment is not described in detail.
In addition, user can be according to the process cycle of the situation control process device of water quality.Such as water body COD satisfactions will
Then stop dosing and aeration when asking, wait certain cycle or wait water body relevant parameter exceeded rear restarting dosing and exposure
Gas.
Can also be the start and stop that processing unit is carried out according to the breeding cycle of water transparency, algae.
Above-described flocculant is polymeric flocculant, aluminum sulfate, one or more of organic flocculant, the throwing of flocculant
Dosage is 10-50ppm.
It is further preferred that dosing part 3 can be made up a prescription and by flocculant by the way of automatic system is with flocculant
It is thrown in water body, and without solid state powder is added by way of dissolving, stirring, it is possible thereby to save substantial amounts of space.
The method for more preferably automatically configuring flocculant is that electrolysis prepares polymeric flocculant, and elder generation is also needed after preparing
Carry out buffered.
Specifically, with reference to Fig. 6 and Fig. 7, dosing part 3 includes the electrolyte chamber 32 and cushion chamber 33 of connection, electrolyte chamber 32
Water inlet 36 is provided with, cushion chamber 33 is provided with flocculant and exports 34 and loop exit 35, and flocculant outlet 34 connects dosing part 3
Medicine outlet 31.Clear water carries out a series of electrochemical reactions and produces flocculant into being electrolysed after electrolyte chamber 32, and flocculant leads to
Cross after cushion chamber 33 and enter flocculant outlet 34 and be thrown to water body liquid level from medicine outlet 31.Above-mentioned loop exit 35 is by pipe
Cycling element connection water inlet 36 on road and pipeline, another part flocculant of cushion chamber 33 is flowed back into by cycling element
Electrolyte chamber 32 carries out electrolysis, activation repeatedly, improves active constituent content.Above-mentioned cycling element can be circulating pump.
It is further preferred that the two ends end of electrolyte chamber 32 is provided with graphite electrode plate 37, electricity is provided between two graphite electrode plates 37
Solution pole plate 38, each electrolytic pole board 38 and graphite electrode plate 37 are parallel to each other.Described electrolytic pole board 38 can be aluminum substrate, thus electricity
The flocculant of solution reaction production is poly-aluminium medicament.
It is further preferred that with reference to Fig. 5, the lower section of raft 1 is additionally provided with the process cartridge 6 of both ends open, the cylinder of process cartridge 6
Ultrasonic Radiation area 61 is formed in chamber.During continuous translation, water body can be flowed into raft 1 from one end of process cartridge 6
And from the other end outflow, this process can also by and impeller (not shown) realize, water body is in Ultrasonic Radiation area 61
When, the algae in water can be by substantial amounts of killing.
For the Ultrasonic Radiation area 61 of generation, process cartridge 6 is provided with ultrasonic activation element 62.
On the basis of above example, moving parts also includes advance unit and steering unit.Advance unit is mainly
Driving raft 1 is moved along a direction, and steering unit is the steering for raft 1, i.e. raft 1
Rotated a certain angle by the track of setting after reaching a certain specified location, then proceed to translation and advance, to reach different positions
Put.
Raft can carry out water process using two kinds of paths as shown in Figure 8 and Figure 9, and both paths can reach
Each position of clarifier-tank.
Embodiment above processes sewage in being used in sewage treatment plant, it is also possible to applies in enclosed waters or opens
The domain that discharges water carries out the treatment of water body.
The above is the preferred embodiment of the present invention, and it does not constitute limiting the scope of the invention.
Claims (10)
1. a kind of water body processing method, it is characterised in that：Reached by swimming in the continuous moving of the processing unit on the water surface
The each position in waters, purified treatment is carried out come the water body to each position, and described purified treatment includes the water to the position
Body is aerated and is added flocculant.
2. water body processing method according to claim 1, it is characterised in that：Exposure from bottom to top is carried out to water body
Gas, the dispensing depth and aeration position of flocculant are substantially in same depth, or flocculant dispensing depth is below water body liquid level
But it is thrown to water body liquid level higher than aeration position depth, or flocculant.
3. water body processing method according to claim 2, it is characterised in that：After the water quality of processing unit monitoring water body, lead to
Cross and automatically control or manually operated mode adjusts aeration rate and flocculant dosage.
4. water body processing method according to claim 3, it is characterised in that：Water quality situation control process dress according to water body
The process cycle put.
5. water body processing method according to claim 1, it is characterised in that：Flocculant is polymeric flocculant, aluminum sulfate, has
One or more of machine flocculant, the dosage of flocculant is 10-50ppm.
6. the water body processing method according to claim 1 or 2 or 3 or 4 or 5, it is characterised in that：Processing unit is voluntarily prepared
Flocculant, and flocculant is thrown to water body automatically.
7. water body processing method according to claim 6, it is characterised in that：Polymeric flocculant is prepared using electrolysis, is made
Polymeric flocculant elder generation buffered after standby is thrown to water body again.
8. water body processing method according to claim 7, it is characterised in that：The part in flocculant after buffered
Water body is thrown to, is electrolysed repeatedly after another part backflow.
9. the water body processing method according to claim 1 or 2 or 3 or 4 or 5, it is characterised in that：Processing unit continuous moving
During use ultrasound wave alga-killing.
10. the water body processing method according to claim 1 or 2 or 3 or 4 or 5, it is characterised in that：Processing unit is according to rule
The route drawn sequentially reaches each water surface site.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710124854.4A CN106915854A (en) | 2017-05-19 | 2017-05-19 | A kind of water body processing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710124854.4A CN106915854A (en) | 2017-05-19 | 2017-05-19 | A kind of water body processing method |
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| Publication Number | Publication Date |
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| CN106915854A true CN106915854A (en) | 2017-07-04 |
Family
ID=59460386
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710124854.4A Pending CN106915854A (en) | 2017-05-19 | 2017-05-19 | A kind of water body processing method |
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| Country | Link |
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| CN (1) | CN106915854A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109384296A (en) * | 2018-12-11 | 2019-02-26 | 大连识汇岛科技服务有限公司 | A kind of swimming pool coagulant delivery device |
| CN110683664A (en) * | 2019-09-26 | 2020-01-14 | 河海大学 | Aeration system for river restoration |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2025011A1 (en) * | 1968-12-02 | 1970-09-04 | Sten Jacquet Ab | |
| CN1210815A (en) * | 1997-08-20 | 1999-03-17 | 马林技研株式会社 | Purifying apparatus for water area |
| JP2932155B2 (en) * | 1995-02-10 | 1999-08-09 | アイサワ工業株式会社 | Water purification method and equipment used for it |
| CN101712497A (en) * | 2009-11-06 | 2010-05-26 | 东南大学 | Ultrasonic algal-removing boat used for water bloom emergency treatment |
| CN203222506U (en) * | 2013-05-10 | 2013-10-02 | 中国水电顾问集团中南勘测设计研究院 | Electrolytic reaction tank and preparing and charging integrated device of polyaluminium flocculating agent |
| CN205933347U (en) * | 2016-08-29 | 2017-02-08 | 广东紫方环保技术有限公司 | Efficient water treatment equipment |
| CN106467330A (en) * | 2016-09-23 | 2017-03-01 | 浙江水利水电学院 | A kind of solar energy water purifying device being applied to lake and its method |
| CN206590997U (en) * | 2017-03-03 | 2017-10-27 | 广州赛特环保工程有限公司 | A kind of sewage disposal system |
-
2017
- 2017-05-19 CN CN201710124854.4A patent/CN106915854A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2025011A1 (en) * | 1968-12-02 | 1970-09-04 | Sten Jacquet Ab | |
| JP2932155B2 (en) * | 1995-02-10 | 1999-08-09 | アイサワ工業株式会社 | Water purification method and equipment used for it |
| CN1210815A (en) * | 1997-08-20 | 1999-03-17 | 马林技研株式会社 | Purifying apparatus for water area |
| CN101712497A (en) * | 2009-11-06 | 2010-05-26 | 东南大学 | Ultrasonic algal-removing boat used for water bloom emergency treatment |
| CN203222506U (en) * | 2013-05-10 | 2013-10-02 | 中国水电顾问集团中南勘测设计研究院 | Electrolytic reaction tank and preparing and charging integrated device of polyaluminium flocculating agent |
| CN205933347U (en) * | 2016-08-29 | 2017-02-08 | 广东紫方环保技术有限公司 | Efficient water treatment equipment |
| CN106467330A (en) * | 2016-09-23 | 2017-03-01 | 浙江水利水电学院 | A kind of solar energy water purifying device being applied to lake and its method |
| CN206590997U (en) * | 2017-03-03 | 2017-10-27 | 广州赛特环保工程有限公司 | A kind of sewage disposal system |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109384296A (en) * | 2018-12-11 | 2019-02-26 | 大连识汇岛科技服务有限公司 | A kind of swimming pool coagulant delivery device |
| CN110683664A (en) * | 2019-09-26 | 2020-01-14 | 河海大学 | Aeration system for river restoration |
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| CB03 | Change of inventor or designer information |
Inventor after: Chen Shuhong Inventor after: Lan Yuandong Inventor after: Cai Baoxiong Inventor after: Ling Qiya Inventor before: Chen Shuhong Inventor before: Lin Rongbin Inventor before: Cai Baoxiong Inventor before: Lian Dongsheng |
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Application publication date: 20170704 |
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