CN207659186U - Water body automatic aeration system - Google Patents
Water body automatic aeration system Download PDFInfo
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- CN207659186U CN207659186U CN201721596505.4U CN201721596505U CN207659186U CN 207659186 U CN207659186 U CN 207659186U CN 201721596505 U CN201721596505 U CN 201721596505U CN 207659186 U CN207659186 U CN 207659186U
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- module
- dissolved oxygen
- oxygen amount
- control process
- water body
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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Abstract
The utility model, which solves, does not in the prior art quantify water body dissolved oxygen amount, and inaccurate problem is held to aeration time.The utility model provides a kind of water body automatic aeration system, including dissolved oxygen amount acquisition module, and control process module is aerated execution module, data memory module；The dissolved oxygen amount acquisition module is connect with the control process module, and dissolved oxygen amount data are provided to the control process module；The data memory module is connect with the control process module, and dissolved oxygen amount threshold range is provided to the control process module；The control process module is connect with the aeration execution module, is controlled the aeration execution module and is opened or stop.This technology embodiment can change OnNow according to dissolved oxygen amount or stop to be aerated, and not only ensure that water body dissolved oxygen amount was sufficient, but also reduce power wastage；The water body dissolved oxygen amount upper limit can be adjusted in time according to current atmospheric pressure and temperature, it is ensured that each oxygenation of water body is all up the dissolved oxygen amount upper limit.
Description
Technical field
The utility model is related to water body treating fields, and in particular to water body automatic aeration system.
Background technology
Water body dissolved oxygen amount is the important indicator of water ecological setting, and in aquaculture field, improving aquaculture density is
The important method of cultured output is promoted, cultivation density is excessively high to cause water body oxygen demand to increase and then lead to anoxic, water hypoxia
Aquatic organism can be caused slow-growing or even dead, the necessity for increasing that water body dissolved oxygen amount is solution water hypoxia is periodically aerated to water body
Means.In landscape water and river water body, if water body dissolved oxygen amount is too low, the lower animal of aquatic ecosystem and well foster microorganism
Death causes water body organism that can not decompose, and it is smelly that organic matter precipitation excessively causes water body to black, so in landscape water and black smelly
In water body treating, it is also necessary to be periodically aerated increase water body dissolved oxygen amount to water body.
No matter aquaculture system or landscape water water body are aerated at present, are all to be assumed according to artificial supervisor, periodically open
Water body aerator is closed, technological deficiency of the existing technology is as follows：
1, water body dissolved oxygen amount is not quantified, aeration time is held and is not allowed, if aeration time is too short, is caused
Water body dissolved oxygen amount is too low, is unfavorable for aquatic organism growth；If aeration time is long, can not be continued growing after water body dissolved oxygen amount saturation
Dissolved oxygen amount then causes power wastage.
2, atmospheric pressure and temperature are all influential on the water body dissolved oxygen amount upper limit, and atmospheric pressure and temperature are dynamically to become
Change, the water body dissolved oxygen amount upper limit can not be harmonized in time, can not ensure that aeration all reaches the dissolved oxygen amount upper limit and takes into account electric power section every time
About.
Utility model content
The utility model by provide water body automatic aeration system, with solve in the prior art not to water body dissolved oxygen amount into
Row quantization, holds aeration time inaccurate problem.
In order to solve the above technical problems, the utility model is achieved using following technical scheme：
Water body automatic aeration system, including dissolved oxygen amount acquisition module, control process module are aerated execution module, and data are deposited
Store up module；The dissolved oxygen amount acquisition module is connect with the control process module, and dissolved oxygen amount is provided to the control process module
Data；The data memory module is connect with the control process module, and dissolved oxygen amount threshold value is provided to the control process module
Range；The control process module is connect with the aeration execution module, is controlled the aeration execution module and is opened or stop.
Preferably, the water body automatic aeration system further includes air pressure acquisition module, the air pressure acquisition module output end
It is connect with the control process module input, barometric information is sent to the control process module.
Preferably, the water body automatic aeration system further includes temperature acquisition module, the temperature acquisition module output end
It is connect with the control process module input, temperature record is sent to the control process module.
Preferably, the water body automatic aeration system further includes data memory module, is stored in the data memory module
There is air temperature and air pressure/dissolved oxygen amount upper data table.
Preferably, the water body automatic aeration system further includes timing module, the timing module and the control process
Module connects.
Preferably, the aeration execution module is the hydraulic turbine or inflator.
Compared with prior art, technical solution provided by the utility model, the technique effect or advantage having are：
1, water body dissolved oxygen amount can be monitored in real time, can change OnNow according to dissolved oxygen amount or stops to be aerated, and both ensure that water
Body dissolved oxygen amount is sufficient, and reduces power wastage.
2, the water body dissolved oxygen amount upper limit can be adjusted in time according to current atmospheric pressure and temperature, it is ensured that each oxygenation of water body is all
It can reach the dissolved oxygen amount upper limit.
Description of the drawings
Fig. 1 is the system construction drawing of the utility model first embodiment；
Fig. 2 is the system construction drawing of the utility model second embodiment；
Fig. 3 is the utility model air temperature and air pressure/dissolved oxygen amount upper limit table of comparisons.
Specific implementation mode
In order to better understand the above technical scheme, being carried out to above-mentioned technical proposal below in conjunction with Figure of description detailed
Explanation.
Fig. 1 show water body automatic aeration system first embodiment, including dissolved oxygen amount acquisition module 1, control process module
2, it is aerated execution module 3, data memory module 4；The dissolved oxygen amount acquisition module 1 is connect with the control process module 2, to institute
It states control process module 2 and dissolved oxygen amount data is provided；The data memory module 4 is connect with the control process module 2, to described
Control process module 2 provides dissolved oxygen amount threshold range；The control process module 2 is connect with the aeration execution module 3, control
The aeration execution module 3 is opened or is stopped.
In engineer application, the threshold range X ∈ [A of dissolved oxygen amount X are preset in data memory module 4 as needed1,B1],
A1It is dissolved oxygen amount lower limiting value, B1It is dissolved oxygen amount upper limit value, the dissolved oxygen amount acquisition module 1 is contacted with by aeration water body, detects water body
Dissolved oxygen amount data simultaneously feed back to the control process module 2.The control process module 2 is by the water body dissolved oxygen amount detected
Data Y1With the default dissolved oxygen amount threshold range X ∈ [A1,B1] compare, as water body dissolved oxygen amount Y1Less than default dissolved oxygen amount threshold value
Lower limit A1When, unlatching aeration instruction is assigned to the aeration execution module 3, the aeration execution module 3 is started to work, to water body
Aeration, as water body dissolved oxygen amount Y2Reach default dissolved oxygen amount upper threshold B1When, it is sent to the aeration execution module 3 and stops aeration
Instruction, the aeration execution module 3 are stopped；The water body automatic aeration system of the technical program can monitor water body dissolved oxygen in real time
Amount, can adjust aeration schemes immediately according to dissolved oxygen amount, not only ensure that water body dissolved oxygen amount was sufficient, but also reduce power wastage.
Fig. 2 show water body automatic aeration system second embodiment, including dissolved oxygen amount acquisition module 1, control process module
2, it is aerated execution module 3, data memory module 4, air pressure acquisition module 5, temperature acquisition module 6；In the data memory module 4
It is stored with air temperature and air pressure/dissolved oxygen amount upper limit table of comparisons, the control process module 2 further comprises the temperature gas being connected with each other
Pressure/dissolved oxygen amount scaling unit 7 and dissolved oxygen amount control unit 8, the air temperature and air pressure/dissolved oxygen amount scaling unit 7 respectively with the number
It is connected according to memory module 4, air pressure acquisition module 5, temperature acquisition module 6；The dissolved oxygen amount control unit 8 respectively with the dissolved oxygen
Measure acquisition module 1, aeration execution module 3 connects；The aeration execution module 3 is the hydraulic turbine or inflator.
In engineer application, air temperature and air pressure/dissolved oxygen amount upper limit control is preset in data memory module 4 as needed
Table, air temperature and air pressure shown in Fig. 3/dissolved oxygen amount upper limit table of comparisons selected parts part air temperature and air pressure/dissolved oxygen amount upper limit value, these data
It is common sense always, this will not be repeated here；The data memory module 4 is also stored with dissolved oxygen amount threshold range X ∈ [A1,BX], wherein A1
It is the dissolved oxygen amount lower limiting value of setting, BXIt is the dissolved oxygen amount upper limit value under current temperature air pressure, for state to be asked.The temperature gas
The current temperature value C that pressure/dissolved oxygen amount scaling unit 7 is acquired according to temperature acquisition module 6 and air pressure acquisition module 5X, current gas pressure
Value DXAnd air temperature and air pressure/dissolved oxygen amount upper limit table of comparisons acquires the dissolved oxygen amount upper limit value B under current temperature air pressureX=F (CX,DX),
Form current dissolved oxygen amount threshold range X ∈ [A1,BX] and be sent to dissolved oxygen amount control unit 8.The dissolved oxygen amount acquisition module 1 with
It is contacted by aeration water body, detect water body dissolved oxygen amount data and feeds back to the dissolved oxygen amount control unit 8.The dissolved oxygen amount control is single
The water body dissolved oxygen amount data Y that member 8 will detect1With the default dissolved oxygen amount threshold range X ∈ [A1,BX] compare, when water body dissolved oxygen
Measure Y1Less than default dissolved oxygen amount bottom threshold A1When, unlatching aeration instruction is assigned to the aeration execution module 3, the aeration is held
Row module 3 is started to work, and is aerated to water body；As the water body dissolved oxygen amount data Y detected2Reach default dissolved oxygen amount upper threshold BX
When, it is sent to the aeration execution module 3 and stops aeration instruction, the aeration execution module 3 is stopped.The technical program
Water body automatic aeration system can adjust the water body dissolved oxygen amount upper limit in time according to the gentle temperature of current atmospheric pressure, it is ensured that water body is each
Oxygenation can reach maximum dissolved oxygen amount；Water body dissolved oxygen amount can be also monitored in time, can adjust aeration schemes immediately according to dissolved oxygen amount,
Not only it ensure that water body dissolved oxygen amount was sufficient, but also reduced power wastage.
Claims (6)
1. water body automatic aeration system, which is characterized in that including dissolved oxygen amount acquisition module, control process module, aeration executes mould
Block, data memory module；The dissolved oxygen amount acquisition module is connect with the control process module, is carried to the control process module
For dissolved oxygen amount data；The data memory module is connect with the control process module, is provided to the control process module molten
Oxygen amount threshold range；The control process module is connect with the aeration execution module, is controlled the aeration execution module and is opened
Or stop.
2. water body automatic aeration system described in claim 1, which is characterized in that the system also includes air pressure acquisition module, institutes
It states air pressure acquisition module output end to connect with the control process module input, air pressure number is sent to the control process module
According to.
3. water body automatic aeration system described in claim 2, which is characterized in that the system also includes temperature acquisition module, institutes
It states temperature acquisition module output end to connect with the control process module input, temperature number is sent to the control process module
According to.
4. any water body automatic aeration systems of claim 1-3, which is characterized in that the system also includes data to store mould
Block is stored with air temperature and air pressure/dissolved oxygen amount upper data table in the data memory module.
5. water body automatic aeration system described in claim 1, which is characterized in that the system also includes timing module, the meter
When module connect with the control process module.
6. water body automatic aeration system described in claim 1, which is characterized in that the aeration execution module is the hydraulic turbine or inflation
Machine.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721596505.4U CN207659186U (en) | 2017-11-26 | 2017-11-26 | Water body automatic aeration system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721596505.4U CN207659186U (en) | 2017-11-26 | 2017-11-26 | Water body automatic aeration system |
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| Publication Number | Publication Date |
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| CN207659186U true CN207659186U (en) | 2018-07-27 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107720989A (en) * | 2017-11-26 | 2018-02-23 | 碧沃丰工程有限公司 | Water body automatic aeration system |
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2017
- 2017-11-26 CN CN201721596505.4U patent/CN207659186U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107720989A (en) * | 2017-11-26 | 2018-02-23 | 碧沃丰工程有限公司 | Water body automatic aeration system |
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