CN209292078U - In-situ purification of water body system - Google Patents
In-situ purification of water body system Download PDFInfo
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- CN209292078U CN209292078U CN201822250007.5U CN201822250007U CN209292078U CN 209292078 U CN209292078 U CN 209292078U CN 201822250007 U CN201822250007 U CN 201822250007U CN 209292078 U CN209292078 U CN 209292078U
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- fermentation vat
- water body
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- bacterium bed
- fermentation
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Abstract
The utility model discloses a kind of in-situ purification of water body systems comprising more set in-situ purification of water body devices；Every set in-situ purification of water body device includes bacterium bed culture integration apparatus, acquisition zone, water inlet pipe, outlet pipe and discharge region；The bacterium bed culture integration apparatus is connected by the water inlet pipe with acquisition zone；The bacterium bed culture integration apparatus is connected by the outlet pipe with discharge region；The acquisition zone is set as accommodating the mud mixture of polluted-water to be processed；The bacterium bed culture integration apparatus is set as carrying out integrated treatment to the mud mixture using ferment, to form relief liquor；The discharge region is set as accommodating the relief liquor from the bacterium bed culture integration apparatus.The system of the utility model can be improved water body purification efficiency and be suitable for large-scale polluted-water and administers.
Description
Technical field
The utility model relates to a kind of in-situ purification of water body system more particularly to it is a kind of using ferment carry out water body in-situ it is net
The system of change.
Background technique
Currently, large amount of sewage is discharged into the water bodys such as river, lake, water body is caused seriously to pollute.How these to be polluted
Water body carries out the project that purification is environment protection field urgent need to resolve.
The purification method of polluted-water mainly has physical method, chemical method, biological method and combination treatment method.Physics
Method efficient quick, but processing cost is too high；Chemical method is more mature, but there may be secondary pollutions；Biological method price
It is cheap, environment itself is influenced smaller.In general, biological method has apparent cost and environment-friendly advantage.However, current city
Aqueous bio purification device on field is more rare, main reason is that its treatment effeciency is not high.Therefore, it is highly desirable to develop
A kind of water body purification is more efficient and is suitable for the in-situ purification of water body system that large-scale polluted-water is administered.
Utility model content
The purpose of this utility model is to provide a kind of in-situ purification of water body systems, and treatment effeciency is higher, are suitable for big
The polluted-water of scale is administered.The utility model is it is a further objective that provide above-mentioned in-situ purification of water body system, every set water
Body purified in situ device forms a dirty water decontamination handles microcirculation, is conducive to the process for shortening relief liquor, improves water body purification
Efficiency.The further object of the utility model is to provide above-mentioned in-situ purification of water body system, and ferment may be implemented
It recycles, to reduce operating cost.
The utility model provides a kind of in-situ purification of water body system comprising more set in-situ purification of water body devices；Wherein, often
Covering in-situ purification of water body device includes bacterium bed culture integration apparatus, acquisition zone, water inlet pipe, outlet pipe and discharge region；It is described
Bacterium bed culture integration apparatus is connected by the water inlet pipe with acquisition zone；The bacterium bed culture integration apparatus passes through described
Outlet pipe is connected with discharge region；The acquisition zone is set as accommodating the mud mixture of polluted-water to be processed；The bacterium bed
Culture integration apparatus is set as carrying out integrated treatment to the mud mixture using ferment, to form relief liquor；Institute
Discharge region is stated to be set as accommodating the relief liquor from the bacterium bed culture integration apparatus.In above-mentioned in-situ purification of water body system
In, every set in-situ purification of water body device forms a dirty water decontamination handles microcirculation, thus be conducive to shorten the process of relief liquor,
Improve water body purification efficiency.
The in-situ purification of water body system of the utility model includes more set in-situ purification of water body devices, while to pollution to be processed
Water body carries out purified treatment, thus is suitable for large-scale polluted-water and administers.The ferment of the utility model can use ability
Those of known to domain, which is not described herein again.In every set in-situ purification of water body device, bacterium bed culture integration apparatus, acquisition zone,
Water inlet pipe, outlet pipe and the quantity of discharge region are not particularly limited, and can be one or more；Preferably, their quantity
It is one.Bacterium bed culture integration apparatus can be using those of known in the art, and which is not described herein again.
In the present invention, polluted-water to be processed usually indicates contaminated water body.There is no special for contaminated degree
Other restriction, such as it is unsatisfactory for local environmental requirement.Contaminated water body can refer to " integrated wastewater discharge standard "
(GB8978-1996), but it is not limited to the standard.
According to the system of utility model, it is preferable that the quantity of the in-situ purification of water body device is 2~1000.At certain
In a little embodiments, the quantity of the in-situ purification of water body device is 3~100, preferably 5~60.The utility model is opened
It proposes that in-situ purification of water body device will be covered invasively used in parallel more, not only increases treatment effeciency, it can also be ensured that Ge Gewei
It acts synergistically between the circulatory system, improves clean-up effect.
According to the system of utility model, it is preferable that further include the aerator being arranged in polluted-water to be processed.Aerator
Polluted-water to be processed can be formed into more uniform mud mixture, to mud mixture is introduced into water inlet pipe, just
In subsequent the dirty water decontamination handles.Aerator can be mobile aerator.According to the system of utility model, it is preferable that described
Aerator is selected from plug-flow type aeration machine rotor, floating type aerator or aeration boat.In certain embodiments, the aerator is selected from and pushes away
Streaming aerator or floating type aerator.
According to the system of utility model, it is preferable that the multiple acquisition zone is evenly distributed in polluted-water to be processed.This
The position distribution of multiple acquisition zones of utility model is uniform, is convenient for even operation, is conducive to improve wastewater purification efficiency.Acquisition zone
Water pump can be set, convenient for mud mixture is introduced water inlet pipe.
According to the system of utility model, it is preferable that every set bacterium bed culture integration apparatus include the above fermentation vat of Pyatyi,
Sedimentation basin and relief liquor storage pool；The above fermentation vat of Pyatyi is set as carrying out at fermentation the mud mixture using ferment
Reason, obtains fermentation liquid；Sedimentation basin is set as fermentation liquid carrying out sedimentation separation, obtains relief liquor and sludge, and by sludge reflux
To the above fermentation vat of Pyatyi；Relief liquor storage pool is configured to collect the relief liquor.Above-mentioned bacterium bed culture integration apparatus
It can accelerate fermenting speed, promote beneficial microorganism breeding.Due to a large amount of beneficial microbes of content in sludge, by sludge circulation
Using ferment dosage can be saved, to reduce operating cost.
In the utility model, the length of the above fermentation vat of Pyatyi can be 8~10m, and width can be 1~3.5m, and high
Degree can be 2~3.5m；The length of sedimentation basin and relief liquor storage pool can be 1~1.5m, and width can be 1~
1.5m, and height can be 2~3.5m.The length of the above fermentation vat of Pyatyi is preferably 9~10m, and width is preferably 1.2~
2.5m, and highly preferred is 2.5~2.8m.The length of sedimentation basin and relief liquor storage pool is both preferably 1.1~1.2m, and width is equal
Preferably 1.1~1.2m, and height is both preferably 2.5~2.8m.
According to the system of utility model, it is preferable that the above fermentation vat of Pyatyi is provided with aerator.Above-mentioned aeration
Equipment includes that blower, aeration supervisor and more aeration branch pipes, the one end for being aerated supervisor are connect with blower；In more aeration branch pipes
In, one end of every aeration branch pipe is connected with the side wall of aeration supervisor, and the other end protrudes into the lower part of the above fermentation vat of Pyatyi.
According to the system of utility model, it is preferable that in the above fermentation vat of the Pyatyi, there are 5 between adjacent fermentation vat
The liquid level difference of~30cm.In the above fermentation vat of the Pyatyi, there are liquid level differences between adjacent fermentation vat；Previous fermentation vat produces
Raw fermentation liquid enters next fermentation vat under the effect of gravity.In this way operating cost can be further decreased with energy saving.Phase
The liquid level difference of adjacent fermentation vat is preferably 8~15cm, more preferably 9~12cm.There are suitable liquid level difference between adjacent fermentation vat,
Not only guaranteed sufficiently to ferment, but also saved fermentation time.
According to the system of utility model, it is preferable that in the above fermentation vat of the Pyatyi, pass through pipe between adjacent fermentation vat
Line connection.Water pump, the side that the fermentation liquid that previous fermentation vat generates passes through pumping can be set in pipeline between adjacent fermentation vat
Formula enters next fermentation vat.The transfer efficiency that fermentation liquid can be improved in this way, further increases wastewater purification efficiency.
According to the system of utility model, it is preferable that the above fermentation vat of Pyatyi include sequentially connected first fermentation vat,
Second fermentation vat, third fermentation vat, the 4th fermentation vat, the 5th fermentation vat and the 6th fermentation vat；First fermentation vat is set as adding
Ferment, the second fermentation vat, third fermentation vat, the 4th fermentation vat, the 5th fermentation vat and the 6th fermentation vat are set as not adding ferment.
Sedimentation basin collects the fermentation liquid from the 6th fermentation vat, and sedimentation separation obtains relief liquor and sludge.Sludge is pumped to the first hair
Ferment pond.Relief liquor is sent to relief liquor storage pool, is then disposed to discharge region.In certain embodiments, the first fermentation vat,
Successively there is gradient from high to low and fall in the second fermentation vat, third fermentation vat, the 4th fermentation vat, the 5th fermentation vat and the 6th fermentation vat
Difference；The fermentation liquid that previous fermentation vat generates enters next fermentation vat under the effect of gravity.It in this way can be with energy saving, into one
Step reduces operating cost.In other embodiments, the first fermentation vat, the second fermentation vat, third fermentation vat, the 4th fermentation
It is connected between pond, the 5th fermentation vat and the 6th fermentation vat by pipeline；The fermentation liquid that previous fermentation vat generates passes through pumping
Mode enters next fermentation vat.
The in-situ purification of water body system of the utility model includes more set in-situ purification of water body devices, while to pollution to be processed
Water body carries out purified treatment, is suitable for large-scale polluted-water and administers.According to the preferred technical solution of the utility model, every set
In-situ purification of water body device forms a dirty water decontamination handles microcirculation, is conducive to the process for shortening relief liquor, it is net to improve water body
Change efficiency.According to the preferred technical solution of the utility model, recycling for ferment is may be implemented in in-situ purification of water body system, from
And reduce operating cost.
Detailed description of the invention
Fig. 1 is a kind of structural schematic diagram of in-situ purification of water body system of the utility model.
Fig. 2 is a kind of structural schematic diagram of bacterium bed culture integration apparatus of the utility model.
The first fermentation vat of 1-；The second fermentation vat of 2-；3- third fermentation vat；The 4th fermentation vat of 4-；The 5th fermentation vat of 5-；6-
Six fermentation vats；7- sedimentation basin；8- relief liquor storage pool；9- bacterium bed culture integration apparatus；The acquisition zone 91-；92- water inlet pipe；93-
Outlet pipe；The discharge region 94-；10- the first in-situ purification of water body device；11- the second in-situ purification of water body device；12- third water body
Purified in situ device.
Specific embodiment
The utility model is further described combined with specific embodiments below, but the protection scope of the utility model is simultaneously
It is without being limited thereto.
Embodiment 1
Fig. 1 is a kind of structural schematic diagram of in-situ purification of water body system of the utility model.The in-situ purification of water body system
Including three sets of in-situ purification of water body devices, respectively the first in-situ purification of water body device 10, the second in-situ purification of water body device 11
With third in-situ purification of water body device 12；It further include the plug-flow type aeration machine rotor (not shown) being arranged in polluted-water to be processed.
Every set in-situ purification of water body device include the acquisition zone 91, one of bacterium bed culture integration apparatus 9, one into
92, outlet pipes 93 of water pipe and a discharge region 94.Bacterium bed culture integration apparatus 9 passes through water inlet pipe 92 and 91 phase of acquisition zone
Connection.Bacterium bed culture integration apparatus 9 is also connected by outlet pipe 93 with discharge region 94.
Fig. 2 is a kind of structural schematic diagram of bacterium bed culture integration apparatus of the utility model.Bacterium bed culture integration is set
Standby 9 include sequentially connected first fermentation vat 1, the second fermentation vat 2, third fermentation vat 3, the 4th fermentation vat 4, the 5th fermentation vat 5,
6th fermentation vat 6, sedimentation basin 7 and relief liquor storage pool 8.First fermentation vat 1 adds ferment, and other fermentation vats do not add ferment
Element.It is connected between each fermentation vat by pipeline.The fermentation liquid that previous fermentation vat generates is entered next by way of pumping
A fermentation vat.Sedimentation basin 7 collects the fermentation liquid from the 6th fermentation vat 6, and sedimentation separation obtains relief liquor and sludge.Sludge is pumped
It send to the first fermentation vat 1.Relief liquor is sent to relief liquor storage pool 8, is delivered to discharge region 94 by outlet pipe 93.
Embodiment 2
In addition to arranged below, remaining is same as Example 1: the first fermentation vat 1, the second fermentation vat 2, third fermentation vat 3,
Successively there is liquid level difference in four fermentation vats 4, the 5th fermentation vat 5 and the 6th fermentation vat 6, exist between adjacent fermentation vat from high to low
The liquid level difference of 10cm.
Embodiment 3
Other than plug-flow type aeration machine rotor is replaced with floating type aerator, remaining is same as Example 1.
Embodiment 4
The in-situ purification of water body system includes except six sets of in-situ purification of water body devices, remaining is same as Example 1.
Embodiment 5
The in-situ purification of water body system includes except 100 sets of in-situ purification of water body devices, remaining is same as Example 1.
The utility model is not limited to the above embodiment, without departing substantially from the substantive content of the utility model,
It may occur to persons skilled in the art that any deformation, improvement, replacement each fall within the scope of the utility model.
Claims (10)
1. a kind of in-situ purification of water body system, which is characterized in that including covering in-situ purification of water body device more；
Wherein, every set in-situ purification of water body device include bacterium bed culture integration apparatus, acquisition zone, water inlet pipe, outlet pipe and
Discharge region；The bacterium bed culture integration apparatus is connected by the water inlet pipe with acquisition zone；The bacterium bed culture integration
Equipment is connected by the outlet pipe with discharge region；
The acquisition zone is set as accommodating the mud mixture of polluted-water to be processed；The bacterium bed culture integration apparatus setting
To carry out integrated treatment to the mud mixture using ferment, to form relief liquor；The discharge region is set as accommodating
Relief liquor from the bacterium bed culture integration apparatus.
2. system according to claim 1, which is characterized in that the quantity of the in-situ purification of water body device is 2~1000
It is a.
3. system according to claim 1, which is characterized in that further include the aeration being arranged in polluted-water to be processed
Machine.
4. system according to claim 3, which is characterized in that the aerator is selected from plug-flow type aeration machine rotor, floating type exposes
Mechanism of qi or aeration boat.
5. system according to claim 4, which is characterized in that the multiple acquisition zone is evenly distributed on contaminant water to be processed
In body.
6. described in any item systems according to claim 1~5, which is characterized in that every set bacterium bed culture integration apparatus wraps
Include the above fermentation vat of Pyatyi, sedimentation basin and relief liquor storage pool；
The above fermentation vat of Pyatyi is set as carrying out fermentation process to the mud mixture using ferment, obtains fermentation liquid；
Sedimentation basin is set as fermentation liquid carrying out sedimentation separation, obtains relief liquor and sludge, and will be more than sludge reflux to Pyatyi
Fermentation vat；
Relief liquor storage pool is configured to collect the relief liquor.
7. system according to claim 6, which is characterized in that the above fermentation vat of Pyatyi is provided with aerator.
8. system according to claim 7, which is characterized in that in the above fermentation vat of the Pyatyi, adjacent fermentation vat it
Between there are the liquid level differences of 5~30cm.
9. system according to claim 7, which is characterized in that in the above fermentation vat of the Pyatyi, adjacent fermentation vat it
Between pass through pipeline connect.
10. system according to claim 6, which is characterized in that the above fermentation vat of Pyatyi includes sequentially connected
One fermentation vat, the second fermentation vat, third fermentation vat, the 4th fermentation vat, the 5th fermentation vat and the 6th fermentation vat；First fermentation vat is set
It is set to addition ferment, the second fermentation vat, third fermentation vat, the 4th fermentation vat, the 5th fermentation vat and the 6th fermentation vat are set as not
Add ferment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822250007.5U CN209292078U (en) | 2018-12-29 | 2018-12-29 | In-situ purification of water body system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822250007.5U CN209292078U (en) | 2018-12-29 | 2018-12-29 | In-situ purification of water body system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209292078U true CN209292078U (en) | 2019-08-23 |
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ID=67649635
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201822250007.5U Active CN209292078U (en) | 2018-12-29 | 2018-12-29 | In-situ purification of water body system |
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| Country | Link |
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| CN (1) | CN209292078U (en) |
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2018
- 2018-12-29 CN CN201822250007.5U patent/CN209292078U/en active Active
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