CN206051621U - Organic faciess retracting device in a kind of extraction wastewater - Google Patents
Organic faciess retracting device in a kind of extraction wastewater Download PDFInfo
- Publication number
- CN206051621U CN206051621U CN201620960580.3U CN201620960580U CN206051621U CN 206051621 U CN206051621 U CN 206051621U CN 201620960580 U CN201620960580 U CN 201620960580U CN 206051621 U CN206051621 U CN 206051621U
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- CN
- China
- Prior art keywords
- recovery pond
- organic faciess
- retracting device
- agitator tank
- extraction wastewater
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Abstract
This utility model belongs to abstraction technique field, and in particular to the organic faciess retracting device in a kind of extraction wastewater, including：Agitator tank, is provided with first through hole and the second through hole, and a waste pipe is connected through the first through hole with the agitator tank；Administration assembly, which is passed through second through hole and is connected with the agitator tank, in the agitator tank with anion surfactant；Recovery pond, which is connected with the agitator tank；Organic faciess accumulator tank, which is arranged on the top of the recovery pond.Organic faciess retracting device in a kind of extraction wastewater that this utility model is provided, which can not only fully reclaim the organic faciess in extraction wastewater, and energy consumption is relatively low.
Description
Technical field
This utility model belongs to abstraction technique field, and in particular to the organic faciess retracting device in a kind of extraction wastewater.
Background technology
At present, in known extraction wastewater, organic faciess are reclaimed based on aeration, and extractant is generally organic faciess, its many tool
There is surface activity, surface tension can be reduced, be conducive to the dispersion of air bubble and make bubble stable, and extractant is attached to gas-liquid circle
On face, with bubble floating, it is separated from water.But, the efficiency of bubble trap oil depends on its surface area, and bubble is less, compares table
Area is bigger, and efficiency is higher.
The bubble produced due to, traditional aeration method cannot to superfine little organic faciess particle adhesion completely, and aerating system energy
Consumption is high, therefore the organic faciess in waste liquid fully cannot be reclaimed, inefficient.
In order to solve the above problems, this utility model provides organic faciess retracting device in a kind of extraction wastewater, and which is not only
The organic faciess in extraction wastewater can be fully reclaimed, and energy consumption is relatively low.
Utility model content
A purpose of the present utility model is to solve at least one the problems referred to above or defect, and provides general behind at least one
The advantage of explanation.
This utility model is it is also an object that there is provided organic faciess retracting device in a kind of extraction wastewater, which solve extraction
Take waste water organic faciess reclaim it is insufficient, and high energy consumption problem, improve organic faciess organic efficiency.
This utility model is it is also an object that provide organic faciess retracting device in a kind of extraction wastewater, which adopts wooden
Plain sodium sulfonate, which can not only be such that profit separates well, while being reduced the effect of organic faciess entrainment and anti-emulsion.
In order to realize that, according to these purposes of the present utility model and further advantage, it is useless that this utility model provides a kind of extraction
Organic faciess retracting device in water, including：
Agitator tank, is provided with first through hole and the second through hole, a waste pipe through the first through hole with it is described
Agitator tank is connected；
Administration assembly, which is passed through second through hole and is connected with the agitator tank, adds anion table in the agitator tank
Face activating agent；
Recovery pond, which is connected with the agitator tank；
Organic faciess accumulator tank, which is arranged on the top of the recovery pond.
This utility model extraction wastewater organic faciess retracting device, overcomes traditional aeration method and reclaims extraction wastewater organic faciess not
Fully, and the high deficiency of consuming energy.
Preferably, the administration assembly includes spiral chemicals feeder, motor and dosing bucket, and the motor is added with the spiral
Medicine machine connects, and drives the spiral chemicals feeder, the spiral chemicals feeder to be connected with the dosing bucket, the spiral chemicals feeder and institute
Motor is stated positioned at the outside top of the agitator tank, the dosing bucket is located at the top of the spiral chemicals feeder.
Automatic Dosing, compares manual dosing, makes chemical feeding quantity more accurate, greatlys save chemical feeding quantity, improves whole device
Organic efficiency.
Preferably, the recovery pond is level Four recovery pond, including one-level recovery pond, secondary recovery pond, three-level recovery pond
And level Four recovery pond, the one-level recovery pond connected with the bottom in the secondary recovery pond, the secondary recovery pond and described three
The top connection of level recovery pond, the three-level recovery pond are connected with the bottom of the level Four recovery pond.
The classification of the recovery pond, it is ensured that enough separation times, so as to ensure that the effect of organic faciess recovery.
Preferably, the anion surfactant is sodium lignin sulfonate.
By the lot of experiments of Surfactant, sodium lignin sulfonate is have selected as anion surfactant, its
Organic faciess can not only be made well to separate with water, while being reduced the effect of organic faciess entrainment and anti-emulsion.
Preferably, the organic faciess accumulator tank is arranged on the both sides end face of the recovery pond.
When the organic faciess in the recovery pond overflow the recovery pond, into the organic faciess accumulator tank, reclaimed
Recycle.
Preferably, also including delivery pump, which is located at the centre of the agitator tank and the recovery pond, and the delivery pump leads to
Cross the first pipeline and connect the agitator tank, the delivery pump connects the entrance point of the recovery pond by second pipe.
The use of the delivery pump, is not only connected to the agitator tank and the recovery pond, and accelerates waste water is defeated
It is sent to the speed of the recovery pond.
Preferably, also including the 3rd pipeline and the 4th pipeline, the 3rd pipeline is connected with the port of export of the recovery pond
Connect, the 4th pipeline is connected with one end of the organic faciess accumulator tank.
The waste water for removing organic faciess is exported from the 3rd pipeline, is recycled, and the organic faciess of recovery are by having with described
4th pipeline of machine phase accumulator tank connection flows out, and is recycled accordingly.
Preferably, also including stirring vane, which is arranged in the agitator tank in a rotative pattern.
Extraction wastewater and sodium lignin sulfonate can be sufficiently mixed, form uniform mixture, give full play to lignin
The effect of the surfactant of sodium sulfonate, so that mixture is in the standing in later stage, can make organic faciess and aqueous phase separation.
The beneficial effects of the utility model
1st, organic faciess retracting device in a kind of extraction wastewater that this utility model is provided, which solves extraction wastewater organic faciess
Reclaim it is insufficient, and high energy consumption problem, improve organic faciess organic efficiency.
2nd, organic faciess retracting device in a kind of extraction wastewater that this utility model is provided, which adopts sodium lignin sulfonate, its
Organic faciess and water in extraction wastewater can not only be made to separate well, while reducing the effect of organic faciess entrainment and anti-emulsion.
3rd, organic faciess retracting device in a kind of extraction wastewater that this utility model is provided, which adopts level Four recovery pond, it is ensured that
Extraction wastewater profit separation time, so as to ensure that effect that organic faciess are reclaimed.
4th, organic faciess retracting device in a kind of extraction wastewater that this utility model is provided, which adopts administration assembly, improves
The speed of administration.
5th, organic faciess retracting device in a kind of extraction wastewater that this utility model is provided, which adopts agitator tank, effectively can subtract
The dispersion suspension phenomenon of few organic phase in wastewater microgranule.
Description of the drawings
Fig. 1 is the structural representation of organic faciess retracting device in extraction wastewater described in the utility model.
Specific embodiment
Below in conjunction with the accompanying drawings this utility model is described in further detail, to make those skilled in the art with reference to explanation
Book word can be implemented according to this.
It should be appreciated that it is used herein such as " have ", "comprising" and " including " term be not precluded from one or
The presence or addition of multiple other elements or its combination.
As illustrated, this utility model provides organic faciess retracting device in a kind of extraction wastewater, including：
Agitator tank 1, is provided with first through hole and the second through hole, and a waste pipe 5 passes through the first through hole and institute
State agitator tank 1 to connect；
Administration assembly 2, which is passed through second through hole and is connected with the agitator tank 1, adds anion in the agitator tank 1
Surfactant；
Recovery pond 3, which is connected with the agitator tank 1；
Organic faciess accumulator tank 4, which is arranged on the top of the recovery pond 3.
This utility model extraction wastewater organic faciess retracting device, overcomes traditional aeration method and reclaims extraction wastewater organic faciess not
Fully, and the high deficiency of consuming energy.
Organic faciess are generally anion basic group, and a certain amount of surfactant is added in extraction wastewater, can change useless
The surface activity of water so as to produce repulsion to anion basic group, increases the organic faciess particle buoyancy being scattered in waste water, passes through
Stand, wastewater surface is floated on organic faciess granule and be separated from water.
The waste water of anion surfactant is added to first pass through 1 low rate mixing of the agitator tank, which can effectively reduce waste water
The dispersion suspension phenomenon of middle organic faciess microgranule, the relief waste water and anion surfactant mixture in the recovery pond
Middle standing, organic faciess microgranule can gradually float on wastewater surface and form organic layer, as thickening for organic layer has by described
Machine phase accumulator tank 4 is reclaimed.
On the basis of above-mentioned situation, another embodiment, the administration assembly 2 include spiral chemicals feeder, motor and add
Drug bucket, the motor are connected with the spiral chemicals feeder, drive the spiral chemicals feeder, the spiral chemicals feeder and the dosing
Bucket connection, the spiral chemicals feeder are located at the outside top of the agitator tank 1 with the motor, and the dosing bucket is located at the spiral shell
The top of rotation chemicals feeder.
This utility model adopts Automatic Dosing, compares manual dosing, makes chemical feeding quantity more accurate, greatlys save chemical feeding quantity,
Improve the organic efficiency of whole device.
The shape of the dosing bucket freely can be designed, as long as reach for anion surfactant to add agitator tank i.e.
Can.
On the basis of above-described embodiment, another embodiment, the recovery pond 3 be level Four recovery pond, including one-level return
Receives pond, secondary recovery pond, three-level recovery pond and level Four recovery pond, the one-level recovery pond are connected with the bottom in the secondary recovery pond
Logical, the secondary recovery pond is connected with the top of the three-level recovery pond, the three-level recovery pond and the level Four recovery pond
Bottom connects.
What the recovery pond 3 is specifically divided into, can according to actual organic faciess and the flow velocity of aqueous phase separation time and pipeline,
To determine to deposit the recovery pond of many large volumes, so as to determine what recovery pond the recovery pond 3 is, the adjacent recovery pond 3
Bottom offsets one from another with top and connects so that after the full recovery pond of the anion surfactant and extraction wastewater stream of mixing again
Into adjacent recovery pond flow, continuously from a recovery pond stream to another recovery pond inside so that the anion of mixing
Surfactant and extraction wastewater can have enough time to be stored in the recovery pond, it is ensured that certain separation time, so as to
Reach the optimum efficiency of organic faciess and water phase fractionated.
Certainly, the recovery pond 3 is at least one-level recovery pond, determines that according to practical situation what the recovery pond 3 is
Recovery pond.
On the basis of above-described embodiment, another embodiment, the anion surfactant are sodium lignin sulfonate.
By the lot of experiments of Surfactant, sodium lignin sulfonate is have selected as anion surfactant, its
Organic faciess can not only be made well to separate with water, while being reduced the effect of organic faciess entrainment and anti-emulsion.
Certainly, the anion surfactant can be selected as metal carboxylate, sulfuric ester salt and phosphates, only
It is the best results of the sodium lignin sulfonate that effect is selected not as sodium lignin sulfonate, this utility model.
On the basis of above-described embodiment, another embodiment, the organic faciess accumulator tank 4 are arranged on the recovery pond 3
Both sides end face on.
Composite waste is allowed to stand in the recovery pond 3, organic faciess microgranule can gradually float on wastewater surface and form organic faciess
Layer, with thickening for organic layer, when the organic faciess in the recovery pond 3 overflow the recovery pond, into the organic faciess
Accumulator tank 4, carries out recycling, does not waste, and environmental protection.
The organic faciess accumulator tank 4 is designed simply, while organic faciess recovery is completed, has saved the cost of device.
On the basis of above-described embodiment, another embodiment, also including delivery pump 11, its be located at the agitator tank 1 with
The centre of the recovery pond 3, the delivery pump 11 connect the agitator tank 1 by the first pipeline 8, and the delivery pump 11 is by the
Two pipelines 9 connect the entrance point of the recovery pond 3.
The use of the delivery pump 11, is not only connected to the agitator tank 1 and the recovery pond 3, and accelerates and will give up
The mixture of water and sodium lignin sulfonate is transported to the speed of the recovery pond 3, so as to reduce the time of whole removal process,
Improve efficiency.
On the basis of above-described embodiment, further embodiment, also including the 3rd pipeline 7 and the 4th pipeline 6, the described 3rd
Pipeline 7 is connected with the port of export of the recovery pond 3, and the 4th pipeline 6 is connected with one end of the organic faciess accumulator tank 4.
The waste water for removing organic faciess exports next workshop section from the 3rd pipeline 7, is recycled, rather than merely
Waste of draining；The organic faciess of recovery are flowed out by the 4th pipeline 6 being connected with the organic faciess accumulator tank 4, carry out phase
The recycling answered, use of the present utility model so that environmental protection and energy saving.
On the basis of above-described embodiment, further embodiment, also including stirring vane 10, which is arranged in a rotative pattern
In the agitator tank.
Extraction wastewater and sodium lignin sulfonate can be sufficiently mixed, play the work of the surfactant of sodium lignin sulfonate
With.
The waste water of addition sodium lignin sulfonate first passes through the stirring vane 10 carries out low rate mixing, and which can effectively reduce useless
In water, the dispersion suspension phenomenon of organic faciess microgranule, improves extraction efficiency.
In order to overcome the shortcomings of that traditional aeration method reclaims that extraction wastewater organic faciess are insufficient, and high energy consumption, this utility model
An extraction wastewater organic faciess retracting device is provided, the device can not only fully reclaim the organic faciess in extraction wastewater, and energy consumption
It is relatively low.
Extraction wastewater organic faciess retracting device is mainly made up of agitator tank, level Four recovery pond and medicine system.Dosing system
System is made up of spiral chemicals feeder, motor and dosing bucket, is fixed on agitator tank.Extraction wastewater flows into low rate mixing tank by pipeline
In, while spiral reagent feeder dosing, after stirring being delivered to level Four recovery pond by pump carries out standing recovery, and organic faciess are by reclaiming
Groove is reclaimed, and processed waste water enters next workshop section by recovery pond lower pipeline.
The embodiment that this utility model also has other selective, is just no longer elaborated here.
Although embodiment of the present utility model is disclosed as above, which is not restricted in description and embodiment
Listed utilization, it can be applied to various suitable fields of the present utility model completely, for those skilled in the art,
Other modification is easily achieved, therefore under the general concept limited without departing substantially from claim and equivalency range, this reality
Specific details is not limited to and shown here as the legend with description with new.
Claims (8)
1. organic faciess retracting device in a kind of extraction wastewater, it is characterised in that include：
Agitator tank, is provided with first through hole and the second through hole, and a waste pipe passes through the first through hole and the stirring
Tank is connected；
Administration assembly, which is passed through second through hole and is connected with the agitator tank, adds anionic surface to live in the agitator tank
Property agent；
Recovery pond, which is connected with the agitator tank；
Organic faciess accumulator tank, which is arranged on the top of the recovery pond.
2. organic faciess retracting device in extraction wastewater as claimed in claim 1, it is characterised in that the administration assembly includes spiral shell
Rotation chemicals feeder, motor and dosing bucket, the motor are connected with the spiral chemicals feeder, drive the spiral chemicals feeder, the spiral shell
Rotation chemicals feeder is connected with the dosing bucket, and the spiral chemicals feeder is located at the outside top of the agitator tank, institute with the motor
Dosing bucket is stated positioned at the top of the spiral chemicals feeder.
3. organic faciess retracting device in extraction wastewater as claimed in claim 1, it is characterised in that the recovery pond is that level Four is returned
Receives pond, including one-level recovery pond, secondary recovery pond, three-level recovery pond and level Four recovery pond, the one-level recovery pond and described two
The bottom connection of level recovery pond, the secondary recovery pond connect with the top of the three-level recovery pond, the three-level recovery pond and
The bottom connection of the level Four recovery pond.
4. organic faciess retracting device in extraction wastewater as claimed in claim 1, it is characterised in that the anion surface active
Agent is sodium lignin sulfonate.
5. organic faciess retracting device in extraction wastewater as claimed in claim 1, it is characterised in that the organic faciess accumulator tank sets
Put on the both sides end face of the recovery pond.
6. organic faciess retracting device in the extraction wastewater as described in any one in claim 1 to 5, it is characterised in that also wrap
Delivery pump is included, which is located at the centre of the agitator tank and the recovery pond, and the delivery pump is by stirring described in the connection of the first pipeline
Tank is mixed, the delivery pump connects the entrance point of the recovery pond by second pipe.
7. organic faciess retracting device in extraction wastewater as claimed in claim 6, it is characterised in that also including the 3rd pipeline and
Four pipelines, the 3rd pipeline are connected with the port of export of the recovery pond, the 4th pipeline and the organic faciess accumulator tank
One end connects.
8. organic faciess retracting device in extraction wastewater as claimed in claim 1, it is characterised in that also including stirring vane, its
It is arranged in the agitator tank in a rotative pattern.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620960580.3U CN206051621U (en) | 2016-08-26 | 2016-08-26 | Organic faciess retracting device in a kind of extraction wastewater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620960580.3U CN206051621U (en) | 2016-08-26 | 2016-08-26 | Organic faciess retracting device in a kind of extraction wastewater |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206051621U true CN206051621U (en) | 2017-03-29 |
Family
ID=58382330
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620960580.3U Expired - Fee Related CN206051621U (en) | 2016-08-26 | 2016-08-26 | Organic faciess retracting device in a kind of extraction wastewater |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206051621U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108751472A (en) * | 2018-06-26 | 2018-11-06 | 山东瀚星生物科技股份有限公司 | Chlorophyll waste liquid extraction element again |
| CN108751473A (en) * | 2018-06-26 | 2018-11-06 | 山东瀚星生物科技股份有限公司 | chlorophyll waste liquid recycling device |
| CN108751505A (en) * | 2018-06-26 | 2018-11-06 | 山东瀚星生物科技股份有限公司 | The device of chlorophyll is extracted in waste liquid |
-
2016
- 2016-08-26 CN CN201620960580.3U patent/CN206051621U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108751472A (en) * | 2018-06-26 | 2018-11-06 | 山东瀚星生物科技股份有限公司 | Chlorophyll waste liquid extraction element again |
| CN108751473A (en) * | 2018-06-26 | 2018-11-06 | 山东瀚星生物科技股份有限公司 | chlorophyll waste liquid recycling device |
| CN108751505A (en) * | 2018-06-26 | 2018-11-06 | 山东瀚星生物科技股份有限公司 | The device of chlorophyll is extracted in waste liquid |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170329 Termination date: 20210826 |