CN205796626U - Negative-pressure type oily-water seperating equipment - Google Patents
Negative-pressure type oily-water seperating equipment Download PDFInfo
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- CN205796626U CN205796626U CN201620588634.8U CN201620588634U CN205796626U CN 205796626 U CN205796626 U CN 205796626U CN 201620588634 U CN201620588634 U CN 201620588634U CN 205796626 U CN205796626 U CN 205796626U
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- Prior art keywords
- separating tank
- oil
- negative
- liquid
- water
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Abstract
This utility model is related to a kind of negative-pressure type oily-water seperating equipment, between oil-water mixture accumulator tank and separating tank, pump is set, utilize pump to be pumped by the profit of mixing to separating tank and be vaporific spraying out by the nozzle in separating tank, in separating tank, the region of the vaporific profit of corresponding nozzle sprinkling arranges heat conduction fins group, in the condition of high temperature after the heating of this heat conduction fins group heated source, therefore, vaporific profit is after unrestrained heat conduction fins group, the relatively low liquid of boiling point in gaseous state and will be discharged separating tank by evaporation, after the cooling down of condenser, it is condensed into liquid and concentrates on storage in recovery accumulator tank, and the higher liquid not evaporated of boiling point will send oil-water mixture accumulator tank back in separating tank, proceed oil-water separation program；Accordingly, by the profit sent in separating tank in atomization shape, and low-boiling liquid can be made directly by thermal evaporation for being arranged on the heat conduction fins group heating within separating tank.
Description
Technical field
This utility model is related to a kind of negative-pressure type oily-water seperating equipment, refers in particular to one and oil-water mixture is carried out oil
During water separates, oil-water separation efficiency can be improved, simultaneously and the use of heat energy can be reduced, to reach the effect of carbon reduction
The innovation structure of negative-pressure type oily-water seperating equipment.
Background technology
All can produce discarded fluid in manufacturing industry or daily life, these fluid must be reclaimed, if otherwise straight
Connect and be discharged outside to, not only pollute rivers and creeks, affect the ecological environment in rivers and creeks, also the soil in basin arround rivers and creeks can be caused dirt
Dye, affects aspect the most extensive.
Owing to discarded fluid generally containing moisture, therefore, when carrying out the recycling of discarded fluid, it is necessary to manage by
Moisture removal in discarded fluid, enables oil, water to separate and recover, and the most common oil, water separate mode are to adopt standing to strike off
Or utilize centrifugal force to be separated with moisture by fluid；These two kinds of modes are unsatisfactory in the effect separating oil, water, cause follow-up place
Very big inconvenience in reason.
Then, inventor just develops a kind of oil-water separator, refer to: (profit divides TaiWan, China TW M470692 U
Disembark) new patent case, it is mainly provided with the first pump in reservoir, makes this first pump be connected with separating tank, to utilize the first pump
The oil-water mixture of pending oil-water separation is pumped to separating tank, and between the first pump and separating tank, is provided with the first valve,
This separating tank is provided with heating unit and heats, and is connected with condenser in separating tank upper end, and this condenser connects the most respectively
There are vacuum pump and reservoir；Utilizing this heating unit that separating tank is carried out heating operation, separating tank inside is taken out by vacuum pump simultaneously
Vacuum, to reduce the air pressure within separating tank, makes the boiling temperature reduction of oil, water, now due to oil with evaporation of water temperature not
With, make low-boiling elder generation be evaporated, and pump to condenser cooling, then flow in reservoir store, and stay separating tank
The liquid of middle storage is then exported to another reservoir, reaches the purpose of oil-water separation.
Although, TW M470692 U (oil-water separator) new patent case have can by oil, water separate mechanism, but
In actual use, but because the heating target of its heating unit is to leave the discarded profit in separating tank in, and for guaranteeing boiling
The low liquid of point can be evaporated, and heating unit must remain heated condition and it is necessary to exports a large amount of heat energy, and this situation is not
Only cause the waste of the energy, and the highest to the efficiency of oil-water separation.
The present inventor is i.e. in view of above-mentioned situation, and develops this utility model.
Utility model content
Main purpose of the present utility model, is to provide a kind of negative-pressure type oily-water seperating equipment, and it mainly makes oil mixing with water
Liquid, in carrying out in oil water separation process, can increase oil, the separation efficiency of water, can reduce the usage amount of heat energy, it is to avoid the energy simultaneously
Waste, has the effect of carbon reduction.
Above-mentioned main purpose of the present utility model and effect, be to be reached by following concrete technological means:
A kind of negative-pressure type oily-water seperating equipment, oil-water mixture is stored in oil-water mixture accumulator tank, wherein, by an oil
The outfan of water mixed liquid conveying pipe connects with separating tank and sets, and the upper group of described oil-water mixture conveying pipe sets the first pump and the first valve
Door, described oil-water mixture conveying pipe is connected nozzle after entering in described separating tank, corresponding described nozzle spray in described separating tank
The region spilling Oil Fog water mixed liquid arranges least one set heat conduction fins group, and described heat conduction fins group is provided thermal source by heating source,
The input of described separating tank top linking threeway gaseous state transfer pipeline, two outfans of described threeway gaseous state transfer pipeline are respectively
Connecing and set recovery reservoir and vacuum pump, described vacuum pump extracts the air in described separating tank, makes described separating tank keep negative pressure
State, is additionally provided with the recovered liquid cooling fall of evaporation in described threeway gaseous state transfer pipeline on described threeway gaseous state transfer pipeline
Temperature is the condenser of liquid, stores in the recovered liquid that cooling down is liquid concentrates on described recovery reservoir.
Negative-pressure type oily-water seperating equipment as above, wherein, described heat conduction fins group includes heat pipe and fin, described fin
Sheet is arranged on the surface of described heat pipe and guides heat energy.
Negative-pressure type oily-water seperating equipment as above, wherein, has working fluid in described heat pipe, makes described heating source
For circulating heating assembly.
Negative-pressure type oily-water seperating equipment as above, wherein, described heating source is hot pin or is electric heater.
Negative-pressure type oily-water seperating equipment as above, wherein, on described threeway gaseous state transfer pipeline and between described point
From being provided with the second valve between groove and described condenser.
Negative-pressure type oily-water seperating equipment as above, wherein, described recovery reservoir connects derivation valve.
Negative-pressure type oily-water seperating equipment as above, wherein, described negative-pressure type oily-water seperating equipment also includes a profit
Mixed liquor accumulator tank, is connected between described separating tank with described oil-water mixture accumulator tank and has liquid recovery tube, described liquids recovery
Pipe is provided with the second pump that the withdrawal liquid after separating in described separating tank can be sent back to described oil-water mixture accumulator tank.
A kind of negative-pressure type oily-water seperating equipment that the utility model proposes, is that the upper group of described oil-water mixture conveying pipe sets
First pump and the first valve, in the opening of described first valve, described first pump can be by described oil-water mixture accumulator tank
In oil-water mixture pump to described separating tank, described oil-water mixture conveying pipe is connected spray after entering in described separating tank
Mouth, is vaporific spraying out by described oil-water mixture from described nozzle, and in described separating tank, corresponding described nozzles spray is vaporific
The region of oil-water mixture arranges least one set heat conduction fins group, and described heat conduction fins group is provided thermal source by heating source, described point
From the input of groove top linking threeway gaseous state transfer pipeline, two outfans of described threeway gaseous state transfer pipeline connect respectively and set back
Storing up liquid bath and vacuum pump, described vacuum pump extracts the air in described separating tank, makes described separating tank keep negative pressure state,
Be additionally provided with on described threeway gaseous state transfer pipeline the recovered liquid of the evaporation in described threeway gaseous state transfer pipeline is cooled into
The condenser of liquid, stores in the recovered liquid that cooling down is liquid concentrates on described recovery reservoir；Described separating tank with
Between described oil-water mixture accumulator tank, linking has liquid recovery tube, described liquid recovery tube to be provided with the second pump by separating tank further
Withdrawal liquid after interior separation sends described oil-water mixture accumulator tank back to.
The beneficial effects of the utility model:
Structure of the present utility model, mainly by by the profit sent in separating tank in atomization shape, and for being arranged on
Heat conduction fins group heating within separating tank makes low-boiling liquid directly by thermal evaporation, to shorten liquid evaporation time, improves
Capacity efficiency.
Accompanying drawing explanation
Fig. 1 is the configuration diagram of this utility model negative-pressure type oily-water seperating equipment；
Fig. 2 is the relation schematic diagram between this utility model separating tank and heat conduction fins group；
Fig. 3 is another embodiment configuration diagram of this utility model negative-pressure type oily-water seperating equipment；
Fig. 4 is the another embodiment configuration diagram of this utility model negative-pressure type oily-water seperating equipment.
Drawing reference numeral illustrates:
1 separating tank 11 nozzle
12 threeway gaseous state transfer pipeline 13 condensers
14 liquid recovery tube 15 second pumps
16 second valves 2 reclaim reservoir
21 derive valve 3 heat conduction fins group
31 heat pipe 32 fins
4 heating source 5 vacuum pumps
6 oil-water mixture accumulator tank 61 oil-water mixture conveying pipes
62 first pump 63 first valves
Detailed description of the invention
In order to technical characteristic of the present utility model, purpose and effect are more clearly understood from, detailed in conjunction with accompanying drawing
It is described as follows:
First, refer to shown in Fig. 1, disclose the configuration diagram of negative-pressure type oily-water seperating equipment of the present utility model.
Negative-pressure type oily-water seperating equipment of the present utility model, includes: a separating tank 1, reclaims reservoir 2, at least
Group heat conduction fins group 3, an at least heating source 4, vacuum pump 5；In the preferred embodiment disclosed in this utility model, also enter one
Step includes an oil-water mixture accumulator tank 6；Wherein:
Arranging oil-water mixture conveying pipe 61 between oil-water mixture accumulator tank 6 and separating tank 1, oil-water mixture carries
On pipe 61, group is provided with the first pump 62 and the first valve 63, and when the first valve 63 is opened, profit can be mixed by the first pump 62
After the oil-water mixture closed in liquid conveying pipe 61 is pumped to separating tank 1, and oil-water mixture conveying pipe 61 enters in separating tank 1
Linking nozzle 11, makes oil-water mixture can spray out in vaporific at nozzle 11, and in separating tank 1, corresponding nozzle 11 is sprayed vaporific
The region of oil-water mixture arranges least one set heat conduction fins group 3, and heat conduction fins group 3 is to be provided thermal source, separating tank by heating source 4
1 top linking has the input of threeway gaseous state transfer pipeline 12, and two outfans of threeway gaseous state transfer pipeline 12 connect respectively and set back
Storing up liquid bath 2 and vacuum pump 5, vacuum pump 5 extracts the air in separating tank 1, makes separating tank 1 keep negative pressure state, in three ventilations
The condenser into liquid that cooled by the recovered liquid of evaporation in threeway gaseous state transfer pipeline 12 it is additionally provided with on state transfer pipeline 12
13, store in the recovered liquid that cooling down is liquid concentrates on recovery reservoir 2；In a preferred embodiment of the present utility model
In, it is provided with the second valve 16 on this threeway gaseous state transfer pipeline 12 and between separating tank 1 and condenser 13；Separating tank 1 with
Between oil-water mixture accumulator tank 6, linking has liquid recovery tube 14, liquid recovery tube 14 to be provided with the second pump 15 by separating tank 1 further
Withdrawal liquid after interior separation sends oil-water mixture accumulator tank 6 back to.
In this utility model one preferred embodiment, as in figure 2 it is shown, this heat conduction fins group 3 includes heat pipe 31 and fin 32, fin
Sheet 32 is provided in the surface of heat pipe 31, in order to guide heat energy；Additionally, in this utility model one preferred embodiment, this heat pipe
There is in 31 working fluid, make the working fluid in heating source 4 opposite heat tube 31 heat, when working fluid flow to corresponding separating tank 1
Place and after completing heat exchange with fin 32, working fluid flows back to reheat at heating source 4 again, makes a circulating heating
Assembly；Wherein, this heating source 4 can be hot pin or be electric heater.
In this utility model one preferred embodiment, reclaiming reservoir 2 connection has derivation valve 21, the liquid that can reclaim
Derive from reclaiming in reservoir 2.
In time operating with, lie in the oil-water mixture storing pending oil-water separation in oil-water mixture accumulator tank 6,
Make the first valve 63 open again, followed by the first pump 62, the oil-water mixture in oil-water mixture accumulator tank 6 is mixed by profit
Close liquid conveying pipe 61 enter separating tank 1 through nozzle 11, due to heating source 4 persistently by thermal energy conduction to heat conduction fins group 3, make heat conduction
The temperature of fins group 3 between the boiling point of two kinds of liquid of oil-water mixture, add through nozzle 11 enter separating tank 1 profit mix
Closing liquid and become spray form, therefore, when the oil-water mixture of spray form descends slowly and lightly in heat conduction fins group 3 in the condition of high temperature, boiling point is low
Liquid (oil or water one of them) will add that separating tank 1 is taken out by this vacuum pump 5 because of being formed steam by thermal evaporation
Vacuum action so that steam i.e. can outwards be pumped entrance threeway gaseous state transfer pipeline 12, by the cooling down of condenser 13
After be again condensed into liquid, and be stored in recovery reservoir 2, additionally, because vacuum pump 5 carries out evacuation action to separating tank 1,
Make separating tank 1 is formed negative pressure state, allow the boiling temperature of oil-water mixture reduce, via condenser 13, steam is carried out cold
But so that the liquid (water or oil) that cooling condenses can flow to reclaim in reservoir 2 and store, air then can by vacuum pump 5 to
Outer extraction, is then available for outwards being derived by derivation valve 21 in reclaiming the liquid stored in reservoir 2, reaches the mesh of oil-water separation
, and via the residual mixed liquor after oil-water separation in this separating tank 1, it then can be after closing this second valve 16, via the
Two pumps 15 are delivered in oil-water mixture accumulator tank 6 mix with oil-water mixture, for again carrying out oil-water separation；Or
When liquid recovery tube 14 is not further attached to oil-water mixture accumulator tank 6, it is possible to use this second pump 15 by separating tank 1 in
Remaining liquid after separation is derived and is processed.
It addition, refer to Fig. 3, lie in corresponding nozzle 11 in separating tank 1 and spray the region of Oil Fog water mixed liquid and arrange two
Group heat conduction fins group 3, and make two groups of heat conduction fins group 3 become upper and lower orientation to be correspondingly arranged, so that trickling down to heat conduction fins group 3
Its low-boiling liquid of Oil Fog water mixed liquid by evaporation effect more preferably；Additionally, this heat conduction fins group 3 can also be such as Fig. 4 institute
Show, in one group of horizontal vertical heat conduction fins group 3, be i.e. equipped with other heat conduction fins group 3, the most also can promote vaporific profit and mix
Close its low-boiling liquid of liquid by evaporation efficiency.
Claims (10)
1. a negative-pressure type oily-water seperating equipment, it is characterised in that by outfan and the separating tank of an oil-water mixture conveying pipe
Connecing and set, the upper group of described oil-water mixture conveying pipe sets the first pump and the first valve, and described oil-water mixture conveying pipe enters described
Being connected nozzle after in separating tank, in described separating tank, the region of corresponding described nozzles spray Oil Fog water mixed liquid arranges at least one
Group heat conduction fins group, described heat conduction fins group is provided thermal source, described separating tank top linking threeway gaseous state conveying pipe by heating source
The input on road, two outfans of described threeway gaseous state transfer pipeline connect respectively and set recovery reservoir and vacuum pump, described vacuum
Pumping takes the air in described separating tank, makes described separating tank keep negative pressure state, on described threeway gaseous state transfer pipeline also
It is provided with the condenser into liquid that cooled by the recovered liquid of evaporation in described threeway gaseous state transfer pipeline, is liquid through cooling down
The recovered liquid of state concentrates in described recovery reservoir and stores.
2. negative-pressure type oily-water seperating equipment as claimed in claim 1, it is characterised in that described heat conduction fins group include heat pipe with
Fin, described fin is arranged on the surface of described heat pipe and guides heat energy.
3. negative-pressure type oily-water seperating equipment as claimed in claim 2, it is characterised in that in described heat pipe, there is working fluid,
Making described heating source is circulating heating assembly.
4. negative-pressure type oily-water seperating equipment as claimed in claim 2, it is characterised in that described heating source is hot pin or is electric heating
Device.
5. negative-pressure type oily-water seperating equipment as claimed in claim 4, it is characterised in that on described threeway gaseous state transfer pipeline and
The second valve it is provided with between described separating tank and described condenser.
6. negative-pressure type oily-water seperating equipment as claimed in claim 5, it is characterised in that described recovery reservoir connects derivation
Valve.
7. negative-pressure type oily-water seperating equipment as claimed in claim 6, it is characterised in that described negative-pressure type oily-water seperating equipment is also
Including an oil-water mixture accumulator tank, it is connected between described separating tank with described oil-water mixture accumulator tank and has liquid recovery tube, institute
State liquid recovery tube to be provided with the withdrawal liquid after separating in described separating tank can be sent back to the of described oil-water mixture accumulator tank
Two pumps.
8. negative-pressure type oily-water seperating equipment as claimed in claim 3, it is characterised in that on described threeway gaseous state transfer pipeline and
The second valve it is provided with between described separating tank and described condenser.
9. negative-pressure type oily-water seperating equipment as claimed in claim 8, it is characterised in that described recovery reservoir connects derivation
Valve.
10. negative-pressure type oily-water seperating equipment as claimed in claim 9, it is characterised in that described negative-pressure type oily-water seperating equipment
Also including an oil-water mixture accumulator tank, being connected between described separating tank with described oil-water mixture accumulator tank has liquid recovery tube,
Described liquid recovery tube is provided with can send the withdrawal liquid after separating in described separating tank back to described oil-water mixture accumulator tank
Second pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620588634.8U CN205796626U (en) | 2016-06-16 | 2016-06-16 | Negative-pressure type oily-water seperating equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620588634.8U CN205796626U (en) | 2016-06-16 | 2016-06-16 | Negative-pressure type oily-water seperating equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205796626U true CN205796626U (en) | 2016-12-14 |
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ID=58142246
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620588634.8U Expired - Fee Related CN205796626U (en) | 2016-06-16 | 2016-06-16 | Negative-pressure type oily-water seperating equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205796626U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112709929A (en) * | 2020-12-29 | 2021-04-27 | 辽宁津大肥业有限公司 | Accurate metering device for liquid ammonia pipeline transportation |
-
2016
- 2016-06-16 CN CN201620588634.8U patent/CN205796626U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112709929A (en) * | 2020-12-29 | 2021-04-27 | 辽宁津大肥业有限公司 | Accurate metering device for liquid ammonia pipeline transportation |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| 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: 20161214 Termination date: 20210616 |