CN108126370A - A kind of weight liquid separator - Google Patents
A kind of weight liquid separator Download PDFInfo
- Publication number
- CN108126370A CN108126370A CN201611089600.5A CN201611089600A CN108126370A CN 108126370 A CN108126370 A CN 108126370A CN 201611089600 A CN201611089600 A CN 201611089600A CN 108126370 A CN108126370 A CN 108126370A
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- CN
- China
- Prior art keywords
- heavy
- fluid
- collection
- basin
- light liquid
- 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.)
- Pending
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 87
- 239000012530 fluid Substances 0.000 claims abstract description 73
- 238000004891 communication Methods 0.000 claims abstract description 4
- 238000000034 method Methods 0.000 abstract description 7
- 238000004519 manufacturing process Methods 0.000 abstract description 6
- 238000000926 separation method Methods 0.000 abstract description 4
- 230000005611 electricity Effects 0.000 abstract 1
- 239000003921 oil Substances 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 3
- 239000010779 crude oil Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/0208—Separation of non-miscible liquids by sedimentation
- B01D17/0214—Separation of non-miscible liquids by sedimentation with removal of one of the phases
Landscapes
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The invention discloses a kind of weight liquid separator, including shell separator, wherein, the shell separator is equipped with feed pipe, and light liquid and heavy-fluid are housed in the separator；The shell separator is equipped with collection heavy-fluid case；The collection heavy-fluid case is connected with the collection heavy-fluid pipe of heavy-fluid bottom, collection heavy-fluid basin is equipped in the collection heavy-fluid case, the collection heavy-fluid basin top is higher than light liquid and the interface of heavy-fluid；The shell separator is additionally provided with collection light liquid basin, and the height of the collection light liquid basin is higher than the height for collecting heavy-fluid basin；The collection light liquid basin sum aggregate heavy-fluid basin is in communication with the outside by hose.The present invention controls light liquid layer thickness by the difference in height of domination set light liquid basin sum aggregate heavy-fluid basin, and when the difference in height for collecting light liquid basin sum aggregate heavy-fluid basin is constant, the thickness of layer of light liquid does not also change, and the interface of weight liquid is also stablized constant.It is not required to electricity consumption in process of production, separation purpose can be reached, but also can greatly reduce race, the generation for emitting accident by not needing to guard.
Description
Technical field
The present invention relates to a kind of weight liquid separator more particularly to a kind of two kinds of liquid mixtures of suitable different specific weight
Weight liquid separator, belong to liquid separation technology field.
Background technology
The mixed liquor that industrial production is frequently encountered the liquid composition of two kinds of different specific weights needs to carry out safe and reliable point
From at present, the weight liquid separation receiver that every profession and trade uses is mostly overflow type or is to scrape template, that is, when light liquid floats heavy-fluid
Surface when, opening overflow port in certain position makes light liquid overflow automatically, a heavy liquid exit is opened at other one, so as to make two
The liquid of kind different specific weight is received by separation.The equilibrium problem that this design enters there is material liquid and light liquid, heavy-fluid flow out,
The interface that weight liquid is formed is moved up and down with the variation of weight liquid proportion, and then influences the stabilization at interface, makes operation
Process is unstable, and weight goes out the risk that liquid has mixed liquid, causes light liquid is much to put light liquid, heavy-fluid much the phenomenon that putting heavy-fluid, from
Dynamicization control effect is bad, and computerized image is that analog image reliability is bad.
For this reason, it may be necessary to the separator of a kind of light liquid outlet and heavy liquid exit pressure stability, ensures that the interface of weight liquid is grasped
Work is stablized, at present weight liquid separator not yet as discovery.
Invention content
In order to overcome the deficiencies of the prior art, the present invention designs a kind of weight liquid separator, utilizes liquid pressure and height
Relation principle realize weight liquid interface stability, weight liquid interfacial level is by the technique effect of production control, and production process is not
It need to artificially guard, energy conservation and environmental protection.
To achieve the above object, the present invention adopts the following technical scheme that：
A kind of weight liquid separator, including shell separator, wherein：
The shell separator is equipped with feed pipe, and light liquid and heavy-fluid are housed in the separator；
The shell separator is equipped with collection heavy-fluid case, and the collection heavy-fluid case is connected with the collection heavy-fluid pipe of heavy-fluid bottom, described
Collect and collection heavy-fluid basin is equipped in heavy-fluid case, the collection heavy-fluid basin top is higher than light liquid and the interface of heavy-fluid；
The shell separator is additionally provided with collection light liquid basin, and the height of the collection light liquid basin is higher than the height for collecting heavy-fluid basin；
The collection light liquid basin sum aggregate heavy-fluid basin is in communication with the outside by hose.
Preferably, the collection light liquid basin sum aggregate heavy-fluid basin is respectively equipped with adjustable handle, collects light liquid basin sum aggregate for adjusting
The height of heavy-fluid basin.
Preferably, the feed pipe is vertical is equipped with several porous sub-feed tubes, and the feed pipe is mutually connected with porous sub-feed tube
It is logical；
The height of the porous sub-feed tube is higher than the height of collection heavy-fluid pipe.
Preferably, the heavy-fluid pipe that integrates is antipriming pipe.
Relative to the prior art, the beneficial effects of the present invention are：
(1) present invention is different using the density of weight liquid, the artificial difference in height for being provided with collection light liquid basin sum aggregate heavy-fluid basin, from
And determine the thickness of layer of light liquid, when the difference in height for collecting light liquid basin sum aggregate heavy-fluid basin is constant, the thickness of layer of light liquid does not also change,
Also stablize constant in the interface of weight liquid.
(2) do not have to kilowatt-hour in process of production, can reach production purpose, but also meeting without a people to guard
Greatly reduce race, the generation for emitting accident.
Description of the drawings
Fig. 1 is the structure sectional view of the present invention.
Fig. 2 is the dimensional structure diagram of the present invention.
Reference sign：1- shell separators, 2- collection heavy-fluid casees, 3- collection heavy-fluid basins, 4- collection light liquid basins, 5- hoses, 6-
Hard tube, the porous collection heavy-fluid pipes of 7-, 8- feed pipes, the porous sub-feed tubes of 9-, 10- adjustable handles, 11- heavy-fluid layers, 12- layers of light liquid.
Specific embodiment
In conjunction with embodiment and Fig. 1, Fig. 2, the present invention is described in more detail, and Fig. 1 is the structure section view of the present invention
Figure, Fig. 2 are the dimensional structure diagram of the present invention.It should be appreciated that the present embodiment is merely to illustrate the present invention rather than limits
Protection scope of the present invention.
A kind of 1 weight liquid separator of embodiment
A kind of weight liquid separator as shown in Figure 1, including 1- shell separators, 2- collection heavy-fluid casees, 3- collection heavy-fluid basins,
4- collection light liquid basins, 5- hoses, 6- hard tubes, the porous collection heavy-fluid pipes of 7-, 8- feed pipes, the porous sub-feed tubes of 9-, 10- adjustable handles,
11- heavy-fluid layers, 12- layers of light liquid.
1- shell separators are equipped with a 2- collection heavy-fluid casees, and 2- collection heavy-fluid casees pass through 6- hard tubes and 1- shell separators bottom
The porous collection heavy-fluid pipe connections of 7-；
1- shell separators are additionally provided with 4- collection light liquid basins, and 3- collection heavy-fluid basins, the 4- collection are equipped in the 2- collection heavy-fluid case
Light liquid basin and 3- collection heavy-fluid basins are in communication with the outside by 5- hoses.
The 4- collection light liquid basin and 3- collection heavy-fluid basins are respectively equipped with 10- adjustable handles, for adjust 4- collection light liquid basins and
The height of 3- collection heavy-fluid basins.
The 1- shell separators are additionally provided with 8- feed pipes, and the 8- feed pipes are vertical to be equipped with the porous sub-feed tubes of several 9-,
The 8- feed pipes and the porous sub-feed tubes of 9- interconnect；
The height of the height of the porous sub-feed tubes of 9- collection heavy-fluid pipe porous higher than 7-.
The operation principle of the present invention is：
When light liquid is oil, and heavy-fluid is water, h is set：The thickness of light liquid, h1：Collect open height on heavy-fluid basin, h2：Collect light liquid
Open height on basin, d：The density of oil, 1：The density of water.
Then according to ρOil×g×h+ρWater× g × (h2-h)=ρWater×g×h1
：D × g × h+g × (h2-h)=g × h1
H=(h1-h2) ÷ (1-d)
Difference in height and the density phase of oil of the thickness of oil reservoir only with collecting light liquid basin sum aggregate heavy-fluid basin it can be seen from formula
It closes.
The application method of 2 weight liquid separator of embodiment
The application method of the present invention：Crude oil is entered by 8- feed pipes in separator, and through the porous sub-feed tube sub-materials of 9-, crude oil is certainly
Dynamic layering, lower section is water layer, and top is oil reservoir, and as 8- feed pipes are constantly fed, the water layer of lower section passes through the porous collection heavy-fluids of 7-
Pipe is collected through 6- hard tubes to 2- collection heavy-fluid casees, then is exported by 3- collection heavy-fluid basins and 5- hoses.Oil reservoir then by 4- collection light liquid basins and
5- hoses export.
Therefore, the present invention is different using the density of weight liquid, the artificial difference in height for being provided with collection light liquid basin sum aggregate heavy-fluid basin,
So as to determine the thickness of layer of light liquid, when the difference in height for collecting light liquid basin sum aggregate heavy-fluid basin is constant, the thickness of layer of light liquid does not also change
Become, the interface of weight liquid is also stablized constant.Do not have to kilowatt-hour in process of production, can reach raw without a people to guard
Purpose is produced, but also race, the generation for emitting accident can be greatly reduced.
The embodiment of the present invention content is disclosed above, however the present embodiment is not limited to the range that the present invention is implemented,
The simple equivalent changes and modifications that claims and description according to the present invention are made, still fall within the technology of the present invention side
In the range of case.
Claims (4)
1. a kind of weight liquid separator, including shell separator, it is characterised in that：
The shell separator is equipped with feed pipe, and light liquid and heavy-fluid are housed in the separator；
The shell separator is equipped with collection heavy-fluid case, and the collection heavy-fluid case is connected with the collection heavy-fluid pipe of heavy-fluid bottom, the collection weight
Collection heavy-fluid basin is equipped in liquid case, the collection heavy-fluid basin top is higher than light liquid and the interface of heavy-fluid；
The shell separator is additionally provided with collection light liquid basin, and the height of the collection light liquid basin is higher than the height for collecting heavy-fluid basin；
The collection light liquid basin sum aggregate heavy-fluid basin is in communication with the outside by hose.
2. weight liquid separator as described in claim 1, which is characterized in that the collection light liquid basin sum aggregate heavy-fluid basin is set respectively
There is adjustable handle, for adjusting the height of collection light liquid basin sum aggregate heavy-fluid basin.
3. weight liquid separator as described in claim 1, which is characterized in that the feed pipe is vertical to be equipped with several porous points
Expects pipe, the feed pipe and porous sub-feed tube interconnect；
The height of the porous sub-feed tube is higher than the height of collection heavy-fluid pipe.
4. weight liquid separator as described in claim 1, which is characterized in that the heavy-fluid pipe that integrates is antipriming pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611089600.5A CN108126370A (en) | 2016-12-01 | 2016-12-01 | A kind of weight liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611089600.5A CN108126370A (en) | 2016-12-01 | 2016-12-01 | A kind of weight liquid separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108126370A true CN108126370A (en) | 2018-06-08 |
Family
ID=62387590
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611089600.5A Pending CN108126370A (en) | 2016-12-01 | 2016-12-01 | A kind of weight liquid separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108126370A (en) |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203999514U (en) * | 2014-07-18 | 2014-12-10 | 徐云飞 | Crude oil water-oil interface electric field dehydration slagging-off compensating groove |
| CN206252887U (en) * | 2016-12-01 | 2017-06-16 | 徐云飞 | A kind of weight liquid separator |
-
2016
- 2016-12-01 CN CN201611089600.5A patent/CN108126370A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203999514U (en) * | 2014-07-18 | 2014-12-10 | 徐云飞 | Crude oil water-oil interface electric field dehydration slagging-off compensating groove |
| CN206252887U (en) * | 2016-12-01 | 2017-06-16 | 徐云飞 | A kind of weight liquid separator |
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