CN102895802A - Cassia oil-water separator - Google Patents
Cassia oil-water separator Download PDFInfo
- Publication number
- CN102895802A CN102895802A CN2012104192529A CN201210419252A CN102895802A CN 102895802 A CN102895802 A CN 102895802A CN 2012104192529 A CN2012104192529 A CN 2012104192529A CN 201210419252 A CN201210419252 A CN 201210419252A CN 102895802 A CN102895802 A CN 102895802A
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- oil
- bay
- filter
- water
- cassia oil
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Abstract
The invention discloses a cassia oil-water separator for the separation of mixed liquor of cassia oil and water. The separator comprises a separation tank. A cassia oil coalescence device is arranged in the separation tank, and is communicated with a cassia oil-water storage tank through a pump pipe. An oil outlet is reserved at the bottom of the separation tank, and a water outlet is reserved on the upper part of the separation tank. The cassia oil coalescence device is a hollow filter element. The middle part of the filter element is a filter cavity communicated with the pump pipe. A filter layer formed by winding a plurality of layers of filter cloth is arranged around the filter cavity. The filter cloth is made from an anticorrosive high polymer material. The filter element is used as the cassia oil coalescence device, the oil and the water can be quickly and completely separated according to the density difference of the water and the cassia oil by using a gravity settling principle, and a separation rate reaches 99 percent.
Description
(1) technical field:
The present invention relates to separator, be specially a kind of to oil of bay water mixed liquid body carry out oil, moisture from the oil of bay separator.
(2) background technology:
At present, a kind of of oil of bay extracting method is the hydrodistillation method, and its technique is simple, no solvent residue, but separation costs is high; The another kind of oil of bay extracting method is to carry out in separator, according to the density contrast of water and oil of bay, utilize sedimentation theory realize oil, moisture from, but because oil of bay water is mixing material, in oil water separator the time of staying too short, cause oil, shipwreck to separate poor effect.
(3) summary of the invention:
For overcoming the deficiency of existing oil of bay water separation technology, the objective of the invention is to propose a kind of oil of bay separator that oil of bay and water are separated fast.
Can realize the oil of bay separator of above-mentioned purpose, comprise knockout drum, the coalescent device of oil of bay is set in the described knockout drum, the coalescent device of described oil of bay is communicated with oil of bay water storage tank by pump line, bottom in knockout drum sets out hydraulic fluid port, sets out the mouth of a river in the top of knockout drum; The coalescent device of described oil of bay is the filter core of hollow, and the mid portion of described filter core is the filter chamber that is communicated with pump line, described filter chamber around for to roll the filter course that forms by multistorey strainer mesh.
The present invention utilizes the affinity coarse separation characteristic of oil of bay and designs the coalescent device of critical component oil of bay, and its operation principle is as follows:
The oil of bay water mixed liquid is pressed into the filter chamber of filter core by the high pressure pump line, and by multilayer filter cloth seepage flow from inside to outside, in this process, oil content is blocked and is adsorbed on the filter cloth, because the affinity that the oil of bay granule has, oil content adsorption-condensation constantly by filter cloth the time becomes the bulky grain oil droplet, at the filter cloth outermost layer, the oil content fusion is the largest particles oil droplet, larger oil droplet sinks under the effect of proportion (the oil of bay relative density is 1.045～1.072), and the moisture content floating, thereby realize the purpose that oil, water separate fast.
For the acid speciality of oil of bay, described filter screen is the anticorrosion filter cloth that macromolecular material is made.
Described filter cloth anticorrosion index is: 90 ° of C of heatproof, acidproof concentration 86%, alkaline-resisting concentration 90%.
The described filter screen number of plies and the inversely proportional relation of filter screen order number, the order number of filter screen is larger, and its number of plies can be relatively less, and the order number of filter screen is less, and its number of plies can be relatively some more.
Advantage of the present invention:
1, oil of bay separator of the present invention with filter core as the coalescent device of oil of bay, according to the density contrast of water and oil of bay, utilize sedimentation theory realize oil, moisture from, reach oil, water thoroughly separates fast, separation rate is up to 99%.
2, present device is applicable to relative density greater than 1.0 oil.
(4) description of drawings:
Fig. 1 is the structural representation of one embodiment of the present invention.
Fig. 2 is the structural representation of filter core in Fig. 1 embodiment.
Figure number sign: 1, knockout drum; 2, pump line; 3, oil of bay water storage tank; 4, oil-out; 5, delivery port; 6, filter core; 7, filter chamber; 8, filter course.
(5) specific embodiment:
Below in conjunction with accompanying drawing technical scheme of the present invention is described further:
Oil of bay separator of the present invention mainly is made of knockout drum 1 and the coalescent device of oil of bay, the conical lower portion of described knockout drum 1 sets out hydraulic fluid port 4, set out the mouth of a river 5 on the top circumference tank skin of knockout drum 1, the coalescent device of described oil of bay is located at knockout drum 1 and is provided with the pipeline of water pump with pump line 2() an end be communicated with, the other end of described pump line 2 is in knockout drum 1 outer connection oil of bay water storage tank 3, as shown in Figure 1.
The coalescent device of described oil of bay is a hollow filter core 6, the mid portion of described filter core 6 is filter chamber 7, rolls into filter course 8 by multistorey strainer mesh around the described filter chamber 7, and described filter chamber 7 is communicated with pump line 2, the described filter screen number of plies and the inversely proportional relation of filter screen order number, as shown in Figure 1.
For adapting to the acid speciality of oil of bay, described filter screen is the anticorrosion filter cloth of making of macromolecular material, and the anticorrosion index of filter cloth is: 90 ° of C of heatproof, acidproof concentration 86%, alkaline-resisting concentration 90%.
The course of work of the present invention:
In the filter chamber 7 of described pump line 2 with the oil-water mixture suction filter core 6 in the oil of bay water storage tank 3, under the pipeline pressure effect, oil-water mixture is by filter course 8 outside seepage flow, and when passing through the filter cloth of different layers respectively, oil content is blocked to be adsorbed in and also forms gradually increasing oil droplet on the filter cloth, in the outermost layer filter cloth, it is maximum that the oil droplet particle reaches, and be deposited on gradually knockout drum 1 bottom downwards, collects by oil-out 4, and moisture content floats over knockout drum 1 top, discharges from delivery port 5.
Claims (4)
1. oil of bay separator, comprise knockout drum (1), it is characterized in that: the coalescent device of oil of bay is set in the described knockout drum (1), the coalescent device of described oil of bay is communicated with oil of bay water storage tank (3) by pump line (2), set out hydraulic fluid port (4) in the bottom of knockout drum (1), set out the mouth of a river (5) in the top of knockout drum (1); The coalescent device of described oil of bay is the filter core (6) of hollow, and the mid portion of described filter core (6) is the filter chamber (7) that is communicated with pump line (2), described filter chamber (7) around for to roll the filter course (8) that forms by multistorey strainer mesh.
2. oil of bay separator according to claim 1 is characterized in that: the anticorrosion filter cloth of described filter screen for making of macromolecular material.
3. oil of bay separator according to claim 2, it is characterized in that: the anticorrosion index of described filter cloth is 90 ° of C of heatproof, acidproof concentration 86%, alkaline-resisting concentration 90%.
4. the described oil of bay separator of any one according to claim 1～3 is characterized in that: the described filter screen number of plies and the inversely proportional relation of filter screen order number.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012104192529A CN102895802A (en) | 2012-10-29 | 2012-10-29 | Cassia oil-water separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012104192529A CN102895802A (en) | 2012-10-29 | 2012-10-29 | Cassia oil-water separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102895802A true CN102895802A (en) | 2013-01-30 |
Family
ID=47568470
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012104192529A Pending CN102895802A (en) | 2012-10-29 | 2012-10-29 | Cassia oil-water separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102895802A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103817967A (en) * | 2014-01-23 | 2014-05-28 | 黄斐 | Liquid food processing device |
| CN106884750A (en) * | 2017-03-28 | 2017-06-23 | 浙江嘉隆机械设备有限公司 | On-line checking autocontrol oil filter |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003126608A (en) * | 2001-10-22 | 2003-05-07 | Hisami Oka | U-shaped continuous oil-water separator |
| CN2832798Y (en) * | 2005-09-13 | 2006-11-01 | 北京石油化工学院 | High-efficiency oil-removing reactor based on novel film materials |
| CN202410406U (en) * | 2011-11-24 | 2012-09-05 | 成都盛尔嘉科技有限公司 | Vinyl monomer gas phase filtering device |
| CN202892976U (en) * | 2012-10-29 | 2013-04-24 | 防城港市防城区那梭香料厂 | Cassia-oil-water separator |
-
2012
- 2012-10-29 CN CN2012104192529A patent/CN102895802A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003126608A (en) * | 2001-10-22 | 2003-05-07 | Hisami Oka | U-shaped continuous oil-water separator |
| CN2832798Y (en) * | 2005-09-13 | 2006-11-01 | 北京石油化工学院 | High-efficiency oil-removing reactor based on novel film materials |
| CN202410406U (en) * | 2011-11-24 | 2012-09-05 | 成都盛尔嘉科技有限公司 | Vinyl monomer gas phase filtering device |
| CN202892976U (en) * | 2012-10-29 | 2013-04-24 | 防城港市防城区那梭香料厂 | Cassia-oil-water separator |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103817967A (en) * | 2014-01-23 | 2014-05-28 | 黄斐 | Liquid food processing device |
| CN103817967B (en) * | 2014-01-23 | 2016-08-17 | 黄斐 | Liquid food processing unit (plant) |
| CN106884750A (en) * | 2017-03-28 | 2017-06-23 | 浙江嘉隆机械设备有限公司 | On-line checking autocontrol oil filter |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20130130 |