CN208430056U - Light dydrocarbon, nine resinae product separator of carbon - Google Patents
Light dydrocarbon, nine resinae product separator of carbon Download PDFInfo
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- CN208430056U CN208430056U CN201820839608.7U CN201820839608U CN208430056U CN 208430056 U CN208430056 U CN 208430056U CN 201820839608 U CN201820839608 U CN 201820839608U CN 208430056 U CN208430056 U CN 208430056U
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Abstract
The utility model relates to light dydrocarbons, nine resinae product separator of carbon.Including heating concentration tank, compound-split tower, condenser, compound-split tower includes upper tower body, lower tank, upper tower body is respectively equipped with recycle stock distributing disc, upper ceramic filter layer, ceramic tube packing, lower ceramic filter layer from top to bottom, upper ceramic filter layer, the filter screen that lower ceramic filter layer is ceramic material, the air hole of the ceramics tube packing is interior to be equipped with wind-fire wheel type grid.The utility model can be used for dividing the carbon ninety percent in light dydrocarbon, nine resinae product of carbon carry out purification processes, and liquefaction efficiency is high.
Description
Technical field
The utility model relates to organic matter separator technical fields, and in particular to a kind of light dydrocarbon, nine resinae product of carbon
Separator.
Background technique
The raw materials for production of existing nine solvent of carbon can be recycled using light dydrocarbon, the by-product of nine resinae product of carbon,
It can sell again.But light dydrocarbon, nine resinae material of carbon mix, because its purity is low apply it is limited；It recycles and because has
Effect constituent content is few, and compositional purity is low, it is difficult to be separately to nine production of resins field of carbon.
Summary of the invention
Purpose of the utility model is to solve the above problems and provide a kind of light dydrocarbon, nine resinae product separator of carbon,
Its purity that nine product of carbon can be improved.
To solve the above-mentioned problems, the technical solution adopted in the utility model is as follows:
Light dydrocarbon, nine resinae product separator of carbon, including heating concentration tank 1, compound-split tower 2, condenser 3, heating
The exhaust outlet of concentration tank 1 is connect with the gas access of compound-split tower 2, and the liquid outlet and material of 2 bottom of compound-split tower are slow
The connection of 4 entrance of tank is rushed, the outlet of material buffer tank 4 is connect with 3 entrance of condenser, 3 material outlet of condenser and compound-split tower 2
The connection of Matter Transfer entrance；
The heating concentration tank 1 is Double-layer clamp jacketing heat concentration tank, and upper part is equipped with feed inlet and exhaust outlet, and tank bottom is set
There is material outlet mouth；
The thermal medium of the condenser 3 is material；
It is characterized in that, the compound-split tower 2 includes upper tower body 21, lower tank 22, lower tank 22 is tank body, upper tower body
21 be cylindrical body, and 22 lower part of lower tank is equipped with gas access 23, and 22 bottom of lower tank is equipped with liquid material outlet 24, upper tower body 21
It is respectively equipped with recycle stock distributing disc 26, upper ceramic filter layer 25, ceramic tube packing 27, lower ceramic filter layer 28 from top to bottom,
Upper ceramic filter layer 25, the filter screen that lower ceramic filter layer 28 is ceramic material, the ceramics tube packing 27 is by several ceramics
Pipe accumulation filling forms, and air hole 271 is uniformly provided on ceramic tube heap, is equipped with wind-fire wheel type grid 272 in air hole 271, thoroughly
Stomata 271 is arranged along ceramic tube fore-and-aft tilt, and slanted angle is 45 degree, the inclined direction phase of adjacent upper layer and lower layer ceramic tube
Instead, the air hole 271 of upper layer and lower layer ceramic tube is oppositely arranged, and the air hole of entire ceramics tube packing 27 is from top to bottom at wave
Shape.
The working principle of the utility model are as follows:
Light dydrocarbon, nine resinae product of carbon gasify in heating concentration tank, and admixture of gas enters the lower tank of compound-split tower
In body.Since lower tank volume becomes larger, then gas atmosphere is lower, and nine larger molecular organics of carbon in gas are due to condensing temperature phase
To height, liquefies and come out in lower tank.Light dydrocarbon small organic molecule is carried a part of continuation of carbon nine secretly and is risen in gaseous form, upper
The process of liter is in, and gas contacts respectively with upper ceramic filter layer, ceramic tube packing, lower ceramic filter layer, the carbon ninety percent in gas
Divide the recycling that is further liquefied.Gas is when by the air hole of ceramic tube packing, under the vortex of wind-fire wheel type grid, gas
In carbon ninety percent divide and come out by further liquefaction separation.Liquid material in the lower tank of compound-split tower is recycled to compound-split
Gas in tower, with rising collides, and promotes gas cooling liquefaction.
Compared with prior art, the utility model advantageous effects are as follows:
The utility model can be used for dividing carry out purification processes to the carbon ninety percent in light dydrocarbon, nine resinae product of carbon, liquefaction
It is high-efficient.
Detailed description of the invention
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, the accompanying drawings in the following description is only
It is some embodiments of the utility model, for those of ordinary skill in the art, in the premise not made the creative labor
Under, it is also possible to obtain other drawings based on these drawings.
Fig. 1 is the structural schematic diagram of light dydrocarbon described in the utility model, nine resinae product separator of carbon；
Fig. 2 is the schematic diagram of internal structure of upper tower body described in the utility model；
Fig. 3 is ceramic tube top view described in the utility model；
Description of symbols: heating concentration tank -1, compound-split tower -2, condenser -3, material buffer tank -4, upper tower body -
21, lower tank -22, gas access -23, liquid material outlet -24, upper ceramic filter layer -25, recycle stock distributing disc -26, pottery
Porcelain tube filler -27, air hole -271, wind-fire wheel type grid -272, lower ceramic filter layer -28.
Specific embodiment
The preferred embodiment of the utility model is described in detail with reference to the accompanying drawing, so that the advantages of the utility model
It can be easier to be readily appreciated by one skilled in the art with feature, to make the protection scope of the utility model apparent clear
Define.
Refering to Figure of description 1 to shown in Fig. 3, light dydrocarbon, nine resinae product separator of carbon, including heating concentration tank 1,
The exhaust outlet of compound-split tower 2, condenser 3, heating concentration tank 1 is connect with the gas access of compound-split tower 2, compound-split tower
The liquid outlet of 2 bottoms is connect with 4 entrance of material buffer tank, and the outlet of material buffer tank 4 is connect with 3 entrance of condenser, condenser 3
Material outlet is connect with the Matter Transfer entrance of compound-split tower 2；
The heating concentration tank 1 is Double-layer clamp jacketing heat concentration tank, and upper part is equipped with feed inlet and exhaust outlet, and tank bottom is set
There is material outlet mouth；
The thermal medium of the condenser 3 is material；
It is characterized in that, the compound-split tower 2 includes upper tower body 21, lower tank 22, lower tank 22 is tank body, upper tower body
21 be cylindrical body, and 22 lower part of lower tank is equipped with gas access 23, and 22 bottom of lower tank is equipped with liquid material outlet 24, upper tower body 21
It is respectively equipped with ceramic filter layer 25, recycle stock distributing disc 26, ceramic tube packing 27, lower ceramic filter layer 28 from top to bottom,
Upper ceramic filter layer 25, the filter screen that lower ceramic filter layer 28 is ceramic material, the ceramics tube packing 27 is by several ceramics
Pipe accumulation filling forms, and air hole 271 is uniformly provided on ceramic tube heap, is equipped with wind-fire wheel type grid 272 in air hole 271, thoroughly
Stomata 271 is arranged along ceramic tube fore-and-aft tilt, and slanted angle is 45 degree, the inclined direction phase of adjacent upper layer and lower layer ceramic tube
Instead, the air hole 271 of upper layer and lower layer ceramic tube is oppositely arranged, and the air hole of entire ceramics tube packing 27 is from top to bottom at wave
Shape.
Basic principles, main features, and advantages of the present invention has been shown and described above.Current row
The technical staff of industry is it should be appreciated that the present utility model is not limited to the above embodiments, retouching in above embodiments and description
The preference of only the utility model is stated, the utility model is not limited by above-mentioned preference, is not departing from the utility model
Under the premise of spirit and scope, the utility model can also have various changes and modifications, these changes and improvements both fall within practical
In novel claimed range.
While there has been shown and described that the embodiments of the present invention, for the ordinary skill in the art,
It is understood that these embodiments can be carried out with a variety of variations in the case where not departing from the principles of the present invention and spirit, repaired
Change, replacement and variant, the scope of the utility model is defined by the appended claims and the equivalents thereof.
Claims (1)
1. light dydrocarbon, nine resinae product separator of carbon, including heating concentration tank (1), compound-split tower (2), condenser (3),
The exhaust outlet of heating concentration tank (1) is connect with the gas access of compound-split tower (2), the liquid discharge of compound-split tower (2) bottom
Mouth is connect with material buffer tank (4) entrance, and material buffer tank (4) outlet is connect with condenser (3) entrance, condenser (3) material
Outlet is connect with the Matter Transfer entrance of compound-split tower (2)；
The heating concentration tank (1) is Double-layer clamp jacketing heat concentration tank, and upper part is equipped with feed inlet and exhaust outlet, and tank bottom is equipped with
Material outlet mouth；
The thermal medium of the condenser (3) is material；
It is characterized in that, the compound-split tower (2) includes upper tower body (21), lower tank (22), lower tank (22) is tank body, on
Tower body (21) is cylindrical body, and lower tank (22) lower part is equipped with gas access (23), and lower tank (22) bottom goes out equipped with liquid material
Mouth (24), upper tower body (21) are respectively equipped with recycle stock distributing disc (26), upper ceramic filter layer (25), ceramic tube from top to bottom and fill out
Material (27), lower ceramic filter layer (28), upper ceramic filter layer (25), the filter screen that lower ceramic filter layer (28) is ceramic material,
The ceramics tube packing (27) is formed by being no less than three ceramic tube accumulation fillings, and air hole (271) are uniformly provided on ceramic tube,
Wind-fire wheel type grid (272) are equipped in air hole (271), air hole (271) is arranged along ceramic tube fore-and-aft tilt, slanted angle
Be 45 degree, the inclined direction of adjacent upper layer and lower layer ceramic tube on the contrary, the air hole (271) of upper layer and lower layer ceramic tube is oppositely arranged,
The air hole of entire ceramics tube packing (27) waviness from top to bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820839608.7U CN208430056U (en) | 2018-06-01 | 2018-06-01 | Light dydrocarbon, nine resinae product separator of carbon |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820839608.7U CN208430056U (en) | 2018-06-01 | 2018-06-01 | Light dydrocarbon, nine resinae product separator of carbon |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208430056U true CN208430056U (en) | 2019-01-25 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820839608.7U Active CN208430056U (en) | 2018-06-01 | 2018-06-01 | Light dydrocarbon, nine resinae product separator of carbon |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112322320A (en) * | 2020-10-21 | 2021-02-05 | 恒河材料科技股份有限公司 | Separation equipment for carbon-nine resin oil and use method thereof |
-
2018
- 2018-06-01 CN CN201820839608.7U patent/CN208430056U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112322320A (en) * | 2020-10-21 | 2021-02-05 | 恒河材料科技股份有限公司 | Separation equipment for carbon-nine resin oil and use method thereof |
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