CN205740906U - Petroleum ether extraction segregation apparatus - Google Patents
Petroleum ether extraction segregation apparatus Download PDFInfo
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- CN205740906U CN205740906U CN201620664754.1U CN201620664754U CN205740906U CN 205740906 U CN205740906 U CN 205740906U CN 201620664754 U CN201620664754 U CN 201620664754U CN 205740906 U CN205740906 U CN 205740906U
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Abstract
This utility model relates to petroleum ether extraction segregation apparatus, its technical scheme is: be provided with sealing lid at the top of extraction tank body, extraction material import it is provided with on the right side sealing lid, it is provided with temperature testing device on the right side of the middle part sealing lid, it is provided with extractant import on the left of the middle part sealing lid, it is provided with atmospheric valve in the left side sealing lid, it is provided with puddler at extraction tank interior center, the top of puddler connects motor, the bottom of puddler is provided with stirring paddle, it is provided with in the bottom of extraction tank body and adds heat pipe, the outlet of extraction tank body connects treating column by drain pipe, the external connection hydrogenation cylinder of described treating column, the inside for the treatment of column is provided with heating pole, the top for the treatment of column is provided with condensing tube, condensing tube connects catcher, described condensing tube tilts to be fixed on the top for the treatment of column；The beneficial effects of the utility model are: simple in construction, easy to use, are effectively increased the effect of extracting of petroleum ether, improve the production efficiency of petroleum ether, decrease the content of impurity and harmful substance, have saved production cost.
Description
Technical field
This utility model relates to field of petrochemical industrial, particularly to a kind of petroleum ether extraction segregation apparatus.
Background technology
Petroleum ether is colourless transparent liquid, has the mixture of kerosene abnormal smells from the patient, predominantly pentane and hexane；Water insoluble, molten
In most organic solvent such as dehydrated alcohol, benzene, chloroform, oils, it is mainly used as solvent and oils and fats processes.
Along with development and the reinforcement of environmental consciousness of national economy, the prescription of petroleum hydrocarbon solvent product is more come by country
The highest.Early stage common petroleum ether product had once been widely used because the big valency of its amount is low, but now with naphtha cut as raw material
The petroleum ether product prepared through common fractional distillation, hydrogenation or additive method is big because of abnormal smells from the patient, boiling range width, and impurity content is high, residual many and
Extremely denouncing, many application are restricted, and have been not suitable with the requirement of current national environmental protection development.Therefore in the urgent need to exploitation
A kind of deep hydrofinishing extraction separation device, to adapt to the market demand of the environmentally friendly solvent of current colorless and odorless.
Summary of the invention
The purpose of this utility model is aiming at the drawbacks described above that prior art exists, it is provided that petroleum ether extraction separates dress
Put, simple in construction, easy to use, it is effectively increased the effect of extracting of petroleum ether, improves the production efficiency of petroleum ether, decrease
Impurity and the content of harmful substance, saved production cost.
Its technical scheme is: include extract tank body, extraction material import, temperature testing device, extractant import, atmospheric valve,
Motor, puddler, stirring paddle, add heat pipe, seal lid, drain pipe, treating column, hydrogenation cylinder, heating pole, condensing tube, catcher,
It is provided with sealing lid at the top of extraction tank body, is provided with extraction material import on the right side sealing lid, sets on the right side of the middle part sealing lid
There is temperature testing device, on the left of the middle part sealing lid, be provided with extractant import, be provided with atmospheric valve in the left side sealing lid, in extraction
Taking tank interior center and be provided with puddler, the top of puddler connects motor, and the bottom of puddler is provided with stirring paddle, at extractor
The bottom of body is provided with and adds heat pipe, and the outlet of extraction tank body connects treating column, the external connection of described treating column by drain pipe
Hydrogenation cylinder, the inside for the treatment of column is provided with heating pole, and the top for the treatment of column is provided with condensing tube, and condensing tube connects catcher, described
Condensing tube tilt to be fixed on the top for the treatment of column.
The inwall of above-mentioned condensing tube is provided with spiral cold plate.
The beneficial effects of the utility model are: simple in construction, easy to use, are effectively increased the effect of extracting of petroleum ether,
Improve the production efficiency of petroleum ether, decrease the content of impurity and harmful substance, saved production cost.
Accompanying drawing explanation
Accompanying drawing 1 is structural representation of the present utility model；
In Fig. 1: extraction tank body 1, extraction material import 2, temperature testing device 3, extractant import 4, atmospheric valve 5, motor 6,
Puddler 7, stirring paddle 8, add heat pipe 9, seal lid 10, drain pipe 11, treating column 12, hydrogenation cylinder 13, heating pole 14, condensing tube
15, catcher 16.
Detailed description of the invention
In conjunction with accompanying drawing 1, the utility model will be further described:
This utility model includes extracting tank body 1, extraction material import 2, temperature testing device 3, extractant import 4, atmospheric valve
5, motor 6, puddler 7, stirring paddle 8, add heat pipe 9, seal lid 10, drain pipe 11, treating column 12, hydrogenation cylinder 13, heating pole
14, condensing tube 15, catcher 16, is provided with sealing lid 10 at the top of extraction tank body 1, is provided with extraction material on the right side sealing lid 10
Import 2, is provided with temperature testing device 3 on the right side of the middle part sealing lid 10, is provided with extractant and enters on the left of the middle part sealing lid 10
Mouth 4, is provided with atmospheric valve 5 in the left side sealing lid 10, is provided with puddler 7, the top of puddler 7 in extraction tank body 1 inside center
Connecting motor 6, the bottom of puddler 7 is provided with stirring paddle 8, is provided with in the bottom of extraction tank body 1 and adds heat pipe 9, going out of extraction tank body 1
Mouth connects treating column 12 by drain pipe 11, the external connection hydrogenation cylinder 13 of described treating column 12, the inside for the treatment of column 12
Being provided with heating pole 14, the top for the treatment of column 12 is provided with condensing tube 15, and condensing tube 15 connects catcher 16, and described condensing tube 15 inclines
Tiltedly it is fixed on the top for the treatment of column 12.
Preferably, the inwall of described condensing tube 15 is provided with spiral cold plate.
Operation principle:
In work process, base oil ether is joined the inside of extraction tank body 1, realize fractional distillation extraction by adding extractant
Take, extraction process is regulated by temperature testing device the extraction temperature within tank body 1 in real time, it is ensured that the temperature of extraction reaches
Effect well, enters treating column internal addition hydrogen, it is achieved refined, after refining, petroleum ether is by evaporating into condensation after extraction
Inside pipe wall realizes condensation, thus prepares high-purity petroleum ether, and this device is in process of production by the tank body of regulation extraction in real time
Temperature, it is ensured that the stability of extraction process, improves the quality of product, reduces the impurity of product.
The above, be only preferred embodiment of the present utility model, and any those of ordinary skill in the art all may profit
This utility model is revised by the technical scheme of above-mentioned elaboration or is revised as the technical scheme of equivalent.Therefore, foundation
Any simple modification that the technical solution of the utility model is carried out or substitute equivalents, belong to the greatest extent this utility model claimed
Scope.
Claims (2)
1. petroleum ether extraction segregation apparatus, is characterized in that: include extracting tank body, extraction material import, temperature testing device, extractant
Import, atmospheric valve, motor, puddler, stirring paddle, add heat pipe, seal lid, drain pipe, treating column, hydrogenation cylinder, heating pole, cold
Solidifying pipe, catcher, be provided with sealing lid at the top of extraction tank body, is provided with extraction material import on the right side sealing lid, is sealing lid
Middle part on the right side of be provided with temperature testing device, seal lid middle part on the left of be provided with extractant import, seal lid left side set
Having atmospheric valve, be provided with puddler at extraction tank interior center, the top of puddler connects motor, and the bottom of puddler is provided with to be stirred
Mixing oar, be provided with in the bottom of extraction tank body and add heat pipe, the outlet of extraction tank body connects treating column by drain pipe, and described is refined
The external connection hydrogenation cylinder of tower, the inside for the treatment of column is provided with heating pole, and the top for the treatment of column is provided with condensing tube, and condensing tube connects
Catcher, described condensing tube tilts to be fixed on the top for the treatment of column.
Petroleum ether extraction segregation apparatus the most according to claim 1, is characterized in that: the inwall of described condensing tube is provided with spiral shell
Rotation cold plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620664754.1U CN205740906U (en) | 2016-06-29 | 2016-06-29 | Petroleum ether extraction segregation apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620664754.1U CN205740906U (en) | 2016-06-29 | 2016-06-29 | Petroleum ether extraction segregation apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205740906U true CN205740906U (en) | 2016-11-30 |
Family
ID=57382721
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620664754.1U Active CN205740906U (en) | 2016-06-29 | 2016-06-29 | Petroleum ether extraction segregation apparatus |
Country Status (1)
| Country | Link |
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| CN (1) | CN205740906U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107189815A (en) * | 2017-05-24 | 2017-09-22 | 张义中 | A kind of nonpetroleum ether extraction separation device |
| CN107941590A (en) * | 2017-07-10 | 2018-04-20 | Cem有限公司 | Prepared using the analytical analysis for being energized decentralized extraction with quick sample |
| CN111315458A (en) * | 2017-10-30 | 2020-06-19 | 惠斯勒科技公司 | Terpene enrichment methods and systems |
-
2016
- 2016-06-29 CN CN201620664754.1U patent/CN205740906U/en active Active
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107189815A (en) * | 2017-05-24 | 2017-09-22 | 张义中 | A kind of nonpetroleum ether extraction separation device |
| CN107941590A (en) * | 2017-07-10 | 2018-04-20 | Cem有限公司 | Prepared using the analytical analysis for being energized decentralized extraction with quick sample |
| CN111315458A (en) * | 2017-10-30 | 2020-06-19 | 惠斯勒科技公司 | Terpene enrichment methods and systems |
| US11406679B2 (en) | 2017-10-30 | 2022-08-09 | Whistler Technologies Corp. | Terpene enrichment methods and systems |
| CN111315458B (en) * | 2017-10-30 | 2022-11-11 | 惠斯勒科技公司 | Terpene enrichment methods and systems |
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