CN204261362U - A kind of gathering-device of Rotary Evaporators volatile matter distillation oil - Google Patents
A kind of gathering-device of Rotary Evaporators volatile matter distillation oil Download PDFInfo
- Publication number
- CN204261362U CN204261362U CN201420680052.3U CN201420680052U CN204261362U CN 204261362 U CN204261362 U CN 204261362U CN 201420680052 U CN201420680052 U CN 201420680052U CN 204261362 U CN204261362 U CN 204261362U
- Authority
- CN
- China
- Prior art keywords
- flask
- rotary evaporators
- receiving flask
- volatile matter
- gathering
- 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.)
- Active
Links
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a kind of gathering-device of Rotary Evaporators volatile matter distillation oil, comprise: evaporative flask (9), described evaporative flask (9) connects a teflon seal mechanism (7), described teflon seal mechanism (7) inside arranges a feed tube (8), and teflon seal mechanism (7) is connected with evaporative flask (9) by a tube connector, and be connected with a condenser (6) by another connection feed tube (5), the lower end of this condenser (6) connects one second receiving flask (3), this second receiving flask (3) connects again one first receiving flask (2), the upper end of described first receiving flask (2) arranges a spiracle (1).It can make the refinement more of volatile oil quality according to different to distill further the oil content do not steamed under normal pressure of negative pressure, and its rational in infrastructure, easy to use, efficient volatile matter distillation oil, has good effect.
Description
Technical field
The utility model relates to a kind of gathering-device of Rotary Evaporators volatile matter distillation oil.
Background technology
At present, Rotary Evaporators be mainly used in the industries such as medicine, chemical industry and bio-pharmaceuticals concentrated, crystallization, drying, be separated solvent.
Volatile matter distillation oil now by mature equipment, but can utilize Rotary Evaporators can obtain continuous still volatile oil device through simple transformation.
Utility model content
The utility model has expanded the scope of application of Rotary Evaporators, utilizes the advantage of Rotary Evaporators evaporimeter dynamic rotary (conventional volatile oil distiller raw material is for static) simultaneously.This application is novel provides a kind of Rotary Evaporators volatile oil gathering-device, its rational in infrastructure, easy to use, efficient volatile matter distillation oil.
It is as follows that the utility model solves the problems of the technologies described above taked technical scheme:
A kind of gathering-device of Rotary Evaporators volatile matter distillation oil, comprise: evaporative flask (9), described evaporative flask (9) connects a teflon seal mechanism (7), described teflon seal mechanism (7) inside arranges a feed tube (8), and teflon seal mechanism (7) is connected with evaporative flask (9) by a tube connector, and be connected with a condenser (6) by another connection feed tube (5), the lower end of this condenser (6) connects one second receiving flask (3), this second receiving flask (3) connects again one first receiving flask (2), the upper end of described first receiving flask (2) arranges a spiracle (1).
Further, preferably, the lower end of described condenser (6) is a tube connector, and this tube connector is connected to described second receiving flask (3), and on tube connector, arrange link folder (4).
Further, preferably, described evaporative flask is the evaporative flask of Rotary Evaporators.
After the utility model takes such scheme, can make the refinement more of volatile oil quality according to different to distill further the oil content do not steamed under normal pressure of negative pressure, its rational in infrastructure, easy to use, efficient volatile matter distillation oil, has good effect.
Other features and advantages of the utility model will be set forth in the following description, and, partly become apparent from description, or understand by implementing the utility model.The purpose of this utility model and other advantages realize by structure specifically noted in write description, claims and accompanying drawing and obtain.
Accompanying drawing explanation
Below in conjunction with accompanying drawing, the utility model is described in detail, to make above-mentioned advantage of the present utility model definitely.
Fig. 1 is the structural representation of the gathering-device of a kind of Rotary Evaporators volatile matter distillation of the utility model oil.
Detailed description of the invention
Below in conjunction with specific embodiment, the utility model is described in detail.
As shown in Figure 1, the gathering-device of described Rotary Evaporators volatile matter distillation oil, comprise: evaporative flask 9, described evaporative flask 9 connects a teflon seal mechanism 7, described teflon seal mechanism 7 inside arranges a feed tube 8, and teflon seal mechanism 7 is connected with evaporative flask 9 by a tube connector, and be connected with a condenser 6 by another connection feed tube 5, the lower end of this condenser 6 connects one second receiving flask 3, this second receiving flask 3 connects one first receiving flask 2 again, the upper end of described first receiving flask 2 arranges a spiracle 1, valve 10 is provided with in the bottom of the second receiving flask 3.
Further, preferably, the lower end of described condenser 6 is a tube connector, and this tube connector is connected to described second receiving flask 3, and on tube connector, arrange a link folder 4.
Further, preferably, described evaporative flask is the evaporative flask of Rotary Evaporators.
In addition, be also connected with a ground valve at the sidewall of described second receiving flask 3, connect volatile oil second receiving flask.The utility model can utilize the transformation of Rotary Evaporators receiving flask to achieve the continuous still of volatile oil, increases the usage range of Rotary Evaporators.
Wherein, operation principle of the present invention is:
Utilize the evaporative flask of Rotary Evaporators to accommodate and wait to steam raw material, utilize negative pressure of vacuum from feed tube suction water to evaporative flask, evaporation process closes vacuum, open condensed water, air-distillation, when liquid to be distilled is collected into the discharge valve of the second receiving flask, adjustment receiving flask bleeder valve, make volatile oil remain on discharge valve, make volatile oil flow to the first receiving flask.
This application is novel also can make the refinement more of volatile oil quality according to different to distill further the oil content do not steamed under normal pressure of negative pressure.
Wherein, it utilizes the evaporative flask 9 of Rotary Evaporators to accommodate to wait to steam raw material, utilize negative pressure of vacuum from feed tube 5,8 suction water to evaporative flask 9, evaporation process closes vacuum, opens condensed water, air-distillation, when liquid to be distilled is collected into the discharge valve of the second receiving flask, adjust the bleeder valve of the second receiving flask, make volatile oil remain on discharge valve, make volatile oil flow to the first receiving flask.
After the utility model takes such scheme, can make the refinement more of volatile oil quality according to different to distill further the oil content do not steamed under normal pressure of negative pressure, its rational in infrastructure, easy to use, efficient volatile matter distillation oil, has good effect.
Last it is noted that the foregoing is only preferred embodiment of the present utility model, be not limited to the utility model, although be described in detail the utility model with reference to previous embodiment, for a person skilled in the art, it still can be modified to the technical scheme described in foregoing embodiments, or carries out equivalent replacement to wherein portion of techniques feature.All within spirit of the present utility model and principle, any amendment done, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (3)
1. the gathering-device of a Rotary Evaporators volatile matter distillation oil, it is characterized in that, comprise: evaporative flask (9), described evaporative flask (9) connects a teflon seal mechanism (7), described teflon seal mechanism (7) inside arranges a feed tube (8), and teflon seal mechanism (7) is connected with evaporative flask (9) by a tube connector, and be connected with a condenser (6) by another connection feed tube (5), the lower end of this condenser (6) connects one second receiving flask (3), this second receiving flask (3) connects again one first receiving flask (2), the upper end of described first receiving flask (2) arranges a spiracle (1).
2. the gathering-device of Rotary Evaporators volatile matter distillation oil according to claim 1, it is characterized in that, the lower end of described condenser (6) is a tube connector, and this tube connector is connected to described second receiving flask (3), and on tube connector, arrange link folder (4).
3. the gathering-device of Rotary Evaporators volatile matter distillation oil according to claim 1, is characterized in that, described evaporative flask is the evaporative flask of Rotary Evaporators.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420680052.3U CN204261362U (en) | 2014-11-14 | 2014-11-14 | A kind of gathering-device of Rotary Evaporators volatile matter distillation oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420680052.3U CN204261362U (en) | 2014-11-14 | 2014-11-14 | A kind of gathering-device of Rotary Evaporators volatile matter distillation oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204261362U true CN204261362U (en) | 2015-04-15 |
Family
ID=52796262
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420680052.3U Active CN204261362U (en) | 2014-11-14 | 2014-11-14 | A kind of gathering-device of Rotary Evaporators volatile matter distillation oil |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204261362U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112023430A (en) * | 2019-06-03 | 2020-12-04 | 中石化南京化工研究院有限公司 | Decoking method of chlorobenzene rectifying still liquid |
-
2014
- 2014-11-14 CN CN201420680052.3U patent/CN204261362U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112023430A (en) * | 2019-06-03 | 2020-12-04 | 中石化南京化工研究院有限公司 | Decoking method of chlorobenzene rectifying still liquid |
| CN112023430B (en) * | 2019-06-03 | 2022-06-21 | 中石化南京化工研究院有限公司 | Decoking method of chlorobenzene rectifying still liquid |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202315378U (en) | Novel steam distilling device | |
| CN204485332U (en) | A kind of novel evacuated decompression concentrator | |
| CN204261362U (en) | A kind of gathering-device of Rotary Evaporators volatile matter distillation oil | |
| CN205833144U (en) | A kind of pilot scale rectifier unit | |
| CN205387932U (en) | Oil -gas separation recovery unit | |
| CN203754676U (en) | Grease dewatering equipment | |
| CN204448059U (en) | steam distillation device | |
| CN205287992U (en) | Gas and liquid separator | |
| CN205323276U (en) | Multifunctional extraction tank | |
| CN205748019U (en) | One can realize quantity-produced condenser | |
| CN203803128U (en) | Centrifugal scraper thin film evaporator | |
| CN204233805U (en) | A kind of THF dehydrating tower reflux of improvement | |
| CN202297496U (en) | Heating flash separation device | |
| CN202610217U (en) | Wine steam recycling device | |
| CN204727863U (en) | Improve the volatile oil extractor of distillate pipe | |
| CN101363693A (en) | High performance atomization and water absorption condenser | |
| CN205391810U (en) | Medical oil -water separator | |
| CN205850874U (en) | A kind of adapter of Rotary Evaporators | |
| CN204170626U (en) | A kind of internally provided with vacuum layer plate frame type separator of permeable vaporizing membrane | |
| CN204211489U (en) | Smart selenium equipment is produced in vacuum distilling | |
| CN203989905U (en) | A kind of spray-drying installation | |
| CN208893643U (en) | A kind of Chinese medicine extraction processing initial concentration device | |
| CN204447342U (en) | Steam refiner | |
| CN204469260U (en) | Toluene distillation system | |
| CN204469667U (en) | A kind of vacuum system for the production of silicone sealant |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20211213 Address after: 723200 Liulin Town, Chenggu County, Hanzhong City, Shaanxi Province Patentee after: Shaanxi Tiangu Pharmaceutical Co.,Ltd. Address before: Room 10608, unit 1, building 6, Tsinghua Science Park, No. 65, Keji Second Road, high tech Zone, Xi'an, Shaanxi 710065 Patentee before: SHAANXI TEEGOO BIOTECHNOLOGY GROUP Co.,Ltd. |