CN202052347U - Continuous material dissolving and column chromatography recrystallization purification system - Google Patents
Continuous material dissolving and column chromatography recrystallization purification system Download PDFInfo
- Publication number
- CN202052347U CN202052347U CN2011200732016U CN201120073201U CN202052347U CN 202052347 U CN202052347 U CN 202052347U CN 2011200732016 U CN2011200732016 U CN 2011200732016U CN 201120073201 U CN201120073201 U CN 201120073201U CN 202052347 U CN202052347 U CN 202052347U
- Authority
- CN
- China
- Prior art keywords
- chuck
- jacket
- column
- column chromatography
- molten material
- 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.)
- Expired - Fee Related
Links
Images
Landscapes
- Treatment Of Liquids With Adsorbents In General (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The utility model relates to a continuous material dissolving and column chromatography recrystallization purification system, which is characterized by being mainly formed by sequentially connecting a material dissolving kettle (1), a material filling column (5) and a crystallization kettle (10) in series, wherein the top end of the material filling column (5) is even provided with a material filling column cover (7), a second jacket (6) is arranged outside the material filling column (5), a cyclic hot water inlet (8) and a cyclic hot water outlet (9) are respectively arranged on the second jacket (6), a third jacket (11) is arranged outside the crystallization kettle (10), a third steam inlet (13) and a low-temperature refrigerant inlet (14) are respectively arranged at the upper part of the third jacket (11), and the lower part of the third jacket (11) is provided with a third jacket medium outlet (15). The continuous material dissolving and column chromatography recrystallization purification system adopts the material filling column with jackets and a crystallization kettle system with heating and concentration solvents for being matched with the material dissolving kettle to be used, and the continuous and efficient refining on solid organic compounds in the fine chemical engineering production and the monomer liquid crystal preparation can be realized.
Description
Technical field
The utility model relates to a kind of continuous molten material, column chromatography recrystallization purifying system, and the continuous molten material, insulation column chromatography and the recrystallization that are mainly used in solid product in the preparation of fine chemistry industry production and monomer liquid crystal are purified.
Background technology
Column chromatography and recrystallization are the conventional means of purification refine SOLID ORGANIC compound.The customary filler post is that glass or lucite are made, and internal diameter is relative with length less, generally can't realize being incubated column chromatography, causes crystallization to separate out for solubility easily than miscellaneous goods, and separating effect reduces.Crystallization kettle generally links to each other with low temperature cryosel bath system, does not have heating concentrated solvent function, when column chromatography solvent for use amount is big, often causes the recrystallization effect relatively poor, and yield is on the low side.
Summary of the invention
The purpose of this utility model is to overcome above-mentioned deficiency, provides a kind of and realizes in continuous high-efficient fine chemistry industry is produced and continuous molten material, column chromatography recrystallization purifying system that the SOLID ORGANIC compound in the monomer liquid crystal preparation is made with extra care.
The purpose of this utility model is achieved in that a kind of continuous molten material, column chromatography recrystallization purifying system, described system mainly is in series successively by molten material still, filled column and crystallization kettle, described filled column top even filled column post lid is arranged, described filled column is outside equipped with second chuck, is respectively arranged with the outlet of circulating hot water import and circulating hot water on described second chuck; Described crystallization kettle is outside equipped with the 3rd chuck, and described the 3rd chuck top is respectively arranged with the 3rd steam inlet and the import of low temperature refrigerant, and the bottom is provided with the 3rd chuck media outlet.
Be connected by stainless steel metal net corrugated flexible hose between described molten material still and the filled column.
Described filled column is the stainless steel helices post.
Operation principle of the present utility model is: molten material still links to each other with the stainless steel helices post by stainless steel metal net corrugated flexible hose, and second chuck of filler cornice insulation reaches the insulation purpose by circulating hot water.The 3rd chuck design of crystallization kettle has two conduit entrances, is respectively the 3rd steam inlet and low temperature refrigerant inlet.Solid chemical compound flows directly into the stainless steel helices post heat stirring and dissolving in molten material still after, in the stainless steel helices post, carry out flowing directly into crystallization kettle behind the chromatography, by the valve of opening the 3rd steam inlet crystallization kettle is heated concentrated solution, open the 3rd JO when a certain amount of and discharge hot water in the 3rd chuck when solvent is concentrated to, feed the dynamic crystallization that refrigerant carries out material by low temperature refrigerant inlet to the 3rd chuck this moment again.
Compared with prior art, the beneficial effects of the utility model are:
The utility model adopts the filled column of strap clamp cover and possesses the crystallization kettle system of heating concentrated solvent, cooperates the use of molten material still, can realize that the SOLID ORGANIC compound to reaching in the monomer liquid crystal preparation in the fine chemistry industry production of continuous high-efficient is made with extra care.
Description of drawings
Fig. 1 is the structural representation of a kind of continuous molten material of the utility model, column chromatography recrystallization purifying system.
Wherein: molten material still 1, first chuck 2, first steam inlet 3, first steam (vapor) outlet 4, filled column 5, second chuck 6, filled column post lid 7, circulating hot water import 8, circulating hot water outlet 9, crystallization kettle 10, the 3rd chuck 11, condenser pipe 12, the 3rd steam inlet 13, low temperature refrigerant import 14, the 3rd chuck media outlet 15.
The specific embodiment
Referring to Fig. 1, a kind of continuous molten material that the utility model relates to, column chromatography recrystallization purifying system, mainly be in series successively by molten material still 1, filled column 5 and crystallization kettle 10, described molten material still 1 is outside equipped with first chuck 2, is respectively arranged with first steam inlet 3 and first steam (vapor) outlet 4 on described first chuck 2; Described filled column 5 tops even filled column post lid 7 is arranged, described filled column 5 is outside equipped with second chuck 6, is respectively arranged with circulating hot water import 8 and circulating hot water outlet 9 on described second chuck 6; Described crystallization kettle 10 is outside equipped with the 3rd chuck 11, and described the 3rd chuck 11 tops are respectively arranged with the 3rd steam inlet 13 and low temperature refrigerant import 14, and the bottom is provided with the 3rd chuck media outlet 15; Described crystallization kettle 10 tops are provided with condenser pipe 12.
Be connected by stainless steel metal net corrugated flexible hose between described molten material still 1 and the filled column 5.
Described filled column 5 is the stainless steel helices post.
Claims (3)
1. a continuous molten material, column chromatography recrystallization purifying system, it is characterized in that: described system mainly is in series successively by molten material still (1), filled column (5) and crystallization kettle (10), described filled column (5) top even filled column post lid (7) is arranged, described filled column (5) is outside equipped with second chuck (6), is respectively arranged with circulating hot water import (8) and circulating hot water outlet (9) on described second chuck (6); Described crystallization kettle (10) is outside equipped with the 3rd chuck (11), and described the 3rd chuck (11) top is respectively arranged with the 3rd steam inlet (13) and low temperature refrigerant import (14), and the bottom is provided with the 3rd chuck media outlet (15).
2. a kind of continuous molten material according to claim 1, column chromatography recrystallization purifying system is characterized in that: be connected by stainless steel metal net corrugated flexible hose between described molten material still (1) and the filled column (5).
3. a kind of continuous molten material according to claim 1 and 2, column chromatography recrystallization purifying system is characterized in that: described filled column (5) is the stainless steel helices post.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011200732016U CN202052347U (en) | 2011-08-05 | 2011-08-05 | Continuous material dissolving and column chromatography recrystallization purification system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011200732016U CN202052347U (en) | 2011-08-05 | 2011-08-05 | Continuous material dissolving and column chromatography recrystallization purification system |
Publications (1)
Publication Number | Publication Date |
---|---|
CN202052347U true CN202052347U (en) | 2011-11-30 |
Family
ID=45012334
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2011200732016U Expired - Fee Related CN202052347U (en) | 2011-08-05 | 2011-08-05 | Continuous material dissolving and column chromatography recrystallization purification system |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN202052347U (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105829496A (en) * | 2013-12-18 | 2016-08-03 | 默克专利股份有限公司 | Method for cleaning a liquid crystal mixture |
CN105980848A (en) * | 2013-12-10 | 2016-09-28 | 默克专利股份有限公司 | Cleaning device |
CN106140541A (en) * | 2015-03-23 | 2016-11-23 | 上海强精金属制品有限公司 | A kind of electrostatic spraying powder body circulation and stress device |
CN113209670A (en) * | 2021-06-23 | 2021-08-06 | 内蒙古工业大学 | Xylo-oligosaccharide separation and purification system and process in sequential simulated moving bed coupling crystallization process |
-
2011
- 2011-08-05 CN CN2011200732016U patent/CN202052347U/en not_active Expired - Fee Related
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105980848A (en) * | 2013-12-10 | 2016-09-28 | 默克专利股份有限公司 | Cleaning device |
US10052566B2 (en) | 2013-12-10 | 2018-08-21 | Merck Patent Gmbh | Purification device for a liquid-crystal mixture |
CN105829496A (en) * | 2013-12-18 | 2016-08-03 | 默克专利股份有限公司 | Method for cleaning a liquid crystal mixture |
CN105829496B (en) * | 2013-12-18 | 2019-01-18 | 默克专利股份有限公司 | Method for purifying liquid crystal compound |
CN106140541A (en) * | 2015-03-23 | 2016-11-23 | 上海强精金属制品有限公司 | A kind of electrostatic spraying powder body circulation and stress device |
CN113209670A (en) * | 2021-06-23 | 2021-08-06 | 内蒙古工业大学 | Xylo-oligosaccharide separation and purification system and process in sequential simulated moving bed coupling crystallization process |
CN113209670B (en) * | 2021-06-23 | 2022-11-11 | 内蒙古工业大学 | Xylo-oligosaccharide separation and purification system and process in sequential simulated moving bed coupling crystallization process |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN202052347U (en) | Continuous material dissolving and column chromatography recrystallization purification system | |
CN101125839A (en) | Processing method for mother liquid in maltol production and device thereof | |
CN204352578U (en) | Alcohol in high concentration recovery tower | |
CN210613654U (en) | Distillation purification device | |
CN209630647U (en) | A kind of serialization preparation facilities of silicone oil | |
CN217612958U (en) | Purification device for medical intermediate | |
CN206621817U (en) | A kind of energy-conserving and environment-protective chlorophenesic acid continuous rectification system | |
CN105199607A (en) | Live air tangent jetting spinning type rosin distillation device and use thereof | |
CN109251140A (en) | Benzoic acid method of purification and purifying plant | |
CN102350082B (en) | Crystallizing tank used for Arteether | |
CN201988208U (en) | Novel alcohol recovery apparatus | |
CN202526925U (en) | Reduced pressure distillation device | |
CN113735695A (en) | Method for preparing high-carbon aldehyde by adopting high-carbon olefin and production device thereof | |
CN210131547U (en) | Chemical raw material pre-dissolving device | |
CN203227319U (en) | Reboiler at bottom of anthracene distillation tower | |
CN202199158U (en) | Special crystalizing tank for vinpocetine | |
CN207324125U (en) | A kind of glacial acetic acid equipment for purifying | |
CN201458996U (en) | Device for removing calcium formate from pentaerythritol in calcium-method production | |
CN207463213U (en) | A kind of n-vinyl pyrrolidone crystallizer | |
CN201894869U (en) | 3-cyanopyridine fractional crystallizer | |
CN2569867Y (en) | Vacuum distillation device | |
CN205528528U (en) | Little algae DHA separation and purification device | |
CN202020932U (en) | Rectification device for ultra-pure nitric acid | |
CN203989914U (en) | A kind of acetic acid purifying plant | |
CN203355332U (en) | Continuous sebacic acid di-methyl ester rectification device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20111130 Termination date: 20140805 |
|
EXPY | Termination of patent right or utility model |