CN205569800U - Natural borneol's multistage condensation crystallization extraction element - Google Patents
Natural borneol's multistage condensation crystallization extraction element Download PDFInfo
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- CN205569800U CN205569800U CN201620333994.3U CN201620333994U CN205569800U CN 205569800 U CN205569800 U CN 205569800U CN 201620333994 U CN201620333994 U CN 201620333994U CN 205569800 U CN205569800 U CN 205569800U
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- crystallization
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Abstract
The utility model discloses a natural borneol's multistage condensation crystallization extraction element, including two at least condensation cooling kettle, condensation cooling kettle has crystallization inner chamber and a cooling water jacket chamber, the cooling water jacket intracavity be equipped with the spiral attached cooling and heat exchanging coil pipe on the crystallization inner chamber, the steam that still is equipped with natural borneol steam on the condensation cooling kettle advances the pipe and is used for the extraction to tie post -crystalline natural borneol's material gravity line, the material gravity line is connected with one and draws centrifuge, condensation cooling kettle's upper end is equipped with the kettle cover of a hydrolock. The utility model discloses can cool off natural borneol's the multiple -order condensation cooling kettle of steam process, and then accomplished the crystallization of condensation thoroughly to natural borneol, and reduced the waste of raw materials widely, improved natural borneol's extraction efficiency.
Description
Technical field
This utility model relates to the processing technique field of natural Broneolum Syntheticum, specifically refers to the multi-stage condensing crystallization extraction element of a kind of natural Broneolum Syntheticum.
Background technology
Natural Broneolum Syntheticum is that the fresh branch and leaf of canella Camphor tree are extracted to be processed into, for white crystals sprills or flaky crystal.
At present, natural Broneolum Syntheticum add man-hour, need the steam wiring with natural Broneolum Syntheticum is crystallized condensation process, but the process equipment of traditional natural Broneolum Syntheticum cannot be accomplished to extract up hill and dale when the extraction of natural Broneolum Syntheticum crystallizes condensation, substantial amounts of wastage of material often occurs, and the structure of traditional extraction equipment is complicated, but the efficiency of the extraction of natural Broneolum Syntheticum is the lowest.
Utility model content
This utility model is in order to solve the above-mentioned deficiency of prior art, it is proposed that the multi-stage condensing crystallization extraction element of a kind of natural Broneolum Syntheticum.
In order to solve above-mentioned technical problem, this utility model is by the following technical solutions: the multi-stage condensing crystallization extraction element of a kind of natural Broneolum Syntheticum, cooling reactor is condensed including at least two, it is connected by steam pipeline between described condensation cooling reactor with condensation cooling reactor, described condensation cooling reactor has crystallization inner chamber, the outside of described crystallization inner chamber is cooling water jecket chamber, described cooling water jecket intracavity is provided with the cooling heat transferring coil pipe that spiral is attached on described crystallization inner chamber, and described cooling heat transferring coil pipe is provided with coolant inlet pipe and coolant goes out pipe；The steam inlet tube of natural Broneolum Syntheticum steam and the material gravity line of the natural Broneolum Syntheticum after extracting crystallization it is additionally provided with on described condensation cooling reactor, described material gravity line connects an extraction centrifuge, and the upper end of described condensation cooling reactor is provided with the kettle cover of a hydrolock.
Further, wherein, the water outlet port, bottom of the condensation cooling reactor being arranged on final stage is provided with aqueous solution recovery tube, and the backflow of described aqueous solution recovery tube is connected to the steam inlet tube of initial stage condensation cooling reactor, and is provided with Pressure gauge on described aqueous solution recovery tube and reclaims air exhauster.
Further, the kettle cover of described hydrolock includes being arranged on Wheel-type truss and four fans being arranged on Wheel-type truss seal lid, and described Wheel-type truss is made up of circular channels and crosswise tank.
Compared with prior art, natural Broneolum Syntheticum steam in condensation cooling reactor can quickly be cooled down by cooling heat transferring coil pipe that the spiral that this utility model uses is arranged rapidly, make the quick condensation-crystallization of natural Broneolum Syntheticum of natural Broneolum Syntheticum steam, and have employed multistage condensation cooling reactor and carry out operation, so steam with natural Broneolum Syntheticum cools down through multistage condensation cooling reactor, and then accomplished condensation-crystallization up hill and dale, greatly reduce the waste of raw material, improve the extraction efficiency of natural Broneolum Syntheticum.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model；
Fig. 2 is the top view of condensation cooling reactor of the present utility model.
Detailed description of the invention
With embodiment, utility model is described in detail below in conjunction with the accompanying drawings.
As illustrated in fig. 1 and 2, the multi-stage condensing crystallization extraction element of the natural Broneolum Syntheticum that the utility model proposes, including two condensation cooling reactors 1, it is connected by steam pipeline 13 between condensation cooling reactor 1 with condensation cooling reactor 1, condensation cooling reactor has crystallization inner chamber 2, the outside of crystallization inner chamber 2 is cooling water jecket chamber 3, is provided with the cooling heat transferring coil pipe 4 that spiral is attached on crystallization inner chamber 2 in cooling water jecket chamber 3, and cooling heat transferring coil pipe 4 is provided with coolant inlet pipe 5 and coolant goes out pipe 6.
Being additionally provided with the steam inlet tube 7 of natural Broneolum Syntheticum steam and the material gravity line 8 of the natural Broneolum Syntheticum after extracting crystallization on condensation cooling reactor 1, material gravity line 8 connects an extraction centrifuge 9, and the upper end of condensation cooling reactor 1 is provided with the kettle cover 10 of a hydrolock.Wherein, the water outlet port, bottom of the condensation cooling reactor being arranged on final stage is provided with aqueous solution recovery tube 11, aqueous solution recovery tube 11 backflow is connected to the steam inlet tube 7 of initial stage condensation cooling reactor, and is provided with Pressure gauge 12 on described aqueous solution recovery tube 11 and reclaims air exhauster 14.
The kettle cover 10 of hydrolock includes being arranged on Wheel-type truss 15 and four fans being arranged on Wheel-type truss 15 seal lid 16, and Wheel-type truss 15 is made up of circular channels and crosswise tank.
In this utility model, have employed multistage condensation-crystallization structure, typically the quantitative design condensation cooling reactor 1 is 4, steam inlet tube 7 is arranged on the condensation cooling reactor of initial stage, steam enters in whole stage purifying device from this steam inlet tube 7, wherein, the moment pre-cooling when steam enters into condensation cooling reactor, and then the crystallization that is liquefied, crystallized product after crystallization piles up on the liquid level of condensation cooling reactor, is dehydrated along with the increase of crystallized product amount is the most just flowed in extraction centrifuge 9 from material gravity line 8.And initial stage condensation cooling reactor in do not complete crystallization steam and aqueous solution carry out being transferred to next stage by steam pipeline 13, the condensation cooling reactor of straight only afterbody, the last steam inlet tube 7 that is back to again carries out the crystallization of secondary again, so circulates and carries out.
Above-described embodiment only have expressed several embodiments of the present utility model, and it describes more concrete and detailed, but can not be therefore understands that be the restriction to this utility model the scope of the claims.It should be pointed out that, for the person of ordinary skill of the art, without departing from the concept of the premise utility, it is also possible to make some deformation and improvement, these broadly fall into protection domain of the present utility model.Therefore, this utility model patent and protection domain should be as the criterion with appended claims.
Claims (3)
1. the multi-stage condensing crystallization extraction element of a natural Broneolum Syntheticum, it is characterized in that: include at least two condensation cooling reactor (1), it is connected by steam pipeline (13) between described condensation cooling reactor (1) with condensation cooling reactor (1), described condensation cooling reactor has crystallization inner chamber (2), the outside of described crystallization inner chamber (2) is cooling water jecket chamber (3), the cooling heat transferring coil pipe (4) that spiral is attached on described crystallization inner chamber (2) it is provided with in described cooling water jecket chamber (3), described cooling heat transferring coil pipe (4) goes out pipe (6) with coolant inlet pipe (5) and coolant；The steam inlet tube (7) of natural Broneolum Syntheticum steam and the material gravity line (8) of the natural Broneolum Syntheticum after extracting crystallization it is additionally provided with on wherein primary condensation cooling reactor (1), described material gravity line (8) connects an extraction centrifuge (9), and the upper end of described condensation cooling reactor (1) is provided with the kettle cover (10) of a hydrolock.
2. the multi-stage condensing crystallization extraction element of natural Broneolum Syntheticum as claimed in claim 1, it is characterized in that: the water outlet port, bottom of the condensation cooling reactor being arranged on final stage is provided with aqueous solution recovery tube (11), the backflow of described aqueous solution recovery tube (11) is connected to the steam inlet tube (7) of initial stage condensation cooling reactor, and is provided with Pressure gauge (12) on described aqueous solution recovery tube (11) and reclaims air exhauster (14).
3. the multi-stage condensing crystallization extraction element of natural Broneolum Syntheticum as claimed in claim 1, it is characterized in that: the kettle cover (10) of described hydrolock includes being arranged on Wheel-type truss (15) and four fans being arranged on Wheel-type truss (15) seal lid (16), and described Wheel-type truss (15) is made up of circular channels and crosswise tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620333994.3U CN205569800U (en) | 2016-04-20 | 2016-04-20 | Natural borneol's multistage condensation crystallization extraction element |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620333994.3U CN205569800U (en) | 2016-04-20 | 2016-04-20 | Natural borneol's multistage condensation crystallization extraction element |
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| CN205569800U true CN205569800U (en) | 2016-09-14 |
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| CN201620333994.3U Active CN205569800U (en) | 2016-04-20 | 2016-04-20 | Natural borneol's multistage condensation crystallization extraction element |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106390507A (en) * | 2016-11-23 | 2017-02-15 | 重庆鹏越科技发展有限公司 | Continuous vacuum crystallization system of titanium black liquor and application method of continuous vacuum crystallization system |
| CN110935189A (en) * | 2019-12-12 | 2020-03-31 | 东莞市泰丰空调制冷设备有限公司 | Condensate water collecting device for steam condensation and using method thereof |
-
2016
- 2016-04-20 CN CN201620333994.3U patent/CN205569800U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106390507A (en) * | 2016-11-23 | 2017-02-15 | 重庆鹏越科技发展有限公司 | Continuous vacuum crystallization system of titanium black liquor and application method of continuous vacuum crystallization system |
| CN110935189A (en) * | 2019-12-12 | 2020-03-31 | 东莞市泰丰空调制冷设备有限公司 | Condensate water collecting device for steam condensation and using method thereof |
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Legal Events
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 343000 Ji'an City, Jiangxi Province Hing town, Jizhou District No. 61 Jiangxi Jinggangshan national agricultural science and Technology Park Patentee after: Jiangxi Forestry Department borneol Polytron Technologies Inc Address before: 343000 Ji'an City, Jiangxi Province Hing town, Jizhou District No. 61 Jiangxi Jinggangshan national agricultural science and Technology Park Patentee before: Linke Borneol Science and Technology Company Limited |