CN203960089U - A kind of high purity L-Borneol extraction element - Google Patents
A kind of high purity L-Borneol extraction element Download PDFInfo
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- CN203960089U CN203960089U CN201420290536.7U CN201420290536U CN203960089U CN 203960089 U CN203960089 U CN 203960089U CN 201420290536 U CN201420290536 U CN 201420290536U CN 203960089 U CN203960089 U CN 203960089U
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- cooling tank
- rectifier
- strainer
- distillation pot
- whizzer
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Abstract
A kind of high purity L-Borneol extraction element that the utility model provides, comprises distiller, first cold bucket, whizzer, storage vat, rectifier, front cooling tank, distillation pot, rear cooling tank, strainer; Described distiller, first cold bucket, whizzer, storage vat, rectifier, front cooling tank, distillation pot, rear cooling tank, strainer successively pipeline connect, and by the control of DCS system.The utility model: the 1. integrated operation of whole plant, the pollution of having avoided pilot process to bring, has also avoided the loss of raw material in operation process greatly; 2. single Controlling System is carried out entirety and is controlled, and has avoided between multiple Controlling System, in the conflict of the each side such as time, energy consumption, manpower consumption, having saved greatly the energy, has reduced enterprise cost; 3. operation is simplified greatly, and 1～3 people can ensure the normal operation of whole plant, has reduced the input of enterprise aspect manpower.
Description
Technical field
The utility model relates to a kind of high purity L-Borneol extraction element.
Background technology
In prior art for the extraction of L-Borneol, also do not have the device of a whole set of automatic operating, although patent " a kind of preparation method of L-Borneol and preparation apparatus (CN102423331B that my company applied in 2011, 2014.01.15) " a kind of preparation apparatus of L-Borneol is provided, but this preparation apparatus does not provide the scheme of integrated a whole set of automatic operating, even the most basic integratedly also do not realize, to such an extent as in practice process, transient process between each equipment can cause great waste to raw material, and there is a great Pollution risk, and each equipment independently arranges, each equipment respectively has control device, and these control device all need independent energy consumption, can cause thus the significant wastage of the energy.
Utility model content
For solving the problems of the technologies described above, the utility model provides a kind of high purity L-Borneol extraction element, this high purity L-Borneol extraction element is by integral structure, the control of DCS entire system, realized integrated the whole series of extracting for L-Borneol and automatically moved, seamless link between each equipment, has avoided Pollution risk greatly, the in aggregates control of each equipment structure, avoid the independent energy consumption of Controlling System, saved greatly the energy, and also greatly reduced the human cost that enterprise need to drop into.
The utility model is achieved by the following technical programs.
A kind of high purity L-Borneol extraction element that the utility model provides, comprises distiller, first cold bucket, whizzer, storage vat, rectifier, front cooling tank, distillation pot, rear cooling tank, strainer; Described distiller, first cold bucket, whizzer, storage vat, rectifier, front cooling tank, distillation pot, rear cooling tank, strainer successively pipeline connect, wherein distiller, rectifier, distillation pot are positioned at extreme lower position, and distiller, rectifier, distillation pot bottom are provided with heating unit; Described just cold bucket is arranged on whizzer top, and the outlet of first cold bucket and whizzer are straight-through; During being connected, the pipeline of described storage vat and rectifier is also provided with feeding pump; Described strainer filters and realizes by production board, and production board can take out from the side exit of strainer; Described filter bottom pipeline is connected in distillation pot bottom, side, and strainer is provided with reflux pump in being connected with the pipeline of distillation pot; The pipeline of described front cooling tank and distillation pot is connected to one-way channel; Described front cooling tank and rear cooling tank share cooling water pipeline.
Described rectifier inside is provided with grid agitator.
Described distiller, first cold bucket, whizzer, storage vat, rectifier, front cooling tank, distillation pot, rear cooling tank, strainer are by the control of DCS system.
The beneficial effects of the utility model are: the 1. integrated operation of whole plant, and the pollution of having avoided pilot process to bring, has also avoided the loss of raw material in operation process greatly; 2. single Controlling System is carried out entirety and is controlled, and has avoided between multiple Controlling System, in the conflict of the each side such as time, energy consumption, manpower consumption, having saved greatly the energy, has reduced enterprise cost; 3. operation is simplified greatly, and 1～3 people can ensure the normal operation of whole plant, has reduced the input of enterprise aspect manpower.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the front view of Fig. 1;
Fig. 3 is the vertical view of Fig. 1;
Fig. 4 is the side-view of Fig. 1;
In figure: 11-distiller, just cold bucket of 12-, 13-whizzer, 14-storage vat, 21-feeding pump, 22-rectifier, cooling tank before 23-, 24-distil pot, cooling tank after 31-, 32-strainer, 33-production board, 34-reflux pump.
Embodiment
Further describe the technical solution of the utility model below, but described in claimed scope is not limited to.
A kind of high purity L-Borneol extraction element as shown in Figures 1 to 4, comprises distiller 11, first cold bucket 12, whizzer 13, storage vat 14, rectifier 22, front cooling tank 23, distillation pot 24, rear cooling tank 31, strainer 32; Described distiller 11, first cold bucket 12, whizzer 13, storage vat 14, rectifier 22, front cooling tank 23, distillation pot 24, rear cooling tank 31, strainer 32 successively pipeline connect, wherein distiller 11, rectifier 22, distillation pot 24 are positioned at extreme lower position, and distiller 11, rectifier 22, distillation pot 24 bottoms are provided with heating unit; Described just cold bucket 12 is arranged on whizzer 13 tops, and the outlet of first cold bucket 12 and whizzer 13 are straight-through; Described storage vat 14 is also provided with feeding pump 21 in being connected with the pipeline of rectifier 22; Described strainer 32 filters by production board 33 to be realized, and production board 33 can take out from the side exit of strainer 32; Described strainer 32 bottom pipe are connected in distillation pot 24 bottoms, side, and strainer 32 is provided with reflux pump 34 in being connected with the pipeline of distillation pot 24; The pipeline of described front cooling tank 23 and distillation pot 24 is connected to one-way channel; Described front cooling tank 23 and rear cooling tank 31 share cooling water pipeline.
Described rectifier 22 inside are provided with grid agitator.
Described distiller 11, first cold bucket 12, whizzer 13, storage vat 14, rectifier 22, front cooling tank 23, distillation pot 24, rear cooling tank 31, strainer 32 are by the control of DCS system.
Claims (3)
1. a high purity L-Borneol extraction element, comprise distiller (11), first cold bucket (12), whizzer (13), storage vat (14), rectifier (22), front cooling tank (23), distillation pot (24), rear cooling tank (31), strainer (32), it is characterized in that: described distiller (11), first cold bucket (12), whizzer (13), storage vat (14), rectifier (22), front cooling tank (23), distillation pot (24), rear cooling tank (31), strainer (32) successively pipeline connects, wherein distiller (11), rectifier (22), distillation pot (24) is positioned at extreme lower position, and distiller (11), rectifier (22), distillation pot (24) bottom is provided with heating unit, described just cold bucket (12) is arranged on whizzer (13) top, and the outlet of first cold bucket (12) and whizzer (13) are straight-through, described storage vat (14) is also provided with feeding pump (21) in being connected with the pipeline of rectifier (22), described strainer (32) filters by production board (33) and realizes, and production board (33) can take out from the side exit of strainer (32), described strainer (32) bottom pipe is connected in distillation pot (24) bottom, side, and strainer (32) is provided with reflux pump (34) in being connected with the pipeline of distillation pot (24), the pipeline of described front cooling tank (23) and distillation pot (24) is connected to one-way channel, described front cooling tank (23) and rear cooling tank (31) share cooling water pipeline.
2. high purity L-Borneol extraction element as claimed in claim 1, is characterized in that: described rectifier (22) inside is provided with grid agitator.
3. high purity L-Borneol extraction element as claimed in claim 1, is characterized in that: described distiller (11), first cold bucket (12), whizzer (13), storage vat (14), rectifier (22), front cooling tank (23), distillation pot (24), rear cooling tank (31), strainer (32) are by the control of DCS system.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420290536.7U CN203960089U (en) | 2014-06-03 | 2014-06-03 | A kind of high purity L-Borneol extraction element |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420290536.7U CN203960089U (en) | 2014-06-03 | 2014-06-03 | A kind of high purity L-Borneol extraction element |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203960089U true CN203960089U (en) | 2014-11-26 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201420290536.7U Active CN203960089U (en) | 2014-06-03 | 2014-06-03 | A kind of high purity L-Borneol extraction element |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104030888A (en) * | 2014-06-03 | 2014-09-10 | 江口县苗药生物科技有限公司 | High-purity Borneolum Luodian extractor |
-
2014
- 2014-06-03 CN CN201420290536.7U patent/CN203960089U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104030888A (en) * | 2014-06-03 | 2014-09-10 | 江口县苗药生物科技有限公司 | High-purity Borneolum Luodian extractor |
| CN104030888B (en) * | 2014-06-03 | 2015-12-09 | 江口县苗药生物科技有限公司 | A kind of high purity L-Borneol extraction element |
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