CN210367611U - Device for preparing oil purifier - Google Patents
Device for preparing oil purifier Download PDFInfo
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- CN210367611U CN210367611U CN201922129768.XU CN201922129768U CN210367611U CN 210367611 U CN210367611 U CN 210367611U CN 201922129768 U CN201922129768 U CN 201922129768U CN 210367611 U CN210367611 U CN 210367611U
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- heat exchanger
- reaction kettle
- petroleum ether
- pipeline
- extraction
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Abstract
The utility model relates to a device for preparing clean oil, belonging to the technical field of spice extraction devices; the extraction reaction kettle is connected with the recovered petroleum ether reaction kettle through a pipeline, the extraction reaction kettle and the recovered petroleum ether reaction kettle are respectively connected with a first heat exchanger and a third heat exchanger through pipelines, the first heat exchanger and the third heat exchanger are respectively connected with a second heat exchanger and a fourth heat exchanger through pipelines, the second heat exchanger is connected to the extraction reaction kettle through a pipeline, and the fourth heat exchanger is connected with the solvent receiving tank through a pipeline; the utility model discloses the extraction liquid need not artifical directly emit, just can flow into automatically and retrieve reation kettle and carry out petroleum ether and retrieve as long as open the valve, has reduced manual operation intensity, and the petroleum ether conveying has all stopped inflammable gas in airtight space and has volatilized and guaranteed production safety, and the petroleum ether rate of recovery obtains rising by a wide margin, and manufacturing cost effectively descends, and sets up the promotion of heat exchanger recovery speed, and production efficiency obviously improves.
Description
Technical Field
The utility model relates to a device of preparation absolute belongs to spices extraction element technical field.
Background
After extraction is finished in the production of the clean oil, extraction liquid is directly discharged manually, the petroleum ether is recovered by using a glass flask, and in the process, the petroleum ether is low in boiling point, easy to volatilize quickly, has large burning and explosion potential safety hazards, and is too much lost, so that the production cost is increased.
SUMMERY OF THE UTILITY MODEL
In order to overcome the problem that exists among the background art, the utility model discloses the extract need not artifical directly emit, just can flow into automatically and retrieve reation kettle and carry out the petroleum ether and retrieve as long as open the valve, has reduced manual operation intensity, and the petroleum ether conveying has all stopped inflammable gas in airtight space and has volatilized and guaranteed production safety, and the petroleum ether rate of recovery is risen by a wide margin, and manufacturing cost effectively descends, and sets up the promotion of heat exchanger recovery speed, and production efficiency obviously improves.
In order to overcome the problem that exists among the background art, for solving above-mentioned problem, the utility model discloses a following technical scheme realizes:
the device for preparing the clean oil comprises an extraction reaction kettle, a petroleum ether recovery reaction kettle, a solvent receiving tank, a first heat exchanger, a second heat exchanger, a third heat exchanger and a fourth heat exchanger, wherein the extraction reaction kettle is connected with the petroleum ether recovery reaction kettle through a pipeline, the extraction reaction kettle and the petroleum ether recovery reaction kettle are respectively connected with the first heat exchanger and the third heat exchanger through pipelines, the first heat exchanger and the third heat exchanger are respectively connected with the second heat exchanger and the fourth heat exchanger through pipelines, the second heat exchanger is connected to the extraction reaction kettle through a pipeline, and the fourth heat exchanger is connected with the solvent receiving tank through a pipeline.
Preferably, a pipeline sight glass and a valve are arranged on a pipeline connected between the extraction reaction kettle and the petroleum ether recovery reaction kettle.
The utility model has the advantages that:
the utility model discloses the extraction liquid need not artifical directly emit, just can flow into automatically and retrieve reation kettle and carry out petroleum ether and retrieve as long as open the valve, has reduced manual operation intensity, and the petroleum ether conveying has all stopped inflammable gas in airtight space and has volatilized and guaranteed production safety, and the petroleum ether rate of recovery obtains rising by a wide margin, and manufacturing cost effectively descends, and sets up the promotion of heat exchanger recovery speed, and production efficiency obviously improves.
Drawings
Fig. 1 is a schematic structural diagram of the present invention.
The reference numbers in the figures are: the method comprises the following steps of 1-extraction reaction kettle, 2-petroleum ether recovery reaction kettle, 3-solvent receiving tank, 4-first heat exchanger, 5-second heat exchanger, 6-pipeline, 7-pipeline sight glass, 8-valve, 9-third heat exchanger and 10-fourth heat exchanger.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention clearer, the following will explain in detail a preferred embodiment of the present invention with reference to the accompanying drawings to facilitate understanding of the skilled person.
As shown in fig. 1, the device for preparing clean oil comprises an extraction reaction kettle 1, a recovered petroleum ether reaction kettle 2, a solvent receiving tank 3, a first heat exchanger 4, a second heat exchanger 5, a third heat exchanger 9 and a fourth heat exchanger 10, wherein the extraction reaction kettle 1 is connected with the recovered petroleum ether reaction kettle 2 through a pipeline 6, the extraction reaction kettle 1 and the recovered petroleum ether reaction kettle 2 are respectively connected with the first heat exchanger 4 and the third heat exchanger 9 through the pipeline 6, the first heat exchanger 4 and the third heat exchanger 9 are respectively connected with the second heat exchanger 5 and the fourth heat exchanger 10 through the pipeline 6, the second heat exchanger 5 is connected with the extraction reaction kettle 1 through the pipeline 6, the fourth heat exchanger 10 is connected with the solvent receiving tank 3 through the pipeline 6, the first heat exchanger 4 and the third heat exchanger 9 both use circulating cooling water, the second heat exchanger 5 and the fourth heat exchanger 10 use chilled water, the installation height of the extraction reaction kettle 1 is larger than that of the recovery reaction kettle, and a discharge hole at the bottom of the kettle is higher than a feed hole at the top of the recovery reaction kettle.
Preferably, a pipeline sight glass 7 and a valve 8 are arranged on a pipeline 6 connected between the extraction reaction kettle 1 and the petroleum ether recovery reaction kettle 2, the extraction liquid in the extraction reaction kettle 1 can be controlled to flow into the petroleum ether recovery reaction kettle 2 by opening the valve 8, the pipeline sight glass 7 can observe the flow reaction condition of the extraction liquid in the pipeline 6 at any time, the production is monitored, and accidents in the production process are avoided.
The utility model discloses a working process: solvent in the extraction reation kettle 1 forms solvent steam through the evaporation and enters into inside 4 first heat exchangers and carry out primary cooling, later flow back to in the extraction reation kettle 1 after getting into the second heat exchanger 5 through pipeline 6 and cooling for be the extraction liquid in the extraction reation kettle 1, later open valve 8, the extraction liquid is from flowing in recovery petroleum ether reation kettle 2, solvent in the recovery petroleum ether reation kettle 2 forms solvent steam through the evaporation and enters into inside 9 third heat exchangers and carry out primary cooling, later flow to solvent receiving tank 3 after getting into fourth heat exchanger 10 through pipeline 6 and cooling and collect.
The utility model discloses the extraction liquid need not artifical directly emit, just can flow into automatically and retrieve reation kettle and carry out petroleum ether and retrieve as long as open the valve, has reduced manual operation intensity, and the petroleum ether conveying has all stopped inflammable gas in airtight space and has volatilized and guaranteed production safety, and the petroleum ether rate of recovery obtains rising by a wide margin, and manufacturing cost effectively descends, and sets up the promotion of heat exchanger recovery speed, and production efficiency obviously improves.
Finally, it is noted that the above-mentioned preferred embodiments illustrate rather than limit the invention, and that, although the invention has been described in detail with reference to the above-mentioned preferred embodiments, it will be understood by those skilled in the art that various changes in form and details may be made therein without departing from the scope of the invention as defined by the appended claims.
Claims (2)
1. An apparatus for producing an oil purifier, comprising: the device for preparing the clean oil comprises an extraction reaction kettle, a petroleum ether recovery reaction kettle, a solvent receiving tank, a first heat exchanger, a second heat exchanger, a third heat exchanger and a fourth heat exchanger, wherein the extraction reaction kettle is connected with the petroleum ether recovery reaction kettle through a pipeline, the extraction reaction kettle and the petroleum ether recovery reaction kettle are respectively connected with the first heat exchanger and the third heat exchanger through pipelines, the first heat exchanger and the third heat exchanger are respectively connected with the second heat exchanger and the fourth heat exchanger through pipelines, the second heat exchanger is connected to the extraction reaction kettle through a pipeline, and the fourth heat exchanger is connected with the solvent receiving tank through a pipeline.
2. The apparatus for preparing an oil purifier as defined in claim 1, wherein: and a pipeline sight glass and a valve are arranged on a pipeline connected between the extraction reaction kettle and the petroleum ether recovery reaction kettle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922129768.XU CN210367611U (en) | 2019-12-03 | 2019-12-03 | Device for preparing oil purifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922129768.XU CN210367611U (en) | 2019-12-03 | 2019-12-03 | Device for preparing oil purifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210367611U true CN210367611U (en) | 2020-04-21 |
Family
ID=70257739
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201922129768.XU Active CN210367611U (en) | 2019-12-03 | 2019-12-03 | Device for preparing oil purifier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN210367611U (en) |
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2019
- 2019-12-03 CN CN201922129768.XU patent/CN210367611U/en active Active
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| CP01 | Change in the name or title of a patent holder |
Address after: 653100 North West Road, Jiulong District, Yuxi hi tech Development Zone, Yunnan Patentee after: Yunnan Runyu Biotechnology Co., Ltd Address before: 653100 North West Road, Jiulong District, Yuxi hi tech Development Zone, Yunnan Patentee before: YUNNAN YUXI YUNXI FLAVOURS AND FRAGRANCES Co.,Ltd. |