CN201506783U - Refining castor oil dehydration device - Google Patents
Refining castor oil dehydration device Download PDFInfo
- Publication number
- CN201506783U CN201506783U CN2009202392045U CN200920239204U CN201506783U CN 201506783 U CN201506783 U CN 201506783U CN 2009202392045 U CN2009202392045 U CN 2009202392045U CN 200920239204 U CN200920239204 U CN 200920239204U CN 201506783 U CN201506783 U CN 201506783U
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- CN
- China
- Prior art keywords
- filler
- castor oil
- dehydration
- dehydration tower
- viscotrol
- 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.)
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Abstract
The utility model discloses a refining castor oil dehydration device which comprises a filler dehydration tower, a condenser communicated with the top of the filler dehydration tower and a receiving tank communicated with the bottom of the condenser; therefore, after a vacuum pump is opened, castor oil containing water released from a washing tank is pumped into the filler dehydration tower; a spray device and stainless steel mesh filler are arranged in the filler dehydration tower; the castor oil containing water is sprayed onto the filler, thereby increasing the gas-liquid contacting area, and strengthening the process in which the two phases gas and liquid are fully mixed and heated in the filler dehydration tower, and water vapor is evaporated; the water vapor enters the receiving tank through a condensing tube; the bottom of the filler dehydration tower is provided with conforming castor oil; and the conforming castor oil is pumped into a decolorization reactor, the vacuum pump works continuously, and the production is continuous. The refining castor oil dehydration device shortens the operation time, improves the product quality, realizes continuous dehydration operation, thereby the product quality is uniform and the enterprise benefit is increased.
Description
Technical field
The utility model relates to a kind of Chemicals equipment, relates in particular to a kind of refining Viscotrol C dewatering unit.
Background technology
Viscotrol C is refining to have had the history of decades at home, and existing process for refining roughly is included as operations such as pickling, alkali cleaning, washing, dehydration, decolouring, the Technology maturation, and each producer's equipment is similar, and working method is similar.
In the existing production operation, alkali cleaning, washing, three production links of dehydration have directly influenced the production cycle of refining Viscotrol C and the output of single device.Look the equipment volume difference, alkali cleaning, washing finish to leave standstill and carry out oily water separation, and the clear time of profit layering was generally 5～15 hours, and the dehydration procedure operation is generally the first normal pressure decompression dehydration then that dewaters.Tradition Viscotrol C dewatering process is: squeeze into the dehydration still from the moisture Viscotrol C that the washing still is emitted with pump, opening steam heats up, look the situation that steams that handleless cup is observed water from pipeline, when observing from looking the effusive water yield of handleless cup when fewer and feweri, the dehydration still vacuumizes under heating condition; When looking anhydrous the flowing down of handleless cup, continued to vacuumize 15 minutes, stop heating, the Viscotrol C that is up to the standards in the still that will dewater is then squeezed into the decolouring still.Moisture Viscotrol C finishes to dehydration from entering the dehydration still, generally needs more than ten hour, and the production cycle is long, produces discontinuous.Although later process adopts gac or activated decoloration, indexs such as outward appearance, free fatty acids, saponification value still are difficult to meet the demands.
The utility model content
Technical problem to be solved in the utility model provides the refining Viscotrol C dewatering unit that a kind of dewatering time is short, operate serialization.
For solving the problems of the technologies described above, the technical solution of the utility model is: refining Viscotrol C dewatering unit, it is characterized in that, comprise: the filler dehydration tower, described filler dehydration tower comprises tower body, the top of described tower body is provided with and washes the moisture Viscotrol C import that still is connected, the bottom of described tower body is provided with the outlet that is connected with the still that decolours, described tower body inside is provided with spray equipment and filler, described spray equipment is positioned at the top of tower body and is communicated with described moisture Viscotrol C import, and described filler is positioned at the middle and lower part of tower body; Condenser, described condenser is connected by the top of pipeline with described filler dehydration tower; Receiving tank, described receiving tank is connected with the bottom of condenser by pipeline.
As a kind of optimized technical scheme, described filler is the Stainless Steel Cloth filler.
After having adopted technique scheme, the beneficial effects of the utility model are: because this refining Viscotrol C dewatering unit comprises the filler dehydration tower, the condenser that is connected with the top of described filler dehydration tower, the receiving tank that is connected with described condenser bottom, so, after opening vacuum pump, with pump moisture Viscotrol C is squeezed in the filler dehydration tower, be provided with spray equipment and Stainless Steel Cloth filler in the described filler dehydration tower, described moisture Viscotrol C is sprayed on the filler, has increased the gas-liquid area that contacts, strengthened solution-air two-phase thorough mixing, after filler dehydration tower back warp was crossed heating, steam was evaporated, and described steam enters receiving tank through condenser, in filler dehydration tower bottom is qualified Viscotrol C, qualified Viscotrol C is drawn into the decolouring still and goes, vacuum pump commentariess on classics of not stopping transport, and production is carried out continuously.The utility model has shortened the operating time, and quality product improves, and has realized the dehydration operation serialization, and making uniform in quality has increased the performance of enterprises.
Description of drawings
Accompanying drawing is the structural representation of the utility model embodiment;
In the accompanying drawing: 1-filler dehydration tower; The moisture Viscotrol C import of 1a-; The 1b-spray equipment; The qualified Viscotrol C outlet of 1c-; 1d-Stainless Steel Cloth filler; The 2-condenser; The 3-receiving tank; The 4-toothed gear pump;
Embodiment
Refining Viscotrol C dewatering unit, as shown in drawings, comprise: filler dehydration tower 1, described filler dehydration tower 1 comprises tower body, the top of described tower body is provided with and washes the moisture Viscotrol C import 1a that still is connected, and the bottom of described tower body is provided with the qualified Viscotrol C outlet 1c that is connected with the still that decolours, and described tower body inside is provided with spray equipment 1b and filler, described spray equipment 1b is positioned at the top of tower body and is communicated with described moisture Viscotrol C import, and described filler is positioned at the middle and lower part of tower body; Condenser 2, described condenser 2 is connected by the top of pipeline with described filler dehydration tower 1; Receiving tank 3, described receiving tank 3 is connected by the bottom of pipeline with condenser 2.The utility model embodiment preferred filler is Stainless Steel Cloth filler 1d.Adopt steam or thermal oil to heat in the chuck of the tower body outer wall setting of described filler dehydration tower.
Principle of work of the present utility model: after opening vacuum pump, the moisture Viscotrol C of emitting from the washing still is driven into the filler filler dehydration tower 1, described moisture Viscotrol C sprays to Stainless Steel Cloth filler 1d through spray equipment 1b, described moisture Viscotrol C is covered with Stainless Steel Cloth filler 1d, heating heat-conducting oil in filler dehydration tower 1, moisture is by rapid evaporation, and the steam of evaporation is extracted to condenser 2, enters receiving tank 3 then; Qualified Viscotrol C is squeezed into decolouring still (perhaps middle vessel) by filler dehydration tower bottom by toothed gear pump 4, and dehydration is carried out continuously.The Stainless Steel Cloth filler 1d that adopts has increased the gas-liquid area that contacts, and has strengthened solution-air two-phase thorough mixing, and under heating state, moisture evaporation is rapid, and production efficiency improves, and produces to be able to serialization.
Aborning, adopt this refining Viscotrol C dewatering unit, make the production cycle shorten to 30 minutes by original about ten hours; The throughput of single device has improved four times; Refining Viscotrol C comprehensive energy consumption per ton reduces more than 10%; Quality product improves, and each quality index obviously is better than old technology; Realize the dehydration operate continuously, uniform in quality, quality index does not have big difference between each batch.
The foregoing description only is giving an example of the utility model embodiment; protection domain of the present utility model is as the criterion with the content of claim; any equivalent transformation that carries out based on technology enlightenment of the present utility model is also within protection domain of the present utility model.
Claims (2)
1. refining Viscotrol C dewatering unit is characterized in that, comprising:
The filler dehydration tower, described filler dehydration tower comprises tower body, the top of described tower body is provided with and washes the moisture Viscotrol C import that still is connected, the bottom of described tower body is provided with the outlet that is connected with the still that decolours, described tower body inside is provided with spray equipment and filler, described spray equipment is positioned at the top of tower body and is communicated with described moisture Viscotrol C import, and described filler is positioned at the middle and lower part of tower body;
Condenser, described condenser is connected by the top of pipeline with described filler dehydration tower;
Receiving tank, described receiving tank is connected with the bottom of condenser by pipeline.
2. refining Viscotrol C dewatering unit as claimed in claim 1 is characterized in that: described filler is the Stainless Steel Cloth filler.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202392045U CN201506783U (en) | 2009-09-28 | 2009-09-28 | Refining castor oil dehydration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202392045U CN201506783U (en) | 2009-09-28 | 2009-09-28 | Refining castor oil dehydration device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201506783U true CN201506783U (en) | 2010-06-16 |
Family
ID=42467912
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009202392045U Expired - Fee Related CN201506783U (en) | 2009-09-28 | 2009-09-28 | Refining castor oil dehydration device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201506783U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102311871A (en) * | 2011-08-08 | 2012-01-11 | 河南工业大学 | Sesame oil dehydration method and device |
| CN103627518A (en) * | 2013-09-12 | 2014-03-12 | 上海制皂(集团)如皋有限公司 | Castor oil dehydration system for soap making |
| CN110903894A (en) * | 2019-10-28 | 2020-03-24 | 陈赣平 | Castor cold oil extraction castor oil device |
| CN112745986A (en) * | 2020-12-15 | 2021-05-04 | 山东省科学院能源研究所 | Method and device for extracting essential oil by steam distillation |
-
2009
- 2009-09-28 CN CN2009202392045U patent/CN201506783U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102311871A (en) * | 2011-08-08 | 2012-01-11 | 河南工业大学 | Sesame oil dehydration method and device |
| CN103627518A (en) * | 2013-09-12 | 2014-03-12 | 上海制皂(集团)如皋有限公司 | Castor oil dehydration system for soap making |
| CN103627518B (en) * | 2013-09-12 | 2015-10-07 | 上海制皂(集团)如皋有限公司 | Soapmaking castor oil dewatering system |
| CN110903894A (en) * | 2019-10-28 | 2020-03-24 | 陈赣平 | Castor cold oil extraction castor oil device |
| CN112745986A (en) * | 2020-12-15 | 2021-05-04 | 山东省科学院能源研究所 | Method and device for extracting essential oil by steam distillation |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100616 Termination date: 20120928 |