CN203079936U - Laboratory-scale deodorization system - Google Patents
Laboratory-scale deodorization system Download PDFInfo
- Publication number
- CN203079936U CN203079936U CN 201220743417 CN201220743417U CN203079936U CN 203079936 U CN203079936 U CN 203079936U CN 201220743417 CN201220743417 CN 201220743417 CN 201220743417 U CN201220743417 U CN 201220743417U CN 203079936 U CN203079936 U CN 203079936U
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- Prior art keywords
- retort
- strainer
- experiment type
- deodoration system
- vacuum pump
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Abstract
The utility model relates to a laboratory-scale deodorization system. The system comprises a reaction tank, a heater, a filter, a filter pump and a vacuum pump, wherein the reaction tank is internally provided with a cooling coil and a steam injection pipe, wherein the heater is connected below the reaction tank; and the filter is connected with an outlet of the reaction tank through a pipeline, the filter pump is arranged on the pipeline arranged between the reaction tank and the filter, and the vacuum pump is connected with the reaction tank. Compared with the prior art, the laboratory-scale deodorization system provided by the utility model has the advantages that the structure is compact, the volume is small, the operation is convenient, a deodorization effect is good, in addition, nutrient components of grease are not damaged, and the quality of an end product is guaranteed.
Description
Technical field
The utility model relates to a kind of deodoration system, especially relates to a kind of experiment type deodoration system.
Background technology
In edible fat production, crude oil is through the materials such as oxide compound of the aldehydes that comes unstuck, depickling and decolouring also contain a certain amount of lipid acid and trace after handling, ketone, hydro carbons, glyceryl ester, the existence of these materials causes grease to have " stink ", grease deodorization is the important procedure in the concise production, be to utilize that there is very big-difference in volatility between malodor components and the triglyceride level, under the high temperature high vacuum condition, malodor components is removed by the wet distillation principle.
Plant wet goods material is carried out the de-odorised production unit, be widely used in industries such as grease processing, it is that the container of hundreds of liters heats that existing deodorization equipment is put into capacity with material, and volume is all huger, the operation more complicated, and application is not suitable for experimentizing.
Chinese patent CN101942358B discloses the dry and cold vacuum deodorization method and apparatus of a kind of grease, its method can remove greasy stink preferably under the situation that significantly reduces the energy and steam consumption, but its equipment is comparatively complicated, and inconvenient operation, and the de-odorised program is comparatively loaded down with trivial details.
The utility model content
The purpose of this utility model be exactly provide in order to overcome the defective that above-mentioned prior art exists a kind of simple in structure, compact, volume is little, the experiment type deodoration system of easy to operate, good deodorization effect.
The purpose of this utility model can be achieved through the following technical solutions:
A kind of experiment type deodoration system, this system comprises retort, well heater, strainer, filtration pump and vacuum pump, be provided with cooling worm and steam-jet siphon in the described retort, described well heater is connected the below of retort, described strainer is connected with the outlet of retort by pipeline, described filtration pump is located on the pipeline between retort and the strainer, and described vacuum pump is connected with retort.
All stretch out outside the retort at the two ends of described cooling worm, feeds water coolant in the described cooling worm.
Be positioned at the outer cooling worm of retort and be provided with ball valve and under meter, regulate flooding quantity by under meter material is cooled off.
One end of described steam-jet siphon is positioned at the centre of retort, and the other end is connected with the vapour source in the external world.
The steam-jet siphon that is positioned at the retort outside is provided with relief valve and tensimeter.
The upper end of described retort offers opening for feed, and the top of retort is provided with vacuum meter.
Be provided with condenser between described vacuum pump and the retort, condenser is located at the ingress of vacuum pump, and the hot gas that enters vacuum pump is cooled off, and keeps low temperature, and vacuum pump is played a protective role.
Described strainer is the pressurization leaf filter.
Pipeline between described retort and the strainer is provided with ball valve, and the filter outlet pipeline is provided with ball valve.
At first, well heater heats the material in the retort and dewaters, and steam enters in the retort by steam-jet siphon material is carried out the high temperature deodorizing, then, vacuum pump provides negative pressure for retort, extract the steam in the material, the stink that vapor zone in the material is discharged from vacuum pump, reaches the de-odorised effect, at last, cooling worm is that the material after the high temperature deodorizing cools off, and cooled material enters strainer by filtration pump, filters the back discharging through filter.
Compared with prior art, the utility model can be realized industrialized all demands, but do not need as production structure in the industry and operate all equipment of more complicated, the utility model compact construction, volume is little, and is easy to operate, and deodorizing effect is good, greasy nutritive ingredient can be do not destroyed in addition, the quality of finished product can be guaranteed.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
Among the figure, 1 is retort, and 2 is vacuum meter, and 3 is cooling worm, 4 is steam-jet siphon, and 5 is tensimeter, and 6 is strainer, and 7 is filtration pump, 8 is temperature sensor, and 9 is well heater, and 10 is under meter, 11 is ball valve, 12 vacuum pumps, and 13 is condenser, 14 is relief valve, and A is the material charging, and B is the material discharging, C is water inlet, and D is water outlet, and E is a steam.
Embodiment
Below in conjunction with the drawings and specific embodiments the utility model is elaborated.
Embodiment
A kind of experiment type deodoration system, as shown in Figure 1, this system comprises retort 1, well heater 9, strainer 6, filtration pump 7 and vacuum pump 12, be provided with cooling worm 3 and steam-jet siphon 4 in the retort 1, well heater 9 is connected the below of retort 1, strainer 6 is connected by the outlet of pipeline with retort 1, and filtration pump 7 is located on the pipeline between retort 1 and the strainer 6, and vacuum pump 12 is connected with retort 1.All stretch out outside the retort 1 at the two ends of cooling worm 3, feeds water coolant in the cooling worm 3, and water coolant water inlet C flows into from the lower end of cooling worm 3, and cooling water outlet D flows out from the upper end of cooling worm 3.Be positioned at retort 1 outer cooling worm 3 and be provided with ball valve 11 and under meter 10, regulate flooding quantity by under meter 10 material is cooled off.One end of steam-jet siphon 4 is positioned at the centre of retort 1, and the other end is connected with the vapour source in the external world.The steam-jet siphon 4 that is positioned at retort 1 outside is provided with relief valve 14 and tensimeter 5.The upper end of retort 1 offers opening for feed, and the top of retort 1 is provided with vacuum meter 2, and the lower end of retort 1 is provided with temperature sensor 8.Be provided with condenser 13 between vacuum pump 12 and the retort 1, condenser 13 is located at the ingress of vacuum pump 12, and the hot gas that enters vacuum pump 12 is cooled off, and keeps low temperature, and vacuum pump 12 is played a protective role.Strainer 6 is the pressurization leaf filter.Pipeline between retort 1 and the strainer 6 is provided with ball valve 11, and strainer 6 export pipelines are provided with ball valve 11.
At first, material charging A enters in the retort 1 by opening for feed, material in 9 pairs of retort of well heater 1 heats and dewaters, steam E enters in the retort 1 by steam-jet siphon 4 material is carried out the high temperature deodorizing, then, vacuum pump 12 provides negative pressure for retort 1, extract the steam E in the material, steam E discharges from vacuum pump 12 with the stink in the material, reaches the de-odorised effect, and is last, cooling worm 3 cools off for the material after the high temperature deodorizing, cooled material enters strainer 6 by filtration pump 7, and after filtering through filter 6, material discharging B flows out from strainer 6.
Claims (9)
1. experiment type deodoration system, it is characterized in that, this system comprises retort, well heater, strainer, filtration pump and vacuum pump, be provided with cooling worm and steam-jet siphon in the described retort, described well heater is connected the below of retort, described strainer is connected with the outlet of retort by pipeline, and described filtration pump is located on the pipeline between retort and the strainer, and described vacuum pump is connected with retort.
2. a kind of experiment type deodoration system according to claim 1 is characterized in that the two ends of described cooling worm are all stretched out outside the retort, feeds water coolant in the described cooling worm.
3. a kind of experiment type deodoration system according to claim 2 is characterized in that, is positioned at the outer cooling worm of retort and is provided with ball valve and under meter.
4. a kind of experiment type deodoration system according to claim 1 is characterized in that an end of described steam-jet siphon is positioned at the centre of retort, and the other end is connected with the vapour source in the external world.
5. a kind of experiment type deodoration system according to claim 4 is characterized in that, the steam-jet siphon that is positioned at the retort outside is provided with relief valve and tensimeter.
6. a kind of experiment type deodoration system according to claim 1 is characterized in that the upper end of described retort offers opening for feed, and the top of retort is provided with vacuum meter.
7. a kind of experiment type deodoration system according to claim 1 is characterized in that, is provided with condenser between described vacuum pump and the retort.
8. a kind of experiment type deodoration system according to claim 1 is characterized in that, described strainer is the pressurization leaf filter.
9. a kind of experiment type deodoration system according to claim 1 is characterized in that the pipeline between described retort and the strainer is provided with ball valve, and the filter outlet pipeline is provided with ball valve.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201220743417 CN203079936U (en) | 2012-12-30 | 2012-12-30 | Laboratory-scale deodorization system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201220743417 CN203079936U (en) | 2012-12-30 | 2012-12-30 | Laboratory-scale deodorization system |
Publications (1)
Publication Number | Publication Date |
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CN203079936U true CN203079936U (en) | 2013-07-24 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN 201220743417 Expired - Lifetime CN203079936U (en) | 2012-12-30 | 2012-12-30 | Laboratory-scale deodorization system |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108570352A (en) * | 2018-05-23 | 2018-09-25 | 阜阳市长海环保设备科技有限公司 | A kind of oil refining device of energy-saving and environment-friendly efficient swill oil vacuum dehydration impurity elimination taste removal |
CN109055017A (en) * | 2018-05-23 | 2018-12-21 | 阜阳市长海环保设备科技有限公司 | Multi-functional trench oil purification oil refining device |
-
2012
- 2012-12-30 CN CN 201220743417 patent/CN203079936U/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108570352A (en) * | 2018-05-23 | 2018-09-25 | 阜阳市长海环保设备科技有限公司 | A kind of oil refining device of energy-saving and environment-friendly efficient swill oil vacuum dehydration impurity elimination taste removal |
CN109055017A (en) * | 2018-05-23 | 2018-12-21 | 阜阳市长海环保设备科技有限公司 | Multi-functional trench oil purification oil refining device |
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Legal Events
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CX01 | Expiry of patent term | ||
CX01 | Expiry of patent term |
Granted publication date: 20130724 |