CN205152181U - A oil -water separator for producing rose hydrosol - Google Patents
A oil -water separator for producing rose hydrosol Download PDFInfo
- Publication number
- CN205152181U CN205152181U CN201520950907.4U CN201520950907U CN205152181U CN 205152181 U CN205152181 U CN 205152181U CN 201520950907 U CN201520950907 U CN 201520950907U CN 205152181 U CN205152181 U CN 205152181U
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- pipe
- separating tank
- hydrosol
- knockout drum
- drainer
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Abstract
The utility model discloses an oil -water separator for producing rose hydrosol, including drainer and knockout drum, the drainer top has connect steam to advance the pipe, pass through duct connections between drainer and the knockout drum, a knockout drum side joint has temperature control device, is equipped with temperature sensor in the knockout drum, the electricity even between temperature sensor and the temperature control device, the knockout drum top has met smart oil pipe, essential oil jar of smart oil pipe other end connection, draw -off pump has still been met on the smart oil pipe, the knockout drum bottom has connect pure dew pipe and compounding pipe, a pure dew jar is connected to the other end of pure dew pipe, is equipped with pure dew ooff valve on the pure dew pipe, a compounding holding vessel is connected to the other end of compounding pipe, is equipped with the compounding ooff valve on the compounding pipe, one side of knockout drum still is equipped with evacuating device. The utility model discloses water oil separating is respond well to practice thrift the process of production, improved the efficiency of production greatly.
Description
Technical field
The utility model belongs to rose production unit technical field, is specifically related to a kind of oily-water seperating equipment for the production of rose.
Background technology
Rose is pure rose extracting solution, does not mix up any essence, wetting Agent for Printing Inks, sanitas etc., is real natural product, so, gentle especially safety.What comprise inside rose is the volatile aromatic composition of a large amount of fresh rose flower, and these fragrance ingredients divide into 2 parts, and water-fast part is exactly Flos Rosae Rugosae quintessence oil, and the part being dissolved in water is exactly rose.It is simultaneously containing macromolecular fragrance ingredient, composition is also complicated especially, nearly kind more than 300, mainly contain alcohol, aldehyde, acid, ester, ether, Deng, these compositions all play the effect of oneself uniqueness, so, rose has comprehensive counterbalance effect, for neutral skin, skin gloss can be strengthened, to oily skin, Tea Tree Essential Oil is secreted, to dry skin, can keep the skin wet rapidly, to sensitive skin, red blood streak can be eliminated, desensitising, to the dim skin of sallow, skin vitality can be strengthened, the people of nearly all skin quality can use rose, embody outstanding cosmetic result.
In the process of producing rose, all the azeotrope being obtained oil and water by distillation mostly, by by azeotrope through oily water separation, thus obtain hydrosol and essential oil, but existing oily-water seperating equipment, be separated not thorough in sepn process, need through distillation repeatedly, refrigerated separation, reach the object be separated completely, add the operation of separation, greatly reduce the efficiency of production.
Utility model content
Technical problem to be solved in the utility model is for above-mentioned the deficiencies in the prior art, a kind of oily-water seperating equipment for the production of rose is provided, its structure is simple, reasonable in design, effectively can carry out being separated of essential oil and hydrosol, substantially increase the efficiency of separation.
The technical scheme that the utility model adopts is: a kind of oily-water seperating equipment for the production of rose, comprise drainer and separating tank, described drainer top is connected to steam inlet tube, described drainer is connected by transfer lime with between separating tank, the discharge end of described transfer lime is positioned at the middle part of separating tank, transfer lime is provided with conveying switch-valve, described separating tank side is connected to temperature control unit, temperature sensor is provided with in separating tank, be electrically connected between described temperature sensor and temperature control unit, described separating tank top is connected to essential oil pipe, essential oil pipe one end is stretched in separating tank, and be positioned at the middle and upper part of separating tank, the other end connects an essential oil tank, described essential oil pipe is also connected to extraction pump, hydrosol pipe and mixing tube is connected to bottom described separating tank, one end of described hydrosol pipe is communicated with bottom separating tank, the other end connects a hydrosol tank, hydrosol pipe is provided with hydrosol switch-valve, one end of described mixing tube is communicated with bottom separating tank, the other end connects a batch mixing hold-up vessel, mixing tube is provided with batch mixing switch-valve, the side of described separating tank is also provided with vacuum extractor.
As preferably, described hydrosol pipe and mixing tube are provided with under meter.
As preferably, described temperature control unit is also connected to a timing register.
The beneficial effects of the utility model are: the utility model structure is simple, reasonable in design, by the steam after distillation is passed through condensation, after forming water of condensation, carry out low temperature, low pressure is separated, and isolated essential oil is discharged respectively by different pipelines from hydrosol simultaneously, finally unsegregated water of condensation is entered in batch mixing hold-up vessel, after collection some amount, re-starting distillation, condensation and be separated, saving the operation of producing, substantially increased the efficiency of production.
Accompanying drawing explanation
Fig. 1 is the utility model structural representation.
In figure: 1, drainer; 2, separating tank; 3, steam inlet tube; 4, transfer lime; 5, switch-valve is carried; 6, temperature control unit; 7, temperature sensor; 8, essential oil pipe; 9, essential oil tank; 10, extraction pump; 11, hydrosol pipe; 12, mixing tube; 13, hydrosol tank; 14, hydrosol switch-valve; 15, batch mixing hold-up vessel; 16, batch mixing switch-valve; 17, vacuum extractor.
Embodiment
Below in conjunction with the accompanying drawings and the specific embodiments the utility model is described in further detail.
Embodiment 1: as shown in Figure 1, the utility model comprises drainer 1 and separating tank 2, described drainer 1 top is connected to steam inlet tube 3, described drainer 1 is connected by transfer lime 4 with between separating tank 2, the discharge end of described transfer lime 4 is positioned at the middle part of separating tank 2, transfer lime 4 is provided with conveying switch-valve 5, described separating tank 2 side is connected to temperature control unit 6, temperature sensor 7 is provided with in separating tank 2, be electrically connected between described temperature sensor 7 and temperature control unit 6, described separating tank 2 top is connected to essential oil pipe 8, essential oil pipe 8 one end is stretched in separating tank 2, and be positioned at the middle and upper part of separating tank 2, the other end connects an essential oil tank 9, described essential oil pipe 8 is also connected to extraction pump 10, hydrosol pipe 11 and mixing tube 12 is connected to bottom described separating tank 2, one end of described hydrosol pipe 11 is communicated with bottom separating tank 2, the other end connects a hydrosol tank 13, hydrosol pipe 11 is provided with hydrosol switch-valve 14, one end of described mixing tube 12 is communicated with bottom separating tank 2, the other end connects a batch mixing hold-up vessel 15, mixing tube 12 is provided with batch mixing switch-valve 16, the side of described separating tank 2 is also provided with vacuum extractor 17.
Embodiment 2: identical with above-described embodiment 1, wherein above-mentioned hydrosol pipe 11 and mixing tube 12 are provided with under meter.
Embodiment 3: identical with above-described embodiment 1, wherein above-mentioned temperature control unit 6 is also connected to a timing register.
To be entered in drainer 1 by steam inlet tube 3 and carry out condensation by distilling the steam that obtains and obtain water of condensation, water of condensation is sent in separating tank 2 by transfer lime 4, start temperature control unit 6 and vacuum extractor 17, lower the temperature and step-down in separating tank 2, after maintaining low temperature certain hour, being separated appears in the profit in water of condensation, essential oil is positioned at upper strata, hydrosol is positioned at lower floor, by extraction pump 10, store in essential oil suction essential oil tank 9, open hydrosol switch-valve 14, hydrosol is delivered in hydrosol tank 13, when opening hydrosol switch-valve 14, close batch mixing switch-valve 16, after essential oil and hydrosol are collected, close hydrosol switch-valve 14 and extraction pump 10, open batch mixing switch-valve 16, batch mixing is sent in batch mixing hold-up vessel 15 and collect, to be stored a certain amount of after, concentrate and carry out re-distillation, condensation be separated.
The utility model structure is simple, reasonable in design, by the steam after distillation is passed through condensation, after forming water of condensation, carry out low temperature, low pressure is separated, and isolated essential oil is discharged respectively by different pipelines from hydrosol simultaneously, finally unsegregated water of condensation is entered in batch mixing hold-up vessel 15, after collection some amount, re-starting distillation, condensation and be separated, saving the operation of producing, substantially increased the efficiency of production.
Claims (3)
1. the oily-water seperating equipment for the production of rose, it is characterized in that: comprise drainer (1) and separating tank (2), described drainer (1) top is connected to steam inlet tube (3), be connected by transfer lime (4) between described drainer (1) with separating tank (2), the discharge end of described transfer lime (4) is positioned at the middle part of separating tank (2), transfer lime (4) is provided with conveying switch-valve (5), described separating tank (2) side is connected to temperature control unit (6), temperature sensor (7) is provided with in separating tank (2), be electrically connected between described temperature sensor (7) and temperature control unit (6), described separating tank (2) top is connected to essential oil pipe (8), essential oil pipe (8) one end is stretched in separating tank (2), and be positioned at the middle and upper part of separating tank (2), the other end connects an essential oil tank (9), described essential oil pipe (8) is also connected to extraction pump (10), described separating tank (2) bottom is connected to hydrosol pipe (11) and mixing tube (12), one end of described hydrosol pipe (11) is communicated with separating tank (2) bottom, the other end connects a hydrosol tank (13), hydrosol pipe (11) is provided with hydrosol switch-valve (14), one end of described mixing tube (12) is communicated with separating tank (2) bottom, the other end connects a batch mixing hold-up vessel (15), mixing tube (12) is provided with batch mixing switch-valve (16), the side of described separating tank (2) is also provided with vacuum extractor (17).
2. a kind of oily-water seperating equipment for the production of rose according to claim 1, is characterized in that: described hydrosol pipe (11) and mixing tube (12) are provided with under meter.
3. a kind of oily-water seperating equipment for the production of rose according to claim 1, is characterized in that: described temperature control unit (6) is also connected to a timing register.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520950907.4U CN205152181U (en) | 2015-11-25 | 2015-11-25 | A oil -water separator for producing rose hydrosol |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520950907.4U CN205152181U (en) | 2015-11-25 | 2015-11-25 | A oil -water separator for producing rose hydrosol |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205152181U true CN205152181U (en) | 2016-04-13 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520950907.4U Active CN205152181U (en) | 2015-11-25 | 2015-11-25 | A oil -water separator for producing rose hydrosol |
Country Status (1)
| Country | Link |
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| CN (1) | CN205152181U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106190577A (en) * | 2016-08-12 | 2016-12-07 | 四川省盛祥玫瑰生态农业开发有限公司 | A kind of preparation method of MEIGUI CHUNLU |
| CN106315495A (en) * | 2016-09-12 | 2017-01-11 | 西安安森智能仪器股份有限公司 | Intelligent oil water pumping draining system |
-
2015
- 2015-11-25 CN CN201520950907.4U patent/CN205152181U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106190577A (en) * | 2016-08-12 | 2016-12-07 | 四川省盛祥玫瑰生态农业开发有限公司 | A kind of preparation method of MEIGUI CHUNLU |
| CN106315495A (en) * | 2016-09-12 | 2017-01-11 | 西安安森智能仪器股份有限公司 | Intelligent oil water pumping draining system |
| CN106315495B (en) * | 2016-09-12 | 2019-01-15 | 西安安森智能仪器股份有限公司 | A kind of grease intelligence evacuation system |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |