CN203033965U - Extrusion discharging extraction tank for natural perfume - Google Patents
Extrusion discharging extraction tank for natural perfume Download PDFInfo
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- CN203033965U CN203033965U CN 201220691297 CN201220691297U CN203033965U CN 203033965 U CN203033965 U CN 203033965U CN 201220691297 CN201220691297 CN 201220691297 CN 201220691297 U CN201220691297 U CN 201220691297U CN 203033965 U CN203033965 U CN 203033965U
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- natural perfume
- control valve
- communicated
- extruding
- storage part
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Abstract
An extrusion discharging extraction tank for natural perfume is provided with a tank body, an extrusion mechanism, an upper pipe system and a lower pipe system. The tank body is provided with a storage part and a sedimentation part which are communicated with each other. The upper pipe system is communicated with the storage part. The extrusion mechanism is arranged on the lower portion of the sedimentation part, the sedimentation part is communicated with an input end of the extrusion mechanism, an output end of the extrusion mechanism is communicated with the lower pipe system, the storage part is a cylinder, and the sedimentation part is a cone. The extrusion discharging extraction tank is further provided with an upper control valve and a lower control valve, the upper control valve is arranged on the upper pipe system, and the lower control valve is arranged on the lower pipe system. The extrusion discharging extraction tank for the natural perfume can improve raw material utilization rate, can guarantee clarity of the perfume, is simple to operate and can improve yield and efficiency of the natural perfume.
Description
Technical field
The utility model relates to natural perfume extractive technique field, particularly relates to a kind of natural perfume extruding and discharging formula extractor.
Background technology
Natural perfume refers to that with vegeto-animal fragrant position be raw material, the aromatoising substance that utilizes physical method such as wet distillation, lixiviate, squeezing etc. from natural matter, to separate, its form often is essential oil, medicinal extract, absolute oil, balm, tincture etc., as rose oil, jasmine concrete, vanilla tincture, white orchid face cream, tell Shandong resinoid, narcissus absolute oil etc.
Natural perfume is derived from natural with it, each effective constituent eurythmy, characteristics such as green, environmental protection, safety, effect are obvious, its effect will be more and more important in the formation of product core technology, especially smell perfume (or spice) and sense of taste improving product, construct taste and the style aspect of product uniqueness, act on more obvious.
At present, the extractor of natural perfume mostly is the shape that right cylinder adds tapered bottom.The right cylinder bottom, tapered bottom top has discharge pipe; Tapered bottom has air pressure valve.In the discharging link, the clear liquid on top flows out from discharge pipe earlier, and tapered bottom can be opened automatically then, and the plant slag charge after the extraction is discharged.And these plant slag charges are attached with a lot of extracting solutions usually, cause the spices productive rate low, especially for those expensive plant materials, have bigger economic waste especially.
Therefore, at the prior art deficiency, provide the high natural perfume extruding and discharging formula extractor of a kind of productive rate very necessary to overcome the prior art deficiency.
Summary of the invention
The purpose of this utility model is to avoid the deficiencies in the prior art part and a kind of natural perfume extruding and discharging formula extractor is provided, and adopts this natural perfume extruding and discharging formula extractor to carry out the spices extraction and has the high characteristics of productive rate.
The purpose of this utility model realizes by following technical measures.
A kind of natural perfume extruding and discharging formula extractor is provided with tank body, pressing mechanism, last tubing system, following tubing system, goes up control valve and following control valve;
Described tank body is provided with storage part and the precipitation portion that is interconnected, and described upper conduit system is communicated with described storage part;
Described pressing mechanism is arranged at the bottom of described precipitation portion, and described precipitation portion is communicated with the input terminus of described pressing mechanism, and the output terminal of described pressing mechanism is communicated with described tubing system down;
The described control valve of going up is arranged at described upper conduit system, and described control valve down is arranged at described tubing system down.
OnState storage part and be set to right cylinder.
Above-mentioned precipitation portion is set to cone.
The output terminal of above-mentioned upper conduit system converges with the described output terminal of tubing system down and is communicated with.
A kind of natural perfume extruding and discharging formula extractor of the present utility model is provided with tank body, pressing mechanism, goes up tubing system and following tubing system; Described tank body is provided with storage part and the precipitation portion that is interconnected, and described upper conduit system is communicated with described storage part; Described pressing mechanism is arranged at the bottom of described precipitation portion, and described precipitation portion is communicated with the input terminus of described pressing mechanism, and the output terminal of described pressing mechanism is communicated with described tubing system down.When this natural perfume extruding and discharging formula extractor extracts discharging then to spices, earlier the clear liquid of storage part is discharged by the upper conduit system and collect, and then with the sedimentation liquid of precipitation portion by the pressing mechanism extrusion process, the clear liquid that obtains by extrusion process passes through tubing system discharge collection down, and the while waste residue passes through the slag-drip opening of pressing mechanism and discharges.This natural perfume extruding and discharging formula extractor can effectively be used the slag charge of precipitation portion, can improve raw material availability, and can guarantee the clarity of spices.Have simple to operate and can improve productive rate and the efficient of natural perfume.
Description of drawings
Utilize accompanying drawing that the utility model is further described, but the content in the accompanying drawing does not constitute any restriction of the present utility model.
Fig. 1 is the structural representation of a kind of natural perfume extruding and discharging of the utility model formula extractor.
In Fig. 1, comprising:
Following tubing system 400,
Following control valve 410.
Embodiment
With the following Examples the utility model is further described.
Embodiment 1.
A kind of natural perfume extruding and discharging formula extractor as shown in Figure 1, is provided with tank body 100, pressing mechanism 200, last tubing system 300, following tubing system 400, goes up control valve 310 and following control valve 410.
Following control valve 410 is arranged at down tubing system 400.The output terminal of last tubing system 300 converges with the output terminal of following tubing system 400 and is communicated with.
This its principle of work of natural perfume extruding and discharging formula extractor is: extract in tank body 100 natural perfume processing back, and storage part 110 is clear liquid, and precipitation portion 120 is sedimentation liquid.Open control valve 310 earlier, the clear liquid in the storage part 110 is discharged by last tubing system 300 and is collected, and after the clear liquid of storage part 110 has been arranged, closes and closes control valve 310.Open down control valve 410 then, and open pressing mechanism 200, the clear liquid that the sedimentation liquid in the precipitation portion 120 obtains after extruding is from tubing system 400 discharges down, and pressing mechanism 200 also carries out automatic sludge discharge.This natural perfume extruding and discharging formula extractor can effectively be used the precipitated liquid of precipitation portion 120, can improve raw material availability, and can guarantee the clarity of spices.Have characteristics simple to operate, can improve productive rate and the efficient of natural perfume.
This natural perfume extruding and discharging formula extractor is applied to the natural perfume production plant; storage tank and extrusion technique are linked together; realize the integrated of the extruding of natural perfume product and discharging; simplify procedures; improve the clarity of natural perfume the finished product; save the labor force, improved productive rate and the efficient of the autonomous natural perfume of mass-producing greatly, have important practical significance.
Embodiment 2.
Adopt natural perfume extruding and discharging formula extractor of the present utility model that chamomile extract 1005 is extracted the back discharging, be positioned at sedimentation liquid discharging after pushing of the precipitation portion 120 of tank body 100.The productive rate of qualities of stevia extract 1005 is 72% ± 10%, be 58% ± 10% and do not use the productive rate of the qualities of stevia extract 1005 of this natural perfume extruding and discharging formula extractor, as seen, can make qualities of stevia extract 1005 productive rates improve 24% by this natural perfume extruding and discharging formula extractor.
Wherein, qualities of stevia extract 1005 adopts following prepared to form.Choose 200 kilograms of sweet Stevia, carry out drying treatment.Sweet Stevia after the drying treatment is inserted in 1800 kilogram of 80% ethanol, be heated to 70 degrees centigrade and keep carrying out in three hours extracting the first time, collect extracting solution for the first time.Add 1800 kilogram of 80% ethanol again, be heated to 70 degrees centigrade, keep carrying out in two hours extracting the second time, collect extracting solution for the second time.Adopt 200 eye mesh screen filtered while hot, merge first, second time filtrate and directly carry out enrichment process.Being concentrated into relative density (20 ℃) is 1.1481 ± 0.0080, after carry out the sedimentation operation.
Sedimentation 16-24 hour again, detect relative density (20 ℃) and be 1. 1481 ± 0.0080, refractive index (20 ℃) is 1.3841 ± 0.0080, acid number is indexs such as 8.54 ± 2.0, qualified back dress storage barrel stores.
Store 10-15 days again, detect relative density (20 ℃) and be 1.1481 ± 0.0080, refractive index (20 ℃) is 1. 3841 ± 0.0080, acid number is indexs such as 8.54 ± 2.0, warehousing after passing.
Carrying out discharging by natural perfume extruding and discharging formula extractor of the present utility model collects.
From present embodiment as can be seen; the utility model has been realized the integrated of the extruding of natural perfume product and discharging; simplify procedures; improve the clarity of natural perfume the finished product; save the labor force; improved productive rate and the efficient of the autonomous natural perfume of mass-producing greatly, had important practical significance.
Embodiment 3.
Adopt natural perfume extruding and discharging formula extractor of the present utility model that almond tincture 1055 is stored the back discharging, be positioned at sedimentation liquid discharging after pushing of the precipitation portion 120 of tank body 100.The productive rate of almond tincture 1055 is 920% ± 10%, is 750% ± 10% and do not use the productive rate of the almond tincture 1055 of this natural perfume extruding and discharging formula extractor, and productive rate improves 23%.
Wherein, almond tincture 1055 adopts following prepared to form.Choose 500 kilograms of almonds, the stoning section.
Adopt 3500 kilogram of 66% alcohol at normal temperature to extract.Detecting relative density (20 ℃) after the discharging is 0.9210 ± 0.0080, and refractive index (20 ℃) is 1.3617 ± 0.0080, and acid number is index such as 0.07 ± 2.0, pack into after qualified storage barrel and warehouse-in.Carrying out discharging by natural perfume extruding and discharging formula extractor of the present utility model collects.
From present embodiment as can be seen; the utility model has been realized the integrated of the extruding of natural perfume product and discharging; simplify procedures; improve the clarity of natural perfume the finished product; save the labor force; improved productive rate and the efficient of the autonomous natural perfume of mass-producing greatly, had important practical significance.
Should be noted that at last; above embodiment is only in order to the technical solution of the utility model to be described but not to the restriction of the utility model protection domain; although with reference to preferred embodiment the utility model has been done detailed description; those of ordinary skill in the art is to be understood that; can make amendment or be equal to replacement the technical solution of the utility model, and not break away from essence and the scope of technical solutions of the utility model.
Claims (4)
1. a natural perfume extruding and discharging formula extractor is characterized in that: be provided with tank body, pressing mechanism, last tubing system, following tubing system, go up control valve and following control valve;
Described tank body is provided with storage part and the precipitation portion that is interconnected, and described upper conduit system is communicated with described storage part;
Described pressing mechanism is arranged at the bottom of described precipitation portion, and described precipitation portion is communicated with the input terminus of described pressing mechanism, and the output terminal of described pressing mechanism is communicated with described tubing system down;
The described control valve of going up is arranged at described upper conduit system, and described control valve down is arranged at described tubing system down.
2. natural perfume extruding and discharging formula extractor according to claim 1, it is characterized in that: described storage part is set to right cylinder.
3. natural perfume extruding and discharging formula extractor according to claim 1 is characterized in that: described precipitation portion is set to cone.
4. natural perfume extruding and discharging formula extractor according to claim 1 is characterized in that: the output terminal of described upper conduit system converges with the described output terminal of tubing system down and is communicated with.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220691297 CN203033965U (en) | 2012-12-14 | 2012-12-14 | Extrusion discharging extraction tank for natural perfume |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220691297 CN203033965U (en) | 2012-12-14 | 2012-12-14 | Extrusion discharging extraction tank for natural perfume |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203033965U true CN203033965U (en) | 2013-07-03 |
Family
ID=48686102
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220691297 Expired - Fee Related CN203033965U (en) | 2012-12-14 | 2012-12-14 | Extrusion discharging extraction tank for natural perfume |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203033965U (en) |
-
2012
- 2012-12-14 CN CN 201220691297 patent/CN203033965U/en not_active Expired - Fee Related
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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: 20130703 Termination date: 20131214 |