CN204265725U - A kind of diffusion type steam walnut oil extraction element - Google Patents
A kind of diffusion type steam walnut oil extraction element Download PDFInfo
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- CN204265725U CN204265725U CN201420752154.1U CN201420752154U CN204265725U CN 204265725 U CN204265725 U CN 204265725U CN 201420752154 U CN201420752154 U CN 201420752154U CN 204265725 U CN204265725 U CN 204265725U
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- distillation bucket
- porous barrier
- emulsion tank
- extraction element
- diffusion type
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Abstract
The utility model discloses a kind of diffusion type steam walnut oil extraction element, comprise vapour generator, distillation bucket, emulsion tank, condenser and water-and-oil separator, described vapour generator, distillation bucket, emulsion tank, condenser and water-and-oil separator are connected in series by technical process priority pipeline, the top of described distillation bucket is provided with steam inlet, be provided with the movable feeding gate of minor axis and plate washer above distillation bucket, distillation bucket bottom is provided with the dump bottom of lower minor axis and button lobe; On the left of described emulsion tank, top is provided with opening for feed, and top is provided with agitator motor, is provided with stirring rake in emulsion tank, and agitator motor drives and connects stirring rake; The utility model shortens logical steaming time, and efficient energy-saving arranges active carbon layer on porous barrier, absorb the impurity in walnut raw material, make the walnut oil of production purer, taste is more perfect, make discharging soon, easily and thoroughly at the bottom of movable porous barrier and movable bucket, oil yield rate is high.
Description
Technical field
The utility model relates to a kind of extraction element, specifically a kind of diffusion type steam walnut oil extraction element.
Background technology
Walnut has the regal title of woody oleiferous plants, and walnut oil unsaturated fatty acid content is high, is senior edible nourishing oil.At present, it is milling process that walnut puies forward the most frequently used method of oil, and this method technique is simple, support equipment is few, production is flexible, but there is the oil yield of walnut kernel and comprehensive utilization ratio not high, especially walnut protein sex change is large, residual oil content is high, and recycle value is low waits shortcomings.And aqua method utilizes non-oil component in oil plant to the difference of oil and water avidity, utilize profit proportion different and the method grease and protein etc. separated simultaneously.This method processing condition are gentle, can obtain the lower albumen of sex change while carrying oil, and it, have simple, the safe and reliable and feature of economy compared with solvent extraction method.The steam of legacy equipment is from bottom to top advanced in distillation bucket, easily by the raw material of the wooden dregs of light weight and so in the gas flow the punching of heart portion fly four and fall apart, intermediate formation hole, surrounding raw material layer heap is thick, intermediate raw material layer is thinning, gage distortion, pyrolysis is insufficient, and hot gas flow from bottom to top, thermal convection is not obvious, and the utilization ratio of heat is low, cause pyrolysis insufficient further, the yield extracting grease is lower.Two is that discharge port is opened on the bucket sidewall of side on the shelf, and discharging speed is not slowly, very thoroughly and not too convenient.
Utility model content
The purpose of this utility model is to provide that a kind of discharging is fast, oil yield rate is high, and pyrolysis sufficient diffusion type steam walnut oil extraction element, to solve the problem proposed in above-mentioned background technology.
For achieving the above object, the utility model provides following technical scheme:
A kind of diffusion type steam walnut oil extraction element, comprise vapour generator, distillation bucket, emulsion tank, condenser and water-and-oil separator, described vapour generator, distillation bucket, emulsion tank, condenser and water-and-oil separator are connected in series by technical process priority pipeline, the top of described distillation bucket is provided with steam inlet, the movable feeding gate of minor axis and plate washer is provided with above distillation bucket, distillation bucket bottom is provided with the dump bottom of lower minor axis and button lobe, and there is gasket movable feeding gate and dump bottom surrounding; Be provided with porous barrier in described distillation bucket, porous barrier is movable porous barrier, and porous barrier side is with middle minor axis, and porous barrier opposite side is provided with movable fagging and crank, and the upper chamber in distillation bucket and lower chamber are equipped with the gas mixture air outlet of being with valve; On the left of described emulsion tank, top is provided with opening for feed, and top is provided with agitator motor, is provided with stirring rake in emulsion tank, and agitator motor drives and connects stirring rake.
Further, the plate face of described porous barrier is covered with active carbon layer.
Further, vaporizing coil is provided with in described condenser.
Further, described vaporizing coil is corrosion resistant metallic substance.
Further, finished pot is connected on the right side of described water-and-oil separator.
Compared with prior art, the utility model steam passes into from top to bottom, because there being the stop of porous barrier, can not go out hole, raw material layer thickness is evenly constant, and hot steam is sprayed from top to bottom, produce thermal convection, both all make pyrolysis even, can suitably shorten logical steaming time, energy-conservation, and raise the efficiency, porous barrier arranges active carbon layer, absorbs the impurity in walnut raw material, make the walnut oil of production purer, taste is more perfect; Make discharging soon, easily and thoroughly at the bottom of movable porous barrier and movable bucket, working efficiency is high, and oil yield rate improves greatly.
Accompanying drawing explanation
Fig. 1 is a kind of structural representation of diffusion type steam walnut oil extraction element.
Fig. 2 is the structural representation distilling bucket in a kind of diffusion type steam walnut oil extraction element.
In figure: 1-vapour generator, 2-distill bucket, 21-plate washer, the upper minor axis of 22-, 23-crank, 24-button lobe, 25-movable fagging, minor axis, 3-porous barrier, 4-active carbon layer, 5-emulsion tank, 51-opening for feed, 52-agitator motor, 53-stirring rake, 6-condenser, 61-vaporizing coil, 7-water-and-oil separator, 8-finished pot in minor axis, 27-under 26-.
Embodiment
Be described in more detail below in conjunction with the technical scheme of embodiment to this patent.
Refer to Fig. 1-2, a kind of diffusion type steam walnut oil extraction element, comprise vapour generator 1, distillation bucket 2, emulsion tank 5, condenser 6 and water-and-oil separator 7, described vapour generator 1, distillation bucket 2, emulsion tank 5, condenser 6 and water-and-oil separator 7 are connected in series by technical process priority pipeline, the top of described distillation bucket 2 is provided with steam inlet, the movable feeding gate of minor axis 22 and plate washer 21 is provided with above distillation bucket 2, distillation bucket 2 bottom is provided with the dump bottom of lower minor axis 26 and button lobe 24, and there is gasket movable feeding gate and dump bottom surrounding, porous barrier 3 is provided with in described distillation bucket 2, porous barrier 3 is movable porous barrier, porous barrier 3 side is with middle minor axis 27, and porous barrier 3 opposite side is provided with movable fagging 25 and crank 23, and the upper chamber in distillation bucket 2 and lower chamber are equipped with the gas mixture air outlet of being with valve, on the left of described emulsion tank 5, top is provided with opening for feed 51, and top is provided with agitator motor 52, is provided with stirring rake 53 in emulsion tank 5, and agitator motor 52 drives and connects stirring rake 53, during utility model works, first distillation bucket 2 base plate button lobe 24 is held on distillation bucket 2 sidewall, make to close up with distillation bucket 2 ladle body at the bottom of 2 barrels, distillation bucket, after porous barrier 3 is put level, with crank 23, fagging 25 is shaken to longitudinal direction by horizontal, withstand porous barrier 3, again the baffle plate 21 of this distillation bucket 2 end face is turned on, feeding gate is opened along upper rotating shaft 22 turns 75 °, by the porous barrier 3 in walnut raw material distillation bucket 2, then feeding gate is barred up, tighten baffle plate 21, after checking the connection of each pipeline and the opening and closing situation of valve, steam in vapour generator 1 is from top to bottom passed in distillation bucket 2, after distillation, the mixture flow of steam and grease enters emulsor 5 through respectively there being the pipeline up and down of Valve controlling, enter condenser 6 afterwards, then water-and-oil separator 7 is entered, walnut raw material after pyrolysis, only need open button lobe 24, base plate rotates 75 ° along lower minor axis 26 and opens, turn crank 23 again, make fagging 25 horizontal, porous barrier 3 side departs from support, middle minor axis 27 rotates 75 °, porous barrier 3 is sagging, the numerous and confused whereabouts of walnut raw material quarrel, thoroughly, fast, complete discharging easily, the utility model steam passes into from top to bottom, because there being the stop of porous barrier 3, can not go out hole, raw material layer thickness is evenly constant, and hot steam is sprayed from top to bottom, produces thermal convection, both all make pyrolysis even, can suitably shorten logical steaming time, energy-conservation, and raise the efficiency, porous barrier 3 arranges active carbon layer 4, absorb the impurity in walnut raw material, make the walnut oil of production purer, taste is more perfect, make discharging soon, easily and thoroughly at the bottom of movable porous barrier 3 and movable bucket, working efficiency is high, and oil yield rate improves greatly.
To those skilled in the art, obvious the utility model is not limited to the details of above-mentioned one exemplary embodiment, and when not deviating from spirit of the present utility model or essential characteristic, can realize the utility model in other specific forms.Therefore, no matter from which point, all should embodiment be regarded as exemplary, and be nonrestrictive, scope of the present utility model is limited by claims instead of above-mentioned explanation, and all changes be therefore intended in the implication of the equivalency by dropping on claim and scope are included in the utility model.Any Reference numeral in claim should be considered as the claim involved by limiting.
In addition, be to be understood that, although this specification sheets is described according to embodiment, but not each embodiment only comprises an independently technical scheme, this narrating mode of specification sheets is only for clarity sake, those skilled in the art should by specification sheets integrally, and the technical scheme in each embodiment also through appropriately combined, can form other embodiments that it will be appreciated by those skilled in the art that.
Claims (5)
1. a diffusion type steam walnut oil extraction element, it is characterized in that, comprise vapour generator (1), distillation bucket (2), emulsion tank (5), condenser (6) and water-and-oil separator (7), described vapour generator (1), distillation bucket (2), emulsion tank (5), condenser (6) and water-and-oil separator (7) are connected in series by technical process priority pipeline, the top of described distillation bucket (2) is provided with steam inlet, distillation bucket (2) top is provided with the movable feeding gate of minor axis (22) and plate washer (21), distillation bucket (2) bottom is provided with the dump bottom of lower minor axis (26) and button lobe (24), there is gasket movable feeding gate and dump bottom surrounding, porous barrier (3) is provided with in described distillation bucket (2), porous barrier (3) is movable porous barrier, porous barrier (3) side is with middle minor axis (27), porous barrier (3) opposite side is provided with movable fagging (25) and crank (23), and the upper chamber in distillation bucket (2) and lower chamber are equipped with the gas mixture air outlet of being with valve, top, described emulsion tank (5) left side is provided with opening for feed (51), top is provided with agitator motor (52), be provided with stirring rake (53) in emulsion tank (5), agitator motor (52) drives and connects stirring rake (53).
2. a kind of diffusion type steam walnut oil extraction element according to claim 1, is characterized in that, the plate face of described porous barrier (3) is covered with active carbon layer (4).
3. a kind of diffusion type steam walnut oil extraction element according to claim 1, is characterized in that, be provided with vaporizing coil (61) in described condenser (6).
4. a kind of diffusion type steam walnut oil extraction element according to claim 3, it is characterized in that, described vaporizing coil (61) is corrosion resistant metallic substance.
5. a kind of diffusion type steam walnut oil extraction element according to claim 1, is characterized in that, described water-and-oil separator (7) right side connects finished pot (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420752154.1U CN204265725U (en) | 2014-12-04 | 2014-12-04 | A kind of diffusion type steam walnut oil extraction element |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420752154.1U CN204265725U (en) | 2014-12-04 | 2014-12-04 | A kind of diffusion type steam walnut oil extraction element |
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| Publication Number | Publication Date |
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| CN204265725U true CN204265725U (en) | 2015-04-15 |
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| CN201420752154.1U Expired - Fee Related CN204265725U (en) | 2014-12-04 | 2014-12-04 | A kind of diffusion type steam walnut oil extraction element |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112011407A (en) * | 2020-09-21 | 2020-12-01 | 合肥蓝胖子生物技术有限公司 | Preparation and extraction process of dendrobium essential oil |
-
2014
- 2014-12-04 CN CN201420752154.1U patent/CN204265725U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112011407A (en) * | 2020-09-21 | 2020-12-01 | 合肥蓝胖子生物技术有限公司 | Preparation and extraction process of dendrobium essential oil |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150415 Termination date: 20161204 |