CN203639440U - Steam diffusion type cedar oil extracting device - Google Patents
Steam diffusion type cedar oil extracting device Download PDFInfo
- Publication number
- CN203639440U CN203639440U CN201320844833.7U CN201320844833U CN203639440U CN 203639440 U CN203639440 U CN 203639440U CN 201320844833 U CN201320844833 U CN 201320844833U CN 203639440 U CN203639440 U CN 203639440U
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- movable
- baffle plate
- steam
- extracting device
- diffusion type
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- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The utility model provides a steam diffusion type cedar oil extracting device. The steam diffusion type cedar oil extracting device is sequentially provided with a steam generator (1), a distillation barrel (2), a condenser (5) and an oil-water separator (6) which are connected in series by using pipelines according to the sequence of technological process, wherein the distillation barrel (2) is internally provided with a porous baffle plate (3), the upper part of the distillation barrel (2) is provided with a steam inlet and a movable feeding door with an upper short shaft (22) and a baffle plate (21), the lower part of the distillation barrel (2) is provided with a movable bottom with a lower short shaft (26) and a buttoned flap (24), sealing gaskets are arranged on the peripheries of the movable feeding door and the movable bottom, the porous baffle plate (3) is a movable porous baffle plate (3), one side of the porous baffle plate (3) is provided with a middle-short shaft (27), and a movable bracing plate (25) and a crank (23) are arranged below the baffle plate of the opposite side, and an upper air chamber and a lower air chamber are provided with mixed gas outlets with valves. The steam diffusion type cedar oil extracting device is used for extracting oil resin of cedarwood, weeping cypress and pines. The distillation barrel of the steam diffusion type cedar oil extracting device is improved in terms of spraying steam from top to bottom, collecting mixed gas of the upper air chamber and the lower air chamber, turning a bottom, discharging and the like, so that the effects of saving energy and labor hour, increasing yield, rapidly and completely discharging materials and the like are achieved.
Description
Technical field
The utility model relates to a kind of extraction element of timber grease, specifically uses the device of grease in hydrodistillation China fir, pine, cypress.
Background technology
" natural resin extracting process and device " patent application of open Liao Su state Mr. Jiang of CN101024754, by steam oven, distillation bucket, cooling tank with oily water separation bucket is in tandem forms, wherein most crucial parts are distillation bucket, this distillation bucket be designed with two point defects: the one, steam is from bottom to top advanced in distillation bucket, easily the raw material of sawdust of light weight and so on is flown to scatter in the punching of air-flow central part, intermediate formation hole, thick, the intermediate raw material layer attenuation of surrounding raw material layer heap, 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, further causes pyrolysis insufficient, and the yield of extracting grease is lower.The 2nd, discharge port is opened on the shelf on the bucket sidewall of side, and discharging speed is not slowly, very thoroughly and not too convenient.
Utility model content
The technical problems to be solved in the utility model is the angle from distillation bucket being carried out to texture improvement, and a kind of vapor diffusion formula oleum Cunninghamiae lanceolatae extraction element is provided.
Solve the problems of the technologies described above and adopt following technical scheme: this vapor diffusion formula oleum Cunninghamiae lanceolatae extraction element, there is successively vapour generator by the priority of technical process by pipeline serial connection, inside there is the distillation bucket of porous barrier, condenser and water-and-oil separator, steam inlet is arranged at the top of described distillation bucket, bring the movable feeding gate of minor axis and plate washer, the dump bottom of the lower minor axis of band and button lobe is arranged at bottom, there is gasket movable feeding gate and dump bottom surrounding, porous barrier is movable porous barrier, one side is with middle minor axis, under the dividing plate of offside, there are movable fagging and crank, upper chamber and lower chamber in distillation bucket all have the gas mixture air outlet with valve.
On the plate face of described movable porous barrier, be covered with gauze layer.
The beneficial effects of the utility model are that steam passes into from top to bottom, because there being stopping of porous barrier, can not go out hole, raw material layer even thickness is constant, and hot steam is sprayed from top to bottom, produces thermal convection, both all make pyrolysis even, can suitably shorten the logical steam time, energy-conservation, and improve yield 10%-15%; Movable porous barrier and the movable bucket end, make discharging fast, convenient and thorough, and work efficiency is high, and the gas mixture of upper and lower air chamber is all collected, and oil yield rate increases.
Brief description of the drawings
Accompanying drawing is the utility model structural representation.
Embodiment
The utility model is described in detail below in conjunction with embodiment and with reference to accompanying drawing: referring to accompanying drawing, this vapor diffusion formula oleum Cunninghamiae lanceolatae extraction element, there is successively vapour generator 1 by the priority of technical process by pipeline serial connection, inside there is the distillation bucket 2 of porous barrier 3, condenser 5 and water-and-oil separator 6, steam inlet is arranged at the top of described distillation bucket 2, bring the movable feeding gate of minor axis 22 and plate washer 21, the dump bottom of the lower minor axis 26 of band and button lobe 24 is arranged at bottom, there is gasket movable feeding gate and dump bottom surrounding, porous barrier 3 is movable porous barrier, one side is with middle minor axis 27, under the dividing plate of offside, there are movable fagging 25 and crank 23, upper chamber and lower chamber in distillation bucket all have the gas mixture air outlet with valve.
On the plate face of described porous barrier 3, be covered with gauze layer.
When use, first distillation barrel soleplate is held on barrel sidewall with button lobe 24, at the bottom of making barrel, close up with ladle body, porous barrier 3 is put after level, with crank 23 by fagging 25 by laterally shaking to longitudinally, withstand porous barrier 3, again the baffle plate 21 of these distillation bucket 2 end faces is turned on, feeding gate turns 90 ° and open along upper rotating shaft 22, China fir fragment or China fir sawdust 4 are placed in as raw material on porous barrier 3 in distillation bucket 2 or gauze, (sawdust particle diameter is little, on dividing plate, pad one deck gauze), then bar up feeding gate, tighten baffle plate 21, check after the connection of each pipeline and the switching situation of valve, steam in vapour generator is from top to bottom passed in distillation bucket 2, for time 0.5-1h, time increases along with the increase of raw material bed thickness, reduce along with reducing of raw material particle size (or sheet is thick), temperature 100-130 DEG C.After distillation, the mixed flow of steam and grease enters cooling tank 5 through the pipeline up and down that respectively has valve control, then enters water-and-oil separator 6, by just natural separation of the difference of proportion.Cedar sawdust after pyrolysis or sheet, only need open button lobe 24, and base plate is opened along 90 ° of lower minor axis rotations, turn crank 23 again, make fagging 25 horizontal, porous barrier one side departs from support, it is sagging that middle minor axis 27 rotates 90 ° of dividing plates, and the numerous and confused whereabouts of China fir quarrel, has completed discharging thoroughly, quickly and easily.In the upper and lower air chamber of distillation bucket, after thermal convection, all have gas mixture, therefore, 2 air chambers is equipped with the air outlet of gas mixture, controls the valve of these two air outlets, favourable abundant pyrolysis.
This device need be pressed design customization except distillation bucket, and all the other all can by amount of finish or output size, select suitable specification, net purchase or commercially available acquisition.
Claims (2)
1. a vapor diffusion formula oleum Cunninghamiae lanceolatae extraction element, there is successively vapour generator (1) by the priority of technical process by pipeline serial connection, inside there is the distillation bucket (2) of porous barrier (3), condenser (5) and water-and-oil separator (6), steam inlet is arranged at the top that it is characterized in that described distillation bucket (2), bring the movable feeding gate of minor axis (22) and plate washer (21), the dump bottom of the lower minor axis (26) of band and button lobe (24) is arranged at bottom, there is gasket movable feeding gate and dump bottom surrounding, porous barrier (3) is movable porous barrier, one side is with middle minor axis (27), under the dividing plate of offside, there are movable fagging (25) and crank (23), upper chamber and lower chamber in distillation bucket all have the gas mixture air outlet with valve.
2. vapor diffusion formula oleum Cunninghamiae lanceolatae extraction element as claimed in claim 1, is covered with gauze layer on the plate face of the movable porous barrier (3) described in it is characterized in that.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320844833.7U CN203639440U (en) | 2013-12-19 | 2013-12-19 | Steam diffusion type cedar oil extracting device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320844833.7U CN203639440U (en) | 2013-12-19 | 2013-12-19 | Steam diffusion type cedar oil extracting device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203639440U true CN203639440U (en) | 2014-06-11 |
Family
ID=50870702
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320844833.7U Expired - Fee Related CN203639440U (en) | 2013-12-19 | 2013-12-19 | Steam diffusion type cedar oil extracting device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203639440U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104498193A (en) * | 2014-12-19 | 2015-04-08 | 王卓贤 | Plant essential oil and concentrated solution production line |
| CN104498194A (en) * | 2014-12-30 | 2015-04-08 | 王卓贤 | Steam autoclave pot |
| WO2016061903A1 (en) * | 2014-10-24 | 2016-04-28 | 王卓贤 | Automatic plant essential oil extract production equipment |
-
2013
- 2013-12-19 CN CN201320844833.7U patent/CN203639440U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2016061903A1 (en) * | 2014-10-24 | 2016-04-28 | 王卓贤 | Automatic plant essential oil extract production equipment |
| CN104498193A (en) * | 2014-12-19 | 2015-04-08 | 王卓贤 | Plant essential oil and concentrated solution production line |
| CN104498194A (en) * | 2014-12-30 | 2015-04-08 | 王卓贤 | Steam autoclave pot |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140611 Termination date: 20141219 |
|
| EXPY | Termination of patent right or utility model |