CN205759844U - Extraction element - Google Patents
Extraction element Download PDFInfo
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- CN205759844U CN205759844U CN201620497905.9U CN201620497905U CN205759844U CN 205759844 U CN205759844 U CN 205759844U CN 201620497905 U CN201620497905 U CN 201620497905U CN 205759844 U CN205759844 U CN 205759844U
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- chamber
- extraction
- tank body
- temperature control
- extraction element
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Abstract
The utility model discloses a kind of extraction element, this extraction element includes that extraction pot, described extraction pot include tank body and the extraction chamber being located in tank body；Described tank body be double-decker and its in be provided with temperature control chamber, described temperature control intracavity is filled with conduction oil, and the bottom of described tank body is provided with and is provided with for connecting temperature control chamber and the oil-out of heat-conducting medium collection device with the top of the oil-in of heater and described tank body for connecting temperature control chamber；The top of described tank body is provided with dog-house；Being inserted with distillation tube on described tank body, one end of described distillation tube is positioned at more than the liquid level of extraction chamber, and its other end extends extraction chamber and is connected with material collecting device；Being provided with conveying screw rod in described extraction chamber, the upper end of described conveying screw rod is fixed on dog-house, is provided with crushing chamber in described conveying screw rod, is provided with the blade for pressing materials in described crushing chamber, has the effect improving natural product dissolution velocity.
Description
Technical field
This utility model relates to natural product extraction separation field, particularly to extraction element.
Background technology
The extract of most natural products has special physiological potency, can be used as medicine, spice and dyestuff.The separation of natural product, purify and identify to be a field the most active in organic chemistry.There is a unique and abundant natural Chinese medicine resource in China, thus to the separation of Effective Component of Chinese Medicine with study particularly significant.
The Chinese patent that application publication number is CN103877744A, Shen Qing Publication day is on June 25th, 2014 discloses a kind of Herba Dendrobii extracts active ingredients mechanism, there is the extraction pot of dog-house including top, described extraction pot sidewall is provided with steam jacket, the inside of extraction pot is provided with tool mesh having openings therein, a mozzle it is additionally provided with in extraction pot, described mozzle one end extends to below screen cloth, and the other end extends outside extraction pot.
During utilizing the effective ingredient in solvent extraction natural product, after natural product contacts with solvent, natural product dissolves and needs the regular hour in a solvent, and natural product dissolves speed in a solvent and affects the extraction efficiency of effective ingredient, does not improves this in prior art.
Utility model content
The purpose of this utility model is to provide a kind of extraction element, which solves the problem that natural product dissolution velocity is slow, has the effect improving natural product dissolution velocity.
Above-mentioned technical purpose of the present utility model has the technical scheme that
A kind of extraction element, including extraction pot, described extraction pot includes tank body and the extraction chamber being located in tank body；Described tank body be double-decker and its in be provided with temperature control chamber, described temperature control intracavity is filled with conduction oil, and the bottom of described tank body is provided with and is provided with for connecting temperature control chamber and the oil-out of heat-conducting medium collection device with the top of the oil-in of heater and described tank body for connecting temperature control chamber；The top of described tank body is provided with dog-house；Being inserted with distillation tube on described tank body, one end of described distillation tube is positioned at more than the liquid level of extraction chamber, and its other end extends extraction chamber and is connected with material collecting device；Being provided with conveying screw rod in described extraction chamber, the upper end of described conveying screw rod is fixed on dog-house, is provided with crushing chamber in described conveying screw rod, is provided with the blade for pressing materials in described crushing chamber.
Use said structure, material in conveying screw rod transport to extraction chamber, on the one hand the probability that material generation solution splashes when feeding intake is little, on the other hand in course of conveying, oarse-grained material can be crushed to little granule (specific surface area is little) body by material extruding mutually between adjacent blade, between blade and the inwall of conveying screw rod, the solid that specific surface area is little can more touch solvent, so effective ingredient can be the most instant to solvent, reduce the impact on effective ingredient dissolution velocity of the raw material primary particle size；It addition, be combined with pyrogenous mode, except the dissolving of effective ingredient can be accelerated, its meltage also can be increased.
More preferably: the pitch of adjacent described blade is gradually reduced from the direction of the bottom of dog-house to tank body.
Use said structure, can progressively be pressed further by crushing by first granule, not only will not destroy blade but also material can be crushed to little granule as far as possible, can guarantee that the material before entering extraction chamber has been small particles material, avoid the large granular materials injury to conveying screw rod further, the effect of pulverizing can also be promoted, obtain homogeneous superfine micropowder.
More preferably: the pitch of adjacent described blade reduces from the direction equimultiple of the bottom of dog-house to tank body.
Use said structure, can progressively be pressed further by crushing by first granule, not only will not destroy blade but also material can be crushed to little granule as far as possible, moreover it is possible to the advance that guarantee material is ordered in conveying screw rod, be conducive to controlling being normally carried out of conveying.
More preferably: the thickness of adjacent described blade is gradually reduced from the direction of the bottom of dog-house to tank body.
Material particles formerly is relatively large, and it extrudes with the blade that thickness is relatively large, and the extruding force that the blade that thickness is big can bear is big, and bulky grain physical impact can be become finely ground particle substance by it；Posterior material particles diminishes relatively, and it extrudes with the blade that thickness is relatively small, and material is not only extruded by the relatively small blade of thickness also to be sheared, and improves the degree of attrition crushing granule.Use said structure, both will not injure blade, moreover it is possible to improve crushing efficiency further.
More preferably: the lower end of described conveying screw rod is stretched into liquid level and arranged.
Using said structure, on the one hand can reduce the situation that material occurs when the system of entrance to splash, on the other hand material contacts in time with solution, increases material dissolution speed further.
More preferably: described material collecting device includes that collecting box, described collecting box include casing and the collecting chamber being located in casing；Described casing be double-decker and its in be provided with cooling chamber, being filled with cooling water in described cooling chamber, the bottom of described casing is provided with and is provided with for connecting cooling chamber and the outlet of cooling medium collection device with the top of the water inlet of chiller and described casing for connecting cooling chamber.
Using said structure, collecting box can be collected fraction and be cooled down by fraction, the fraction multi_layer extraction in collecting chamber after collecting, and obtains the extract that purity is high.
More preferably: the distillation tube one end stretching into collecting chamber setting is positioned at the bottom of collecting chamber.
Use said structure, gas-liquid is coexisted or the fraction of pure gas is placed in the bottom of collecting chamber, so that gas first stretches in solution and absorbed by solution or motion makes gas be cooled to liquid from the bottom up, improve the collecting effect of fraction further.
More preferably: the bottom of described casing is connected with discharge nozzle, one end of described discharge nozzle is connected with material collecting barrel；Described discharge nozzle is tee T, and it connects setting with collecting chamber, extraction chamber and material collecting barrel respectively.
Use said structure, liquid after condensed is layered in collecting chamber, the material of light specific gravity effective ingredient such as (generally) volatile oil in the natural product bank of tubes that separates through top goes out and again distills utilization in discharge nozzle enters back into extraction chamber than heavy material (major part for natural product in the material such as water), during recycle Extraction solvent, economic and environment-friendly.
More preferably: in the described distillation tube that extraction chamber is arranged, be provided with filter course.
Use said structure, the solid powder of splashing can be stopped, improve the purity of the fraction entered in distillation tube.
In sum, this utility model has the advantages that
During use, opening fixture block, put into by material on breach, material is delivered in the extraction chamber of conduction oil temperature control through conveying screw rod, and in course of conveying, material is the most crushed；Material after pulverizing enters in extraction chamber, its specific surface area is big, can be rapidly dissolved in high-temperature solvent, at high temperature system starts distillation, gas enters in distillation tube to after filter course filters solid slag, gas condenses in distillation inner air tube tentatively condenses and enter the collecting chamber of cooled water control temperature further, liquid after condensed is layered in collecting chamber, the material of light specific gravity effective ingredient such as (generally) volatile oil in the natural product bank of tubes that separates through top goes out and again distills utilization in discharge nozzle enters back into extraction chamber than heavy material (major part for natural product in the material such as water), during recycle Extraction solvent, economic and environment-friendly.
Accompanying drawing explanation
Fig. 1 is the structural representation of embodiment 1；
Fig. 2 is the A portion enlarged drawing of Fig. 1.
In figure, 1, extraction pot；101, tank body；102, extraction chamber；2, temperature control chamber；3, oil-in；4, oil-out；5, conveying motor；6, conveying screw rod；7, breach；8, crushing chamber；9, blade；10, fixture block；11, stirring motor；12, air vent is extracted；13, stirring paddle；14, regulation pipe；15, distillation tube；16, filter course；17, collecting box；1701, casing；1702, collecting chamber；18, cooling chamber；19, water inlet；20, outlet；21, air vent；22, pipe is separated；23, discharge nozzle.
Detailed description of the invention
Below in conjunction with accompanying drawing, this utility model is described in further detail.
This specific embodiment is only to explanation of the present utility model; it is not to restriction of the present utility model; the present embodiment can be made after reading this specification by those skilled in the art as required does not has the amendment of creative contribution, but as long as all being protected by Patent Law in right of the present utility model.
Embodiment 1: extraction element, as shown in Figure 1-2.
With reference to Fig. 1, this extraction element includes extraction pot 1, and this extraction pot 1 includes tank body 101 and the extraction chamber 102 being located in tank body 101.This tank body 101 is in double-decker, and is provided with temperature control chamber 2 in interlayer.The top of oil-in 3 and temperature control chamber 2 that the bottom in temperature control chamber 2 is communicated with temperature control chamber 2 and heater (not shown) is communicated with temperature control chamber 2 and the oil-out 4 of heat-conducting medium collection device (not shown), by oil-in 3, conduction oil is packed in temperature control chamber 2, the conduction oil to temperature control chamber 2 be charged to oil-out 4 after again in oil-out 4 drains into heat-conducting medium collection device.
With reference to Fig. 1, the top of tank body 101 is provided with dog-house, and this dog-house is inserted with the conveying screw rod 6 controlled through conveying motor 5.The upper end of conveying screw rod 6 is fixed on dog-house, and its other end straight down and stretches into liquid level setting.Material is in the breach 7 of conveying screw rod 6 upper end enters the crushing chamber 8 of conveying screw rod 6, and the material in crushing chamber 8 is gradually pulverized under the extruding of blade 9.Being connected with matched fixture block 10 on breach 7, fixture block 10 can be used for opening and closing breach 7.From dog-house to the direction of the bottom of tank body 101 on, the pitch equimultiple of adjacent blade 9 reduces and the thickness of adjacent blade 9 is gradually reduced.
With reference to Fig. 1, the top of tank body 101 is provided with stirring motor 11, extracts air vent 12 and connected entrance.It is connected with on stirring motor 11 and stretches into the stirring paddle 13 that liquid level is arranged.The bottom of tank body 101 is provided with regulation pipe 14.
In conjunction with Fig. 1 and Fig. 2, connected entrance is connected with distillation tube 15 and connected entrance is provided with filter course 16.One end of distillation tube 15 is positioned at more than the liquid level of extraction chamber 102, and its other end extends extraction chamber 102 and is connected with collecting box 17.
With reference to Fig. 1, collecting box 17 includes casing 1701 and the collecting chamber 1702 being located in casing 1701.Distillation tube 15 one end stretching into collecting chamber 1702 setting is positioned at the bottom of collecting chamber 1702.This casing 1701 is in double-decker, and is provided with cooling chamber 18 in interlayer.The top of water inlet 19 and casing 1701 that the bottom of casing 1701 is communicated with cooling chamber 18 and chiller (not shown) is communicated with cooling chamber 18 and the outlet 20 of cooling medium collection device (not shown), by water inlet 19, cooling water is packed in cooling chamber 18, the cooling water to cooling chamber 18 be charged to outlet 20 after again in outlet 20 drains into cooling medium collection device.
With reference to Fig. 1, the top of casing 1701 is provided with collection air vent 21 and separates pipe 22, separates pipe 22 and stretches into distillation tube 15 one end that collecting chamber 1702 arranges and be positioned at the top of collecting chamber 1702.
With reference to Fig. 1, the bottom of casing 1701 is provided with discharge nozzle 23, and discharge nozzle 23 is in tee T, and it connects setting with collecting chamber 1702, extraction chamber 102 and material collecting barrel (not shown) respectively, and is equipped with valve on pipeline.
During use, opening fixture block 10, put into by material on breach 7, material is delivered in the extraction chamber 102 of conduction oil temperature control through conveying screw rod 6, and in course of conveying, material is the most crushed；Material after pulverizing enters in extraction chamber 102, its specific surface area is big, can be rapidly dissolved in high-temperature solvent, at high temperature system starts distillation, gas enters in distillation tube 15 to after filter course 16 filters solid slag, gas air in distillation tube 15 condenses in tentatively condensing and enter the collecting chamber 1702 of cooled water control temperature further, liquid after condensed is layered in collecting chamber 1702, the material of light specific gravity effective ingredient such as (generally) volatile oil in the natural product pipe 22 that separates through top is discharged and is again distilled utilization in discharge nozzle 23 enters back into extraction chamber 102 than heavy material (major part for natural product in the material such as water), during recycle Extraction solvent, economic and environment-friendly.
Claims (9)
1. an extraction element, including extraction pot (1), described extraction pot (1) includes tank body (101) and the extraction chamber (102) being located in tank body (101)；Described tank body (101) is provided with temperature control chamber (2) in double-decker and in it, being filled with conduction oil in described temperature control chamber (2), the bottom of described tank body (101) is provided with and is provided with the oil-out (4) for connecting temperature control chamber (2) and heat-conducting medium collection device with the top of the oil-in of heater (3) and described tank body (101) for connecting temperature control chamber (2)；The top of described tank body (101) is provided with dog-house；It is characterized in that, described tank body (101) is inserted with distillation tube (15), and one end of described distillation tube (15) is positioned at more than the liquid level of extraction chamber (102), and its other end extends extraction chamber (102) and is connected with material collecting device；Being provided with conveying screw rod (6) in described extraction chamber (102), the upper end of described conveying screw rod (6) is fixed on dog-house, is provided with crushing chamber (8) in described conveying screw rod (6), is provided with the blade (9) for pressing materials in described crushing chamber (8).
Extraction element the most according to claim 1, it is characterised in that the pitch of adjacent described blade (9) is gradually reduced from the direction of the bottom of dog-house to tank body (101).
Extraction element the most according to claim 1, it is characterised in that the pitch of adjacent described blade (9) reduces from the direction equimultiple of the bottom of dog-house to tank body (101).
Extraction element the most according to claim 1, it is characterised in that the thickness of adjacent described blade (9) is gradually reduced from the direction of the bottom of dog-house to tank body (101).
Extraction element the most according to claim 1, it is characterised in that the lower end of described conveying screw rod (6) is stretched into liquid level and arranged.
Extraction element the most according to claim 1, it is characterised in that described material collecting device includes that collecting box (17), described collecting box (17) include casing (1701) and the collecting chamber (1702) being located in casing (1701)；Described casing (1701) is provided with cooling chamber (18) in double-decker and in it, being filled with cooling water in described cooling chamber (18), the bottom of described casing (1701) is provided with and is provided with the outlet (20) for connecting cooling chamber (18) and cooling medium collection device with the top of the water inlet of chiller (19) and described casing (1701) for connecting cooling chamber (18).
Extraction element the most according to claim 6, it is characterised in that stretch into distillation tube (15) one end that collecting chamber (1702) arranges and be positioned at the bottom of collecting chamber (1702).
Extraction element the most according to claim 7, it is characterised in that the bottom of described casing (1701) is connected with discharge nozzle (23), one end of described discharge nozzle (23) is connected with material collecting barrel；Described discharge nozzle (23) is in tee T, and it connects setting with collecting chamber (1702), extraction chamber (102) and material collecting barrel respectively.
Extraction element the most according to claim 1, it is characterised in that be provided with filter course (16) in the described distillation tube (15) that extraction chamber (102) is arranged.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620497905.9U CN205759844U (en) | 2016-05-26 | 2016-05-26 | Extraction element |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620497905.9U CN205759844U (en) | 2016-05-26 | 2016-05-26 | Extraction element |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205759844U true CN205759844U (en) | 2016-12-07 |
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ID=57407276
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620497905.9U Expired - Fee Related CN205759844U (en) | 2016-05-26 | 2016-05-26 | Extraction element |
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| Country | Link |
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| CN (1) | CN205759844U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106867828A (en) * | 2017-04-24 | 2017-06-20 | 贵州省仁怀市茅台镇永泰酒业股份有限公司 | A kind of Quick production method of Chinese chestnut wine |
| CN107775835A (en) * | 2017-12-11 | 2018-03-09 | 洛阳乐森石化新材料有限公司 | A kind of polymer stirring and dissolving device |
| CN108465267A (en) * | 2018-06-12 | 2018-08-31 | 倪菁菁 | A kind of pharmaceutical purpose supercritical extracting equipment |
| WO2019041887A1 (en) * | 2017-08-31 | 2019-03-07 | 山东江天生物科技有限公司 | High-performance extraction device |
-
2016
- 2016-05-26 CN CN201620497905.9U patent/CN205759844U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106867828A (en) * | 2017-04-24 | 2017-06-20 | 贵州省仁怀市茅台镇永泰酒业股份有限公司 | A kind of Quick production method of Chinese chestnut wine |
| WO2019041887A1 (en) * | 2017-08-31 | 2019-03-07 | 山东江天生物科技有限公司 | High-performance extraction device |
| CN107775835A (en) * | 2017-12-11 | 2018-03-09 | 洛阳乐森石化新材料有限公司 | A kind of polymer stirring and dissolving device |
| CN108465267A (en) * | 2018-06-12 | 2018-08-31 | 倪菁菁 | A kind of pharmaceutical purpose supercritical extracting equipment |
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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: 20161207 Termination date: 20200526 |
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| CF01 | Termination of patent right due to non-payment of annual fee |