CN203886231U - Nicotine sulfate extraction device - Google Patents
Nicotine sulfate extraction device Download PDFInfo
- Publication number
- CN203886231U CN203886231U CN201420300784.5U CN201420300784U CN203886231U CN 203886231 U CN203886231 U CN 203886231U CN 201420300784 U CN201420300784 U CN 201420300784U CN 203886231 U CN203886231 U CN 203886231U
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- extraction
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Abstract
The utility model discloses a nicotine sulfate extraction device. The nicotine sulfate extraction device comprises an extraction tank, a discharging opening, a discharging valve, a liquid outlet, a feeding opening, a gas outlet and a stirrer, wherein the extraction tank is internally provided with a filtering barrel; the filtering barrel is used for dividing the extraction tank into a collection chamber and a filtering reaction chamber. The tank is internally provided with the filtering barrel; after materials enter the filtering reaction chamber, oil and water are vertically and downwards fed through an annular spraying pipe; the materials can be uniformly stirred and mixed under the effect of the stirrer so that the permeation of a solvent to the materials is effectively enhanced; the extraction of active ingredients of the materials is complete and the extraction rate is high; the utilization amount of the solvent is effectively reduced; meanwhile, the filtering area of the filtering barrel is large so that extraction liquid can rapidly pass through the filtering barrel to enter the collection chamber, and furthermore, the filtering speed is effectively increased, the filtering efficiency is improved to the greatest extent, the materials are unlikely to be blocked, the filtering effect is good and the materials are smooth to discharge; the nicotine sulfate extraction device is simple in structure and is easy to popularize and use.
Description
Technical field
The utility model belongs to tobacco product extraction equipment technical field, is specifically related to a kind of nicotine sulphate leaching device.
Background technology
At present, a lot of areas of China are all plantation tobacco, in the tobacco leaf of the annual results of tobacco grower, most of qualified tobacco leaf is directly sold tobacco company, but tobacco leaf inferior all can be left major part every year, can not buy, can not burn, again can not as fertilizer sources, simultaneously, the tobacco rod that also has some, also because can not get reasonably utilizing the waste by vain, after testing, in tobacco leaf and tobacco rod, contain 1～5% nicotine, it is nicotine, nicotine is the important component part of smoking deterent and environmental type pesticide, pharmaceutically also having been widely used, it is treatment senile dementia, Parkinson is whole, the active drug of depression, therefore, extraction nicotine from these discarded tobaccos and tobacco rod, these discarded tobaccos and tobacco rod are reasonably utilized, turning waste into wealth is a large problem of current tobacco business research.And at present, the leaching device of conventional extraction nicotine is mainly by the charging aperture on pot for solvent extraction and pot for solvent extraction, discharging opening, water inlet, oil-in, the filter screen of agitating device and discharging opening, adopt this device extraction nicotine, mainly there is the problem of the following aspects: 1. water inlet and oil-in flow down along tank skin, solid accumulation is in tank, only depend on the agitating device can not be fully by material and water, oil is uniformly mixed fully, can not reach the object of abundant immersion, various effective elements in material are extracted fully, not only recovery rate is low, and the solvent needing is also more, 2. because the slag liquid separation in tank body only depends on the screen pack of slag notch to complete, not only filter area is little, the weak effect of filtration, and also screen pack easily stops up, and extract flowed out and have some setbacks, and the time of filtration is long, the efficiency of final impact extraction.Therefore, develop a kind of simple in structure, good filtration effect, recovery rate is high, efficiency is high, can be desirability with the nicotine sulphate leaching device that less solvent is produced higher concentration leachate.
Summary of the invention
A kind of simple in structure, good filtration effect of the purpose of this utility model, recovery rate are high, and efficiency is high, can produce with less solvent the nicotine sulphate leaching device of higher concentration leachate.
The purpose of this utility model is to realize like this, comprise pot for solvent extraction, discharge gate, blow-off valve, liquid outlet, be arranged on the charging aperture on pot for solvent extraction top cover, gas outlet and mixer, in pot for solvent extraction, be provided with filter cylinder, filter cylinder is divided into pot for solvent extraction collecting chamber and filters reative cell, filter in reative cell and be provided with heater, filter cylinder is by upper cone, cylinder and lower cone form, lower cone is fixed on the pot for solvent extraction base plate of discharge gate top, the middle and lower part of cylinder and lower cone are the structure with the circular arc web plate composition of sieve aperture, two-layer circular spray tube is installed on the inwall of upper cone, upper strata circular spray tube is connected with water inlet, lower floor's circular spray tube is connected with oil groove by oil-in, the shower nozzle outlet of circular spray tube is installed vertically downward.
The utility model by arranging filter cylinder in tank, material enters and filters after reative cell, the You Heshui feeding by circular spray tube feeds vertically downward, under the effect of mixer, can be uniformly mixed, effectively increased the infiltration of solvent to material, make the extraction of material active ingredient more complete, recovery rate is higher, and effectively reduce the consumption of solvent, simultaneously, the filter area of the screen pack of filter cylinder is larger, leachate after extracting can be entered in collecting chamber by filter cylinder fast, effectively raise the speed of filtration, farthest improved the efficiency of filtering, and be difficult for putty, good filtration effect, discharge is smooth and easy, simple in structure, be easy to promote the use of.
Accompanying drawing explanation
Fig. 1 is the utility model overall structure schematic diagram;
In figure: 1-discharge gate, 2-blow-off valve, 3 collecting chambers, 4-pot for solvent extraction, 5-cylinder, 6-asbestos heat-insulation layer, 7-filter cylinder, 8-upper cone, 9-shower nozzle, 10-water inlet, 11-charging aperture, 12-visor, 13-circular spray tube, 14-oil groove, 15-oil-in, 16-overfall, 17-heater, 18-mixer, 19-liquid outlet, 20-lower cone, 21-filters reative cell.
The specific embodiment
Below in conjunction with accompanying drawing, the utility model is further described, but never in any form the utility model is limited, any change or the improvement based on the utility model training centre, done, all belong to protection domain of the present utility model.
As shown in Figure 1, the utility model comprises pot for solvent extraction 4, discharge gate 1, blow-off valve 2, liquid outlet 19, be arranged on the charging aperture 11 on pot for solvent extraction 4 top covers, gas outlet and mixer 18, in pot for solvent extraction 4, be provided with filter cylinder 7, filter cylinder 7 is divided into pot for solvent extraction 4 collecting chamber 3 and filters reative cell 21, filter in reative cell 21 and be provided with heater 17, filter cylinder 7 is by upper cone 8, cylinder 5 and lower cone 20 form, lower cone 20 is fixed on pot for solvent extraction 4 base plates of discharge gate 1 top, the middle and lower part of cylinder 5 and lower cone 8 are the structure with the circular arc web plate composition of sieve aperture, two-layer circular spray tube 13 is installed on the inwall of upper cone 8, upper strata circular spray tube 13 is connected with water inlet 10, lower floor's circular spray tube 13 is connected with oil groove 14 by oil-in 15, shower nozzle 9 outlets of circular spray tube 13 are installed vertically downward.
The course of work of the present utility model is: the material import 11 of the material that first will leach from pot for solvent extraction 4 top covers adds by conveying worm, enter into and filter in reative cell 21, and spray into after a certain amount of 6# oil and water by circular spray tube 13, under the stirring action of mixer 18, material and stirring solvent are mixed, then open the heater 17 in filter cylinder 7, be heated to the required reaction temperature of material, for the temperature in real-time monitoring of tank, in described filtration reative cell 21, thermocouple thermometer is also installed, in the process of heating, mixer 18 is also in continuous rotation, the solid suspended material of scarifying, in accelerating solid material, active ingredient spreads in solvent, after heating finishes, mixer 18 also quits work, make its material filter the interior abundant reaction of reative cell 21, the leachate leaching between the stage of reaction enters in collecting chamber 3 by filter cylinder 7, after lixiviate reaction finishes, open liquid outlet 19 and discharge leachate, liquid outlet 19 has certain altitude apart from the tank body of pot for solvent extraction 4, in case be deposited on a small quantity the superfine powder of screen surface, from liquid outlet 19, discharge, affect the purity of leachate, after leaching liquor is emptying, open blow-off valve 2, solid material is discharged by discharge gate 1 under the slow stirring of mixer 18, after deslagging finishes, by water inlet 10, add a small amount of flushing water to rinse by circular spray tube 13 superfine powder that is attached to filter cylinder 7 screen surface, it is discharged from slag-drip opening, a leaching process finishes to carry out next leaching process.
Further, on pot for solvent extraction 4 housings of described collecting chamber 3, the overfall 16 lower than coghill net plate height 200～300mm being installed, is that counter the flowing back to of leachate in order to prevent from entering in collecting chamber 3 filtered in reative cell 21, affects recovery rate.
For reaching good filter effect and recovery rate, described upper cone 8 is 120～150 ° with the setting angle of cylinder 5, and described lower cone 20 is 120～180 ° with the setting angle of cylinder 5.In order to make material temperature constant in the process of reaction, the tank body outside of described pot for solvent extraction 4 is provided with asbestos heat-insulation layer 6.
Further, being also provided with visor 12 on the top cover of described pot for solvent extraction 4, is for the ease of observing the operation situation of pot for solvent extraction 4 interior materials.
Claims (6)
1. a nicotine sulphate leaching device, comprise pot for solvent extraction (4), discharge gate (1), blow-off valve (2), liquid outlet (19), be arranged on the charging aperture (11) on pot for solvent extraction (4) top cover, gas outlet and mixer (18), it is characterized in that: in described pot for solvent extraction (4), be provided with filter cylinder (7), described filter cylinder (7) is divided into pot for solvent extraction (4) collecting chamber (3) and filters reative cell (21), in described filtration reative cell (21), be provided with heater (17), described filter cylinder (7) is by upper cone (8), cylinder (5) and lower cone (20) form, described lower cone (20) is fixed on pot for solvent extraction (4) base plate of discharge gate (1) top, the middle and lower part of described cylinder (5) and lower cone (8) are the structure with the circular arc web plate composition of sieve aperture, two-layer circular spray tube (13) is installed on the inwall of described upper cone (8), upper strata circular spray tube (13) is connected with water inlet (10), lower floor's circular spray tube (13) is connected with oil groove (14) by oil-in (15), shower nozzle (9) outlet of described circular spray tube (13) is installed vertically downward.
2. a kind of nicotine sulphate leaching device according to claim 1, is characterized in that: on pot for solvent extraction (4) housing of described collecting chamber (3), the overfall (16) lower than coghill net plate height 200～300mm is installed.
3. a kind of nicotine sulphate leaching device according to claim 1, is characterized in that: described upper cone (8) is 120～150 ° with the setting angle of cylinder (5), and lower cone (20) is 120～180 ° with the setting angle of cylinder (5).
4. a kind of nicotine sulphate leaching device according to claim 1, is characterized in that: the tank body outside of described pot for solvent extraction (4) is provided with asbestos heat-insulation layer (6).
5. a kind of nicotine sulphate leaching device according to claim 1, is characterized in that: on the top cover of described pot for solvent extraction (4), be also provided with visor (12).
6. a kind of nicotine sulphate leaching device according to claim 1, is characterized in that: in described filtration reative cell (21), thermocouple thermometer is also installed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420300784.5U CN203886231U (en) | 2014-06-09 | 2014-06-09 | Nicotine sulfate extraction device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420300784.5U CN203886231U (en) | 2014-06-09 | 2014-06-09 | Nicotine sulfate extraction device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203886231U true CN203886231U (en) | 2014-10-22 |
Family
ID=51712684
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420300784.5U Expired - Fee Related CN203886231U (en) | 2014-06-09 | 2014-06-09 | Nicotine sulfate extraction device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203886231U (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105641969A (en) * | 2016-01-08 | 2016-06-08 | 严修长 | Traditional Chinese medicine extraction tank |
| CN106731960A (en) * | 2015-11-25 | 2017-05-31 | 衡阳屹顺化工有限公司 | A kind of mirabilite ore stirring and dissolving device |
| CN106731114A (en) * | 2016-11-11 | 2017-05-31 | 江苏荣豪生物环保科技有限公司 | A kind of rubbish solid-liquid separator |
| CN106890491A (en) * | 2015-12-17 | 2017-06-27 | 宁波荣辉纳米技术有限公司 | A kind of new and effective dregs of fat separation equipment |
| CN110124351A (en) * | 2019-05-24 | 2019-08-16 | 亳州职业技术学院 | A kind of preparing new-type medical herbs drink tablets extraction element and preparation method |
| CN111437943A (en) * | 2020-04-17 | 2020-07-24 | 南京信息职业技术学院 | Kiwi fruit seed autosegregation machine |
| CN111760377A (en) * | 2020-07-09 | 2020-10-13 | 唐山三友氯碱有限责任公司 | Latex conveying system and method in production process of special resin for polyvinyl chloride |
-
2014
- 2014-06-09 CN CN201420300784.5U patent/CN203886231U/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106731960A (en) * | 2015-11-25 | 2017-05-31 | 衡阳屹顺化工有限公司 | A kind of mirabilite ore stirring and dissolving device |
| CN106890491A (en) * | 2015-12-17 | 2017-06-27 | 宁波荣辉纳米技术有限公司 | A kind of new and effective dregs of fat separation equipment |
| CN105641969A (en) * | 2016-01-08 | 2016-06-08 | 严修长 | Traditional Chinese medicine extraction tank |
| CN106731114A (en) * | 2016-11-11 | 2017-05-31 | 江苏荣豪生物环保科技有限公司 | A kind of rubbish solid-liquid separator |
| CN110124351A (en) * | 2019-05-24 | 2019-08-16 | 亳州职业技术学院 | A kind of preparing new-type medical herbs drink tablets extraction element and preparation method |
| CN111437943A (en) * | 2020-04-17 | 2020-07-24 | 南京信息职业技术学院 | Kiwi fruit seed autosegregation machine |
| CN111437943B (en) * | 2020-04-17 | 2021-07-20 | 南京信息职业技术学院 | Kiwi fruit seed autosegregation machine |
| CN111760377A (en) * | 2020-07-09 | 2020-10-13 | 唐山三友氯碱有限责任公司 | Latex conveying system and method in production process of special resin for polyvinyl chloride |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141022 Termination date: 20210609 |