CN206138783U - Leach equipment suitable for powder - Google Patents
Leach equipment suitable for powder Download PDFInfo
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- CN206138783U CN206138783U CN201621135495.XU CN201621135495U CN206138783U CN 206138783 U CN206138783 U CN 206138783U CN 201621135495 U CN201621135495 U CN 201621135495U CN 206138783 U CN206138783 U CN 206138783U
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- leaching
- powder
- finished product
- pipe
- discharge nozzle
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Abstract
The utility model belongs to leach the ware field, concretely relates to leach equipment suitable for powder, including leaching the jar, leach and be equipped with the separation chamber in the jar, the outer wall of separation chamber, part or whole diffusion barrier material that adopts, leaching jar the top and having a feed inlet, the below has the extract product of leaching export and a finished product discharge port, the inlet pipe that feed inlet department connects, the finished product discharging pipe that finished product discharge port department connects respectively with import, the exit linkage of separation chamber, leach the extract product exit and connect and leach the extract product discharging pipe, it has raw powder and solvent to lead to in the inlet pipe. The utility model discloses a diffusion barrier has been realized fully having improved and having leached efficiency and leaching effect the leaching of active ingredient in the powdered material, compares the traditional handicraft, and active ingredient's yield can improve more than 30%.
Description
Technical field
This utility model is related to a kind of leaching equipment suitable for powder, belongs to infuser field.
Background technology
At present, generally using infuser by material (include Chinese medicine, the root of plant, stem, flower, leaf, fruit etc., especially Semen Gossypii,
The oil crop such as Semen arachidis hypogaeae) in protein, the effective ingredient such as oils and fatss leached.Entered using screen in conventionally employed infuser
Row is leached, and needs material is made embryo piece or granule first before concrete operations, then embryo piece or granule are placed on screen,
Solvent is sprayed on the material above screen, effective ingredient (soluble compound) is leached from material, and under screen
Side is dropped down onto in leaching tanks, finally carries out being refining to obtain required effective ingredient by infusion solution.
But as embryo piece or granule are little with the mass transfer area of solvent, therefore leaching effect is bad, and leaching efficiency is low, the time
Long, if wanting to improve leaching effect, improving the yield of effective ingredient, best mode is that material is made powder.But because of screen
Spacing it is larger, the material of such powder can leak down from screen, or during solvent spray block screen, because
The version of this existing infuser causes which leach to the material of powder.
Except above-mentioned points, the embryo piece used in traditional infuser in the preparation, is needed by softening → rolling embryo → drying etc.
Series of processes process, needs using substantial amounts of steam in softening process, therefore it is relatively large to consume energy, and prepares above-mentioned
Cheng Zhong, cell wall shell-broken effect are poor, so as to cause later stage leaching effect poor, while can also destroy in preparation process protein or
The effective ingredient such as oils and fatss, the yield of effective ingredient are low.Granule used in traditional infuser is then needed in the preparation through crushing
The step of → pelletize, and granule is relatively large, is unfavorable for the leaching of effective ingredient.
Utility model content
The technical problems to be solved in the utility model is：Overcome deficiency of the prior art, there is provided a kind of to be applied to powder
, leaching effect is good, can improve the leaching equipment of the yield of effective ingredient.
Leaching equipment suitable for powder described in the utility model, including batch extractor, are provided with separation chamber in batch extractor；Point
From the outer wall of room, some or all of employing separation membrane material；There is above batch extractor charging aperture, lower section has leaches extract
Outlet and finished product discharging opening, at charging aperture connect feed pipe, finished product discharge outlet connection finished product discharge nozzle respectively with separate
The import of room, outlet connection, leach the connection of extract exit and leach extract discharge nozzle, be connected with feed pipe powder stock and
Solvent；Leach and pacify cartridge control valve on extract discharge nozzle and finished product discharge nozzle.
Operation principle process of the present utility model is as follows：The powder stock for crushing and solvent are carried out into feed pipe
Mixing, and entered in separation chamber, in the presence of seperation film by import, the effective ingredient of leaching is passed through with the mixture of solvent
Seperation film is entered and is separated in outdoor batch extractor, and sends into follow-up refining step by leaching extract discharge nozzle, and then to having
Effect composition is extracted, meanwhile, after each separation chamber's leaching effective ingredient, remaining finished product (containing protein etc.) is discharged by finished product
Pipe is collected, and carries out later stage application by processing.
This utility model is by solving the technology that existing leaching equipment cannot be applied to powder material using seperation film
Bottleneck, realizes the leaching to effective ingredient in powder material.Because material is during powder material is broken into, can be with
Break cell wall well, be conducive to the leaching of effective ingredient, can from largely reduce stay in material it is effective into
The content divided, compares embryo piece or granule with advantage big with the mass transfer area of solvent, that leaching effect is good, therefore passes through this reality
Leaching efficiency and leaching effect can fully be improved with new, traditional handicraft is compared, the yield of effective ingredient can improve 30%
More than.
Preferably, blending tank is set up, blending tank is provided with solvent inlet pipe and powder stock inlet pipe, and solvent inlet pipe, powder are former
Control valve is respectively mounted on material inlet pipe, the feed pipe described in the discharging opening connection of blending tank installs pump on feed pipe.It is mixed by setting up
Tank is closed, solvent can be made fully to react with powder stock, in being conducive to powder stock, leach the leaching of extract.
Preferably, heat exchanger is installed on described solvent inlet pipe.In normal leaching process, solvent temperature is too high or mistake
It is low all to produce negative consequence：When solvent temperature is too high, raw material and leaching extract etc. are easily destroyed；Solvent temperature is too low
When, leaching efficiency is also low.By solvent being made to reach suitable temperature using heat exchanger, so as to effectively improve leaching extract
Leaching velocity.
Preferably, agitator is installed in described blending tank.Agitator is conventional equipment, and which is by stirring vane, shaft
Constitute with motor, drive shaft to rotate by motor, so that the stirring vane on shaft is rotated, realize to molten
Agent is mixed with powder stock stirring, so can fully be leached the leaching extract in powder stock, effectively can be shortened again
Extraction time, improves leaching effect.
Preferably, described separation chamber arranges multiple, and the multiple separation chambers of correspondence are provided with consolidating for fixedly separated room two ends
Fixed board, correspondence separation chamber are respectively provided with two fixed plates and separation chamber's quantity identical plate hole, are respectively welded in two fixed plates
Reducer pipe one, reducer pipe two, and two fixed plates are gone out by reducer pipe one, the feed pipe of reducer pipe two and respective side, finished product respectively
Expects pipe connects, and the import of each separation chamber is connected with feed pipe by co-route (i.e. reducer pipe one), and in the same manner, each separation chamber goes out
Mouth is connected with finished product discharge nozzle by reducer pipe two, i.e., solvent is entered by same feed pipe with the mixed material of powder stock and become
After footpath is managed the import of separated room in the lump and is dispensed in each separation chamber, and each separation chamber leaches effective ingredient, remaining finished product (contains
Protein etc.) converged to same finished product discharge nozzle by reducer pipe two, it is collected by finished product discharge nozzle.
Preferably, the reducer pipe one being connected with feed pipe, which is more than feed pipe with the internal diameter of one end of fixed plate weld
Internal diameter；The reducer pipe two being connected with finished product discharge nozzle, which is more than in finished product discharge nozzle with the internal diameter of one end of fixed plate weld
Footpath.
Preferably, described seperation film adopts micro-filtration membrane, or ultrafilter membrane, or NF membrane.Can be with concrete application
Selected according to the granularity of powder.
Leaching equipment described in the utility model can be used for the leaching of oils and fatss in oil crop powder, using when oil plant is made
Thing powder and solvent are sent in the separation chamber of batch extractor, and the oils and fatss in oil crop powder under solvent action are leached and passed through
In the batch extractor that seperation film is entered on the outside of separation chamber, in batch extractor, oils and fatss are extracted along leaching with the mixture (i.e. miscella) of solvent
Flow out in thing discharge nozzle, last miscella is admitted to follow-up refining procedure and carries out refine, and remaining finished product (contains egg in separation chamber
White matter etc.) processed from finished product discharge nozzle feeding subsequent handling, such as evaporate the solvent in finished product by baking operation.Tradition
Grease lixiviating process cell wall is broken using " pressure embryo → drying → expanded " technique mostly, but leaching velocity slowly, time length, energy
Consumption is high, and leaching effect is undesirable；This utility model is then first to crush (to enter by flour mill by oil crop according to the difference of oil plant
Row dry grinding or to carry out wet-milling by macerator pump broken) it is powdered, so as to break cell wall well, be conducive to the leaching of oils and fatss
Go out, reduce the content for staying in oils and fatss in oil crop, improve the yield of oils and fatss, while leaching velocity is fast, the time is short, saving
The energy, application effect are notable.
Leaching equipment described in the utility model can also be used for Chinese medicinal powder or plant (root, stem, leaf, flower, fruit etc.) powder
The leaching of effective ingredient in end, concrete leaching process are identical with the leaching process of oils and fatss in above-mentioned oil crop powder, equally may be used
With the extraction time for shortening effective ingredient, the yield for improving effective ingredient, improve leaching efficiency, reducing energy consumption.
This utility model is had an advantageous effect in that compared with prior art：
This utility model is by solving the technology that existing leaching equipment cannot be applied to powder material using seperation film
Bottleneck, realizes the leaching to effective ingredient in powder material, and compares embryo piece or granule, powder with solvent
Mass transfer area is big, the advantage that leaching effect is good such that it is able to from containing for the effective ingredient for largely reducing staying in material
Amount, fully improves leaching efficiency and leaching effect, compares traditional handicraft, and the yield of effective ingredient can improve more than 30%.
Description of the drawings
Fig. 1 is structural representation of the present utility model；
Fig. 2 is the partial enlarged drawing at I positions in Fig. 1.
In figure：1st, solvent inlet pipe；2nd, heat exchanger；3rd, control valve；4th, stirring vane；5th, shaft；6th, powder stock inlet pipe；
7th, blending tank；8th, motor；9th, pump；10th, feed pipe；11st, batch extractor；12nd, finished product discharge nozzle；13rd, leach extract discharge nozzle；
14th, reducer pipe one；15th, fixed plate；16th, import；17th, separation chamber；18th, export；19th, reducer pipe two.
Specific embodiment
Below in conjunction with the accompanying drawings embodiment of the present utility model is described further：
As shown in Figure 1, 2, the leaching equipment suitable for powder described in the utility model includes batch extractor 11, batch extractor 11
Separation chamber 17 is provided with inside；The outer wall of separation chamber 17, some or all of employing separation membrane material；There is above batch extractor 11 charging
Mouthful, lower section has leaches extract discharging opening and finished product discharging opening, and at charging aperture, the feed pipe 10 of connection, finished product discharge outlet connect
The finished product discharge nozzle 12 for connecing import 16 respectively with separation chamber 17, outlet 18 be connecteds, leach the connection leaching of extract discharge outlet
Extract discharge nozzle 13, is connected with powder stock and solvent in feed pipe 10；Leach extract discharge nozzle 13 and finished product discharge nozzle 12
Upper peace cartridge control valve 3.
Operation principle process of the present utility model is as follows：The powder stock for crushing and solvent are entered into feed pipe 10
Row mixing, and entered in separation chamber 17, in the presence of seperation film by import 16, the effective ingredient of leaching and the mixing of solvent
In the batch extractor 11 that thing is entered outside separation chamber 17 through seperation film, and subsequently refined work is sent into by leaching extract discharge nozzle 13
Sequence, and then effective ingredient is extracted, meanwhile, each separation chamber 17 leaches remaining finished product after effective ingredient (containing protein etc.)
Be collected by finished product discharge nozzle 12, and later stage application is carried out by processing.Seperation film in this utility model can be adopted
Micro-filtration membrane, or ultrafilter membrane, or NF membrane, can be selected according to the granularity of powder in concrete application.
In the present embodiment, blending tank 7 is additionally arranged, blending tank 7 is provided with solvent inlet pipe 1 and powder stock inlet pipe 6, solvent
Control valve 3, the feed pipe 10 described in the discharging opening connection of blending tank 7, feed pipe 10 are respectively mounted on inlet pipe 1, powder stock inlet pipe 6
Upper installation pump 9, by setting up blending tank 7, can be such that solvent fully reacts with powder stock, leach and carry in being conducive to powder stock
Take the leaching of thing；Heat exchanger 2 is installed on solvent inlet pipe 1, by solvent being made to reach suitable temperature using heat exchanger 2, is had
Effect improves the leaching velocity for leaching extract；Agitator is installed in blending tank 7, agitator is by stirring vane 4,5 and of shaft
Motor 8 is constituted, and drives shaft 5 to rotate by motor 8, so that the stirring vane 4 on shaft 5 is rotated, is realized
Solvent is mixed with powder stock stirring, so the leaching extract in powder stock can fully be leached, again can be effective
Shorten extraction time, improve leaching effect.
Separation chamber 17 in the present embodiment arranges multiple, and corresponding multiple separation chambers 17 are provided with fixedly separated room two ends
Fixed plate 15, correspondence separation chamber 17 are respectively provided with two fixed plates 15 and 17 quantity identical plate hole of separation chamber, two fixed plates
Be respectively welded reducer pipe 1, reducer pipe 2 19 on 15, and two fixed plates 15 respectively by reducer pipe 1, reducer pipe 2 19 with
The feed pipe 10 of respective side, finished product discharge nozzle 12 connect, and the import 16 of each separation chamber 17 is by co-route (i.e. reducer pipe one
14) connect with feed pipe 10, in the same manner, the outlet 18 of each separation chamber 17 is connected with finished product discharge nozzle 12 by reducer pipe 2 19, i.e.,
The mixed material of solvent and powder stock enters 16 points of the import of reducer pipe 1 separated room 17 by same feed pipe 10
Allocate in each separation chamber 17, and after each separation chamber 17 leaches effective ingredient remaining finished product (containing protein etc.) by reducer pipe two
19 converge to same finished product discharge nozzle 12, are collected by finished product discharge nozzle 12；The reducer pipe 1 being connected with feed pipe 10, its
It is more than the internal diameter of feed pipe 10 with the internal diameter of one end of the welding of fixed plate 15；The reducer pipe 2 19 being connected with finished product discharge nozzle 12,
Internal diameter of the internal diameter of its one end welded with fixed plate 15 more than finished product discharge nozzle 12.
Leaching equipment described in the utility model both can be used for Chinese medicinal powder or plant (root, stem, leaf, flower, fruit etc.)
The leaching of effective ingredient in powder, it is also possible to for the leaching of oils and fatss in oil crop powder.Now leaching equipment is made in oil plant
Application in thing powder in oil extraction is made described below：
Using when oil crop powder and solvent are sent in the separation chamber 17 of batch extractor 11, in oil crop powder
Oils and fatss leach under solvent action and through seperation film enter separation chamber 17 on the outside of batch extractor 11 in, in batch extractor 11 oils and fatss with
The mixture (i.e. miscella) of solvent is admitted to follow-up refining procedure along outflow in extract discharge nozzle 13, last miscella is leached
Refine is carried out, and from separation chamber 17, remaining finished product (containing protein etc.) is carried out from the feeding subsequent handling of finished product discharge nozzle 12
Reason, such as evaporates the solvent in finished product by baking operation.Traditional grease lixiviating process is mostly using " pressure embryo → drying → swollen
Change " technique breaks cell wall, but leaching velocity is slow, time length, high energy consumption, and leaching effect is undesirable；This utility model is then root
According to oil plant difference first by oil crop crush (dry grinding is carried out by flour mill or to carry out wet-milling by macerator pump broken) into
Powder, so as to break cell wall well, is conducive to the leaching of oils and fatss, reduces the content for staying in oils and fatss in oil crop,
The yield of oils and fatss is improve, while leaching velocity is fast, the time is short, save energy, application effect is notable.
Claims (7)
1. a kind of leaching equipment suitable for powder, it is characterised in that：Including batch extractor (11), batch extractor (11) is interior to be provided with separation
Room (17)；The outer wall of separation chamber (17), some or all of employing separation membrane material；There is above batch extractor (11) charging aperture,
Lower section has leaches extract discharging opening and finished product discharging opening, and at charging aperture, the feed pipe (10) of connection, finished product discharge outlet connect
The finished product discharge nozzle (12) for connecing import (16) respectively with separation chamber (17), outlet (18) be connecteds, leaching extract discharge outlet
Extract discharge nozzle (13) is leached in connection, and feed pipe is connected with powder stock and solvent in (10)；Leach extract discharge nozzle (13)
With peace cartridge control valve (3) on finished product discharge nozzle (12).
2. the leaching equipment suitable for powder according to claim 1, it is characterised in that：Set up blending tank (7), blending tank
(7) solvent inlet pipe (1) and powder stock inlet pipe (6) are provided with, solvent inlet pipe (1), powder stock inlet pipe are respectively mounted control on (6)
Valve (3), the feed pipe (10) described in the discharging opening connection of blending tank (7), installs pump (9) on feed pipe (10).
3. the leaching equipment suitable for powder according to claim 2, it is characterised in that：On described solvent inlet pipe (1)
Heat exchanger (2) is installed.
4. the leaching equipment suitable for powder according to claim 2, it is characterised in that：Peace in described blending tank (7)
Dress agitator.
5. according to arbitrary described leaching equipment suitable for powder in Claims 1 to 4, it is characterised in that：Described separation
Room (17) arranges multiple, and the multiple separation chambers (17) of correspondence are provided with the fixed plate (15) at fixedly separated room two ends, and correspondence is separated
Room (17) is respectively provided with two fixed plates (15) and separation chamber (17) quantity identical plate hole；Two fixed plates are welded on (15) respectively
Reducer pipe one (14), reducer pipe two (19) are connect, and respectively by the charging of reducer pipe one (14), reducer pipe two (19) and respective side
Pipe (10), finished product discharge nozzle (12) connection.
6. according to the leaching equipment suitable for powder described in claim 5, it is characterised in that：It is connected with feed pipe (10)
Reducer pipe one (14), the internal diameter of its one end welded with fixed plate (15) are more than the internal diameter of feed pipe (10)；With finished product discharge nozzle
(12) reducer pipe two (19) for connecting, the internal diameter of its one end welded with fixed plate (15) are interior more than finished product discharge nozzle (12)
Footpath.
7. according to the leaching equipment suitable for powder described in claim 1,2,3,4 or 6, it is characterised in that：Described divides
Micro-filtration membrane, or ultrafilter membrane, or NF membrane are adopted from film.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621135495.XU CN206138783U (en) | 2016-10-18 | 2016-10-18 | Leach equipment suitable for powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621135495.XU CN206138783U (en) | 2016-10-18 | 2016-10-18 | Leach equipment suitable for powder |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206138783U true CN206138783U (en) | 2017-05-03 |
Family
ID=58623551
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621135495.XU Expired - Fee Related CN206138783U (en) | 2016-10-18 | 2016-10-18 | Leach equipment suitable for powder |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206138783U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107287028A (en) * | 2017-08-18 | 2017-10-24 | 刘玉通 | A kind of alcohol extracting taking technique of oil Class material Ultramicro-powder |
-
2016
- 2016-10-18 CN CN201621135495.XU patent/CN206138783U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107287028A (en) * | 2017-08-18 | 2017-10-24 | 刘玉通 | A kind of alcohol extracting taking technique of oil Class material Ultramicro-powder |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| 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: 20170503 Termination date: 20181018 |