CN205850301U - A kind of rapeseed meal phytic acid extraction equipment - Google Patents
A kind of rapeseed meal phytic acid extraction equipment Download PDFInfo
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- CN205850301U CN205850301U CN201620839266.XU CN201620839266U CN205850301U CN 205850301 U CN205850301 U CN 205850301U CN 201620839266 U CN201620839266 U CN 201620839266U CN 205850301 U CN205850301 U CN 205850301U
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- phytic acid
- dense
- storage tank
- high concentration
- extraction equipment
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Abstract
The utility model discloses a kind of rapeseed meal phytic acid extraction equipment；Extraction equipment includes phytic acid extractor, disc type desolventizing device, dense phytic acid liquid storage tank, dense phytic acid liquid vaporizer and the phytic acid liquid storage tank that the first enclosed screw conveyor that feeding conveyor is connected is connected with the first enclosed screw conveyor with feeding conveyor；Phytic acid extractor includes blending tank, extracter and drains transport platform；The bottom of extracter is provided with high concentration extract and accommodates chamber, high concentration extract accommodates the bottom in chamber and is provided with leakage fluid dram, disc type desolventizing device is connected with draining transport platform by the second enclosed screw conveyor, high concentration extract is accommodated the leakage fluid dram in chamber and is retracted in dense phytic acid liquid storage tank by high concentration extract by high concentration extraction liquid pump, dense phytic acid liquid vaporizer is connected with dense phytic acid liquid storage tank, and phytic acid liquid storage tank is connected with dense phytic acid liquid vaporizer；This utility model simple in construction, easy to use, can extract and obtain high concentration, pure finished product phytic acid.
Description
Technical field
This utility model relates to phytic acid and extracts processing technique field, particularly to a kind of rapeseed meal phytic acid extraction equipment.
Background technology
There is a certain amount of phytic acid in rapeseed meal, phytic acid can affect the feeding value of rapeseed meal to a certain extent, generally
In feed industry, usually done Passivation Treatment rather than removed it；But phytic acid has in industries such as food, chemical industry, medicine
Purposes widely, be important fine chemical product, therefore phytic acid is extracted from rapeseed meal and both can improve Semen Allii Tuberosi
Dregs of rice palatability, it also avoid the waste of phytic acid.
Utility model content
The technical problems to be solved in the utility model is to provide a kind of simple in construction, can extract the Semen Allii Tuberosi of high concentration phytic acid
Dregs of rice phytic acid extraction equipment.
For reaching above-mentioned purpose, the technical solution of the utility model is as follows:
A kind of rapeseed meal phytic acid extraction equipment；Described extraction equipment includes:
One feeding conveyor；
One the first enclosed screw conveyor being connected with feeding conveyor；
The one phytic acid extractor being connected with the first enclosed screw conveyor, described phytic acid extractor includes blending tank, extraction
Machine and drain transport platform, described blending tank is for receiving the rapeseed meal come to the first enclosed screw conveyor conveying, and general
It mixes with solvent；Extracter is connected with blending tank, for extracting rapeseed meal mixed in blending tank；Drain conveying
Platform is connected with extracter, for carrying out carrying and draining process by the solid material after extraction；
The bottom of described extracter is provided with high concentration extract and accommodates chamber, and described high concentration extract accommodates the bottom in chamber and sets
There is leakage fluid dram；
The described bottom draining transport platform is provided with low concentration extract recycling cavity, the end of described low concentration extract recycling cavity
Portion is provided with leakage fluid dram；
One disc type desolventizing device, described disc type desolventizing device is connected with draining transport platform, and described disc type desolventizing device is for by solid
Solvent extraction in material is out；
One dense phytic acid liquid storage tank, described high concentration extract accommodates the leakage fluid dram in chamber by high concentration extraction liquid pump by highly concentrated
Degree extract is retracted in dense phytic acid liquid storage tank；
One dense phytic acid liquid vaporizer, described dense phytic acid liquid vaporizer is connected with dense phytic acid liquid storage tank, for high concentration being extracted
Take the phytic acid in liquid and solvent is separated；
One phytic acid liquid storage tank, described phytic acid liquid storage tank is connected with dense phytic acid liquid vaporizer, is used for storing the evaporation of dense phytic acid liquid
The phytic acid that device extracts.
In an embodiment of the present utility model, described extraction equipment also includes a low concentration extract circulating pump, institute
State concentration extract circulating pump for being returned in blending tank by the low concentration extract in low concentration extract recycling cavity.
In an embodiment of the present utility model, described extraction equipment also includes a high concentration extract filter, institute
State high concentration extract filter to be arranged between high concentration extraction liquid pump and dense phytic acid liquid storage tank, in high concentration extract
Impurity, it is pure for making the high concentration extract in arrival dense phytic acid liquid storage tank.
In an embodiment of the present utility model, described extraction equipment also includes a condenser for solvent, and described solvent is cold
Condenser is for the solvent receiving disc type desolventizing device and dense phytic acid liquid vaporizer is separated, and cools down it.
In an embodiment of the present utility model, described extraction equipment also includes a circulating evaporator, and described circulation is steamed
Send out device to be connected with phytic acid liquid storage tank, by remaining solvent extraction in phytic acid in phytic acid liquid storage tank out, thus obtain finished product phytic acid.
In an embodiment of the present utility model, described circulating evaporator includes that heater, separator and solvent are received
Collection condenser, separator is connected with heater.
In an embodiment of the present utility model, described extraction equipment also includes a finished product phytic acid storage tank, described circulation
Vaporizer is connected with finished product phytic acid storage tank by delivery pump.
In an embodiment of the present utility model, described phytic acid extractor is single-stage chain type extractor.
In an embodiment of the present utility model, described condenser for solvent is horizontal pipe bundle condenser.
In an embodiment of the present utility model, described disc type desolventizing device and drain and be provided with the second closing between transport platform
Conveying worm.
By technique scheme, the beneficial effects of the utility model are:
This utility model simple in construction, easy to use, can extract and obtain high concentration, pure finished product phytic acid.
Accompanying drawing explanation
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, below will be to embodiment
Or the required accompanying drawing used is briefly described in description of the prior art, it should be apparent that, the accompanying drawing in describing below is only
It is embodiments more of the present utility model, for those of ordinary skill in the art, in the premise not paying creative work
Under, it is also possible to other accompanying drawing is obtained according to these accompanying drawings.
Fig. 1 is utility model works schematic diagram；
Numeral and the corresponding component title represented by letter in figure:
10, material conveyer the 20, first enclosed screw conveyor 30, phytic acid extractor 31, blending tank 32, extracter
33, transport platform 40, disc type desolventizing device 50, dense phytic acid liquid storage tank 60, dense phytic acid liquid vaporizer 70, phytic acid liquid storage tank are drained
80, low concentration extract circulating pump 90, high concentration extraction liquid pump 91, high concentration extract filter 100, condenser for solvent
110, circulating evaporator 120, finished product phytic acid storage tank the 130, second sealing spiral conveyer 140, delivery pump.
Detailed description of the invention
For the technological means making this utility model realize, creation characteristic, reach purpose and be easy to understand with effect, under
Face combines and is specifically illustrating, and this utility model is expanded on further.
Shown in Figure 1, the utility model discloses a kind of rapeseed meal phytic acid extraction equipment；Extraction equipment includes feeding defeated
The first enclosed screw conveyor 20 sending machine 10 to be connected with feeding conveyor 10 is connected with the first enclosed screw conveyor 20
Phytic acid extractor 30, disc type desolventizing device 40, dense phytic acid liquid storage tank 50, dense phytic acid liquid vaporizer 60 and phytic acid liquid storage tank 70.
Phytic acid extractor 30 includes blending tank 31, extracter 32 and drains transport platform 33, and blending tank 31 is used for receiving
The rapeseed meal come to the first enclosed screw conveyor 20 conveying, and it is mixed with solvent；Extracter 32 is connected with blending tank 31,
For rapeseed meal mixed in blending tank 31 is extracted；Drain transport platform 33 to be connected with extracter 32, for extracting
After solid material carry out carrying and draining process；The bottom of extracter 32 is provided with high concentration extract and accommodates chamber, and high concentration extracts
Liquid accommodates the bottom in chamber and is provided with leakage fluid dram；The bottom draining transport platform 33 is provided with low concentration extract recycling cavity, and low concentration extracts
The bottom of liquid recycling cavity is provided with leakage fluid dram；Disc type desolventizing device 40 is connected with draining transport platform 33, and disc type desolventizing device 40 is for by solid
Solvent extraction in body material is out；High concentration extract is accommodated the leakage fluid dram in chamber and high concentration is extracted by high concentration extraction liquid pump 90
Take liquid to be retracted in dense phytic acid liquid storage tank 50；Dense phytic acid liquid vaporizer 60 is connected with dense phytic acid liquid storage tank 50, for by high concentration
Phytic acid and solvent in extract are separated；Phytic acid liquid storage tank 70 is connected with dense phytic acid liquid vaporizer 60, is used for storing dense phytic acid
The phytic acid that liquid vaporizer extracts.
This utility model extraction equipment also includes a low concentration extract circulating pump 80, high concentration extraction liquid pump 90, highly concentrated
Degree extract filter 91, condenser for solvent 100, circulating evaporator 110 and finished product phytic acid storage tank 120；Concentration extract follows
Ring pump 80 is for returning the low concentration extract in low concentration extract recycling cavity in blending tank 31；High concentration extract mistake
Filter 91 is arranged between high concentration extraction liquid pump 90 and dense phytic acid liquid storage tank 50, and the impurity in high concentration extract makes
It is pure for arriving the high concentration extract in dense phytic acid liquid storage tank；Condenser for solvent 100 is used for receiving disc type desolventizing device 40
The solvent separated with dense phytic acid liquid vaporizer 60, and it is cooled down；Circulating evaporator 110 is with phytic acid liquid storage tank 70 even
Connect, by remaining solvent extraction in phytic acid in phytic acid liquid storage tank 70 out, thus obtain finished product phytic acid；Circulating evaporator 110 leads to
Cross delivery pump 140 to be connected with finished product phytic acid storage tank 120.
Operation principle of the present utility model is as follows:
First rapeseed meal continuously enters in the first sealing spiral conveyer 20 by feeding conveyor 10, the first sealing screw
Conveyer 20 is connected with the import of phytic acid extractor 30, and the first sealing spiral conveyer 20 has conveying material and sealed solvent gas
The effect of body；Rapeseed meal is after the first sealing spiral conveyer 20 enters phytic acid extractor 30, first in fore blending tank 31
Being sufficiently mixed with solvent, extract in being then fed into horizontal segment extracter 32, solvent (ethanol) is to the phytic acid calcium in rapeseed meal
Carrying out continuous-dissolution extraction, the high concentration extract produced after extraction enters the high concentration extract bottom extracter and accommodates chamber
In, the solid material produced after extraction is through tilting to drain after transport platform 33 drains by the second sealing spiral conveyer 130 feeding dish
In formula desolventizing device 40, after steaming solvent by steam heating in disc type desolventizing device 40, send to warehouse storage, disc type desolventizing device 40
The solvent evaporated enters condenser for solvent 100 and condenses Posterior circle use.
The low concentration extract that solid material produces after draining is back in low concentration extract recycling cavity, low concentration extract
Circulating pump 80 low concentration extract is returned in front end blending tank 31 with newly enter rapeseed meal and mix, high concentration extract is through too high
Concentration extraction liquid pump 90 is extracted out and passes through to enter in dense phytic acid liquid storage tank 50 after high concentration extract filter 91 filters to store；Dense
The outlet of phytic acid liquid storage tank 50 is connected with dense phytic acid liquid vaporizer 60, and the solvent that dense phytic acid liquid vaporizer 60 evaporates enters solvent
Condenser 100 condenses Posterior circle and uses；The phytic acid liquid obtained enters phytic acid liquid storage tank 70 and stores, and phytic acid liquid storage tank 70 is arranged on height
Position, enters circulating evaporator 110 by flow by gravity and carries out last concentration；Circulating evaporator 110 by heater, separator with
And solvent collects condenser composition, phytic acid liquid initially enters and carries out climbing-film evaporation in heater, and solution is carried out point in the separator
From, the solvent evaporated is upwardly into solvent and collects in condenser, and plant acid solution is downwardly into the storage tank of separator bottom, storage tank
Bottom is connected with heater, and plant acid solution is circulated concentration；Concentrate qualified finished product phytic acid and extracted out feeding by delivery pump 140
Finished product phytic acid storage tank 120 stores.
Extraction process is mainly carried out at phytic acid extractor, and phytic acid extractor is single-stage chain type extractor, and it is mixed to arrange front end
Clutch so that rapeseed meal can be sufficiently mixed with solvent, improves extraction efficiency；Phytic acid extractor also sets up VFC, according to entering
Doses adjusts rotating speed automatically, it is ensured that effect of extracting.
Precipitation operation is mainly carried out in disc type desolventizing machine, and disc type desolventizing machine uses many charging trays, and the shallow bed of material designs, and utilizes water
Steam is as thermal source, and owing to this kind of desolventizing machine heating surface (area) (HS is big, rapeseed meal is heated evenly, so solvent removal effect ten sub-argument
Think.
Evaporization process is mainly carried out in dense phytic acid liquid vaporizer, circulating evaporator, and dense phytic acid liquid vaporizer uses vertical
Column tube evaporimeter, its disengagement area is big, and efficiency is high；Circulating evaporator uses heater, separator, solvent to collect condenser and ties mutually
The design closed, and it is qualified to product to make phytic acid liquid circulate rectification wherein, it is ensured that product quality.
Condensation procedure is mainly carried out in condenser for solvent, uses horizontal pipe bundle condenser, and heat exchange area is big, condensation effect
Good, use process Maintenance free.
Of the present utility model ultimate principle and principal character and of the present utility model advantage have more than been shown and described.One's own profession
Skilled person will appreciate that of industry, this utility model is not restricted to the described embodiments, described in above-described embodiment and description
Principle of the present utility model is simply described, on the premise of without departing from this utility model spirit and scope, this utility model is also
Have various changes and modifications, in the range of these changes and improvements both fall within claimed this utility model.This utility model
Claimed scope is defined by appending claims and equivalent thereof.
Claims (10)
1. a rapeseed meal phytic acid extraction equipment；It is characterized in that, described extraction equipment includes:
One feeding conveyor；
One the first enclosed screw conveyor being connected with feeding conveyor；
The one phytic acid extractor being connected with the first enclosed screw conveyor, described phytic acid extractor include blending tank, extracter with
And drain transport platform, described blending tank for receive to first enclosed screw conveyor conveying come rapeseed meal, and by itself and
Solvent mixes；Extracter is connected with blending tank, for extracting rapeseed meal mixed in blending tank；Drain transport platform with
Extracter connects, for carrying out carrying and draining process by the solid material after extraction；
The bottom of described extracter is provided with high concentration extract and accommodates chamber, and described high concentration extract accommodates the bottom in chamber and is provided with row
Liquid mouth；
The described bottom draining transport platform is provided with low concentration extract recycling cavity, and the bottom of described low concentration extract recycling cavity sets
There is leakage fluid dram；
One disc type desolventizing device, described disc type desolventizing device is connected with draining transport platform, and described disc type desolventizing device is for by solid material
Solvent extraction out；
One dense phytic acid liquid storage tank, described high concentration extract is accommodated the leakage fluid dram in chamber and high concentration is extracted by high concentration extraction liquid pump
Take liquid to be retracted in dense phytic acid liquid storage tank；
One dense phytic acid liquid vaporizer, described dense phytic acid liquid vaporizer is connected with dense phytic acid liquid storage tank, for by high concentration extract
In phytic acid and solvent separate；
One phytic acid liquid storage tank, described phytic acid liquid storage tank is connected with dense phytic acid liquid vaporizer, is used for storing dense phytic acid liquid vaporizer and carries
The phytic acid taken out.
A kind of rapeseed meal phytic acid extraction equipment the most according to claim 1, it is characterised in that described extraction equipment also includes
One low concentration extract circulating pump, described concentration extract circulating pump is for extracting the low concentration in low concentration extract recycling cavity
Take liquid to return in blending tank.
A kind of rapeseed meal phytic acid extraction equipment the most according to claim 1, it is characterised in that described extraction equipment also includes
One high concentration extract filter, described high concentration extract filter is arranged on high concentration extraction liquid pump and dense phytic acid liquid storage tank
Between, the impurity in high concentration extract, it is pure for making the high concentration extract in arrival dense phytic acid liquid storage tank.
A kind of rapeseed meal phytic acid extraction equipment the most according to claim 1, it is characterised in that described extraction equipment also includes
One condenser for solvent, described condenser for solvent for the solvent receiving disc type desolventizing device and dense phytic acid liquid vaporizer is separated,
And it is cooled down.
A kind of rapeseed meal phytic acid extraction equipment the most according to claim 1, it is characterised in that described extraction equipment also includes
One circulating evaporator, described circulating evaporator is connected with phytic acid liquid storage tank, is carried by remaining solvent in phytic acid in phytic acid liquid storage tank
Take out, thus obtain finished product phytic acid.
A kind of rapeseed meal phytic acid extraction equipment the most according to claim 5, it is characterised in that described circulating evaporator includes
Condenser collected by heater, separator and solvent, and separator is connected with heater.
A kind of rapeseed meal phytic acid extraction equipment the most according to claim 5, it is characterised in that described extraction equipment also includes
One finished product phytic acid storage tank, described circulating evaporator is connected with finished product phytic acid storage tank by delivery pump.
A kind of rapeseed meal phytic acid extraction equipment the most according to claim 1, it is characterised in that described phytic acid extractor is single
Level chain type extractor.
A kind of rapeseed meal phytic acid extraction equipment the most according to claim 4, it is characterised in that described condenser for solvent is sleeping
Formula pipe bundle condenser.
A kind of rapeseed meal phytic acid extraction equipment the most according to claim 1, it is characterised in that described disc type desolventizing device with
Drain and between transport platform, be provided with the second enclosed screw conveyor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620839266.XU CN205850301U (en) | 2016-08-04 | 2016-08-04 | A kind of rapeseed meal phytic acid extraction equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620839266.XU CN205850301U (en) | 2016-08-04 | 2016-08-04 | A kind of rapeseed meal phytic acid extraction equipment |
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| Publication Number | Publication Date |
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| CN205850301U true CN205850301U (en) | 2017-01-04 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201620839266.XU Expired - Fee Related CN205850301U (en) | 2016-08-04 | 2016-08-04 | A kind of rapeseed meal phytic acid extraction equipment |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108079618A (en) * | 2017-11-13 | 2018-05-29 | 涟源康麓生物科技有限公司 | It is atomized extraction element and extracting method |
| CN111375225A (en) * | 2020-03-30 | 2020-07-07 | 山东凯斯达机械制造有限公司 | Immersed swelling extractor and use method thereof |
-
2016
- 2016-08-04 CN CN201620839266.XU patent/CN205850301U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108079618A (en) * | 2017-11-13 | 2018-05-29 | 涟源康麓生物科技有限公司 | It is atomized extraction element and extracting method |
| CN111375225A (en) * | 2020-03-30 | 2020-07-07 | 山东凯斯达机械制造有限公司 | Immersed swelling extractor and use method thereof |
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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: 20170104 Termination date: 20180804 |
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| CF01 | Termination of patent right due to non-payment of annual fee |