CN205115342U - Use device of rice bran as raw material extraction phytic acid calcium - Google Patents
Use device of rice bran as raw material extraction phytic acid calcium Download PDFInfo
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- CN205115342U CN205115342U CN201520907368.6U CN201520907368U CN205115342U CN 205115342 U CN205115342 U CN 205115342U CN 201520907368 U CN201520907368 U CN 201520907368U CN 205115342 U CN205115342 U CN 205115342U
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- alkali
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- acid
- rice bran
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Abstract
The utility model provides an use device of rice bran as raw material extraction phytic acid calcium, includes that heavy partial, the first separation part of the feeding part, the acid that loop through the pipeline intercommunication, delivery pump, the heavy subtotal of alkali separate the part at last and is linked together, the utility model aims to solve the technical problem that an use device of rice bran as raw material extraction phytic acid calcium is provided, can solve the problem of the utilization of resources of rice bran.
Description
Technical field
The utility model relates to a kind of phytic acid ca extraction element, and especially a kind of device taking rice bran as raw material and extract phytic acid ca, belongs to grain chemical machinery field.
Background technology
China's yield of brown rice occupies first place in the world in recent years always, and the by product rice bran output of Rice producing is huge, but how to use as feed, and economic worth is lower.And rice bran is a kind of resource with very high economic worth, in rice bran except Rice pollard oil, rice bran protein, also be rich in multiple useful component, the content of fourth (a kind of double salt that the metal ion such as phytic acid and calcium, magnesium, potassium is formed) as Sino-Philippines in defatted rice bran can reach about 10%, at present, many grain processing enterprises do not utilize this part resource, but are processed as feed by rice bran.If be that raw material extracts luxuriant and rich with fragrance fourth and then prepares the utilization ratio that the product such as phytic acid and inositol both can improve defatted rice bran with defatted rice bran, can value-added content of product be increased again, extend rice industry chain, concerning grain processing enterprise, there is actual meaning.
Summary of the invention
Technical problem to be solved in the utility model is to provide a kind of device taking rice bran as raw material and extract phytic acid ca, can solve the problem of the utilization of resources of rice bran.
For solving the problems of the technologies described above, the technical scheme that the utility model adopts is: a kind of is that raw material extracts the device of phytic acid ca with rice bran, comprises and being connected with last separate part by the feeding part of pipeline communication, the heavy part of acid, first separate part, transferpump, the heavy part of alkali successively.
Further, feeding part comprises colloidal mill, is provided with hopper, hopper is communicated with water inlet pipe, water inlet pipe is provided with water intaking valve at the charging port of colloidal mill, is communicated with discharge nozzle at the discharging port of colloidal mill.
Further, the heavy part of acid comprises acid heavy tank, sour storage tank and urea storage tank, abrasive material import, slurry outlet and solution inlet port is provided with on tank is sunk in acid, on tank is sunk in acid, agitator is installed, abrasive material inlet communication in one end of discharge nozzle, sour storage tank and urea storage tank by pipeline communication in solution inlet port.
Further, first separate part comprises disk plate centrifuge, heavy phase storage tank and light phase temporary storage tank, the charging port of disk plate centrifuge is by pipeline and slurry outlet, the heavy phase port of disk plate centrifuge is communicated with heavy phase storage tank by pipeline, the light phase port of disk plate centrifuge is communicated with light phase temporary storage tank by pipeline, light phase temporary storage tank by pipeline communication on the entrance end of transferpump.
Further, the heavy part of alkali comprises alkali and sinks tank, the first alkali storage tank and the second alkali storage tank, on alkali sinks tank, be provided with the heavy liquid import of acid, alkali sinks liquid outlet and alkali lye import, agitator and pH value survey meter are installed on alkali sinks tank, first alkali storage tank and the second alkali storage tank are by pipeline communication in alkali lye import, and the exit end connection of transferpump is sunk in liquid import in acid.
Further, last separate part comprises tripod pendulum type batch centrifugal, and the charging port of tripod pendulum type batch centrifugal sinks liquid by pipeline and alkali and exports and be connected.
Preferably, agitator comprises a drive-motor be positioned at outside tank body, and be connected with the torsion output terminal of drive-motor with one end, the other end extends to the stir shaft in tank body, and the end winding support being positioned at one end of tank body at stir shaft is connected with stirring rake.
A kind of device taking rice bran as raw material and extract phytic acid ca that the utility model provides, achieving with defatted rice bran is the device that raw material extracts luxuriant and rich with fragrance fourth, and then provides the foundation for preparing the product such as phytic acid and inositol; Achieve the recycling of Rice producing tankage, improve the utilization ratio of defatted rice bran; This apparatus structure is reasonable, simple to operate.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model,
Fig. 2 is structural representation of the present utility model.
Embodiment
Below in conjunction with accompanying drawing, the utility model is described further:
In figure: feeding part 1, the heavy part 2 of acid, first separate part 3, alkali sinks part 4, last separate part 5, transferpump 6, agitator 7, colloidal mill 101, hopper 102, water inlet pipe 103, discharge nozzle 104, the heavy tank 201 of acid, abrasive material import 202, solution inlet port 203, slurry outlet 204, acid storage tank 205, urea storage tank 206, disk plate centrifuge 301, heavy phase storage tank 302, light phase temporary storage tank 303, alkali sinks tank 401, the heavy liquid import 402 of acid, alkali lye import 403, alkali sink liquid outlet 404, first alkali storage tank 405, second alkali storage tank 406, pH value survey meter 407, tripod pendulum type batch centrifugal 501, drive-motor 701, stir shaft 702, stirring rake 703, first discharge valve 240, acid filling valve 250, urea valve 260, water intaking valve 130, conveying valve 330, the heavy fluid valve 420 of acid, second discharge valve 440, first note alkali valve 450, second note alkali valve 460.
As illustrated in fig. 1 and 2: a kind of is that raw material extracts the device of phytic acid ca with rice bran, comprise and sink part 4 by the feeding part 1 of pipeline communication, the heavy part 2 of acid, first separate part 3, transferpump 6, alkali successively and be connected with last separate part 5.
Further, feeding part 1 comprises colloidal mill 101, is provided with hopper 102, hopper 102 is communicated with water inlet pipe 103 at the charging port of colloidal mill 101, water inlet pipe 103 is provided with water intaking valve 130, is communicated with discharge nozzle 104 at the discharging port of colloidal mill 101.
Further, the heavy part 2 of acid comprises acid heavy tank 201, sour storage tank 205 and urea storage tank 206, abrasive material import 202, slurry outlet 204 and solution inlet port 203 is provided with on tank 201 is sunk in acid, on tank 201 is sunk in acid, agitator 7 is installed, abrasive material import 202 is communicated with the one end at discharge nozzle 104, sour storage tank 205 and urea storage tank 206 by pipeline communication in solution inlet port 203.
Further, first separate part 3 comprises disk plate centrifuge 301, heavy phase storage tank 302 and light phase temporary storage tank 303, the charging port of disk plate centrifuge 301 is communicated with slurry outlet 204 by pipeline, the heavy phase port of disk plate centrifuge 301 is communicated with heavy phase storage tank 302 by pipeline, the light phase port of disk plate centrifuge 301 is communicated with light phase temporary storage tank 303 by pipeline, light phase temporary storage tank 303 by pipeline communication on the entrance end of transferpump 6.
Further, alkali sinks part 4 and comprises alkali and sink tank 401, first alkali storage tank 405 and the second alkali storage tank 406, on alkali sinks tank 401, be provided with the heavy liquid import 402 of acid, alkali sinks liquid outlet 404 and alkali lye import 403, agitator 7 and pH value survey meter 407 are installed on alkali sinks tank 401, first alkali storage tank 405 and the second alkali storage tank 406 are by pipeline communication in alkali lye import 403, and the exit end connection of transferpump 6 is sunk in liquid import 402 in acid.
Further, last separate part 5 comprises tripod pendulum type batch centrifugal 501, and the charging port of tripod pendulum type batch centrifugal 501 sinks liquid by pipeline and alkali and exports 404 and be connected.
Preferably, agitator 7 comprises a drive-motor 701 be positioned at outside tank body, be connected with the torsion output terminal of drive-motor 701 with one end, the other end extends to the stir shaft 702 in tank body, the end winding support being positioned at one end of tank body at stir shaft 702 is connected with stirring rake 703, and wherein tank body comprises the heavy tank 201 of acid and alkali and sinks tank 401.
In the utility model:
The pipeline that even sour storage tank 205 and acid are sunk between tank 201 is provided with acid filling valve 250,
The pipeline that connection urea storage tank 206 and acid are sunk between tank 201 is provided with urea valve 260,
Pipeline between connection abrasive material outlet 204 and disk plate centrifuge 301 is provided with the first discharge valve 240,
Pipeline between the light phase temporary storage tank 303 of connection and transferpump 6 is provided with and carries valve 330,
The pipeline that connection transferpump 6 and alkali sink between tank 401 is provided with the heavy fluid valve 420 of acid,
Pipeline between connection acid solution outlet 404 and tripod pendulum type batch centrifugal 501 is provided with the second discharge valve 440,
The pipeline that connection first alkali storage tank 405 and alkali sink between tank 401 is provided with the first note alkali valve 450,
The pipeline that connection second alkali storage tank 406 and alkali sink between tank 401 is provided with the second note alkali valve 460.
Before this device does not enter material, filling 2% dilute hydrochloric acid solution in sour storage tank 205 in advance, in urea storage tank 206, filling 1% urea soln, is filled with 10% aqua calcis, the sodium hydroxide solution of 20% concentration of annotating in the second alkali storage tank 406 tank in the first alkali storage tank 405.
Working process of the present utility model is as follows:
The first step, startup colloidal mill 101, open the water intaking valve 130 on water inlet pipe 103, close the first discharge valve 240, defatted rice bran is dropped in hopper 102, the slurry of milled flows in the heavy tank 201 of acid along feed-pipe, opens the agitator 7 on the heavy tank 201 of acid, opens acid filling valve 250 and urea valve 260 simultaneously, and sink tank 201 to acid by a certain percentage and inject 2% dilute hydrochloric acid solution and 1% urea soln, lixiviate 3 hours.
Second step, lixiviate are after 3 hours, start disk plate centrifuge 301 and transferpump 6, open the first discharge valve 240, conveying valve 330 and acid and sink fluid valve 420, acidleach material is separated, heavy phase material after separation flow into heavy phase storage tank 302, and light phase materials inflow is delivered to alkali through light phase temporary storage tank 303 and transferpump 6 and sunk in tank 401.
The agitator 7 that 3rd step, unlatching alkali sink on tank 401, open the first note alkali valve 450, first use 10% aqua calcis neutralizing acid immersion liquid in the first alkali storage tank 405, alkali can be observed by pH value survey meter 407 and sink the pH value of material in tank 401, pH value is reduced to about 3.5, close the first note alkali valve 450, open the second note alkali valve 460, the sodium hydroxide solution of 20% concentration in the second alkali storage tank 406 is slowly added, until pH value is about 6.0, close the agitator 7 that alkali sinks on tank 401, leave standstill 2 hours.
4th step, after standing 2 hours, open the second discharge valve 440, the precipitation of being sunk by alkali bottom tank 401 is put into tripod pendulum type batch centrifugal 501 and is dewatered, and just can obtain phytic acid ca and to wet crude product.
Claims (7)
1. be the device that raw material extracts phytic acid ca with rice bran, it is characterized in that: comprise and being connected with last separate part (5) by the feeding part (1) of pipeline communication, sour heavy part (2), first separate part (3), transferpump (6), alkali heavy partly (4) successively.
2. a kind of device taking rice bran as raw material and extract phytic acid ca according to claim 1, it is characterized in that: feeding part (1) comprises colloidal mill (101), at the charging port of colloidal mill (101), hopper (102) is installed, hopper (102) is communicated with water inlet pipe (103), water inlet pipe (103) is provided with water intaking valve, is communicated with discharge nozzle (104) at the discharging port of colloidal mill (101).
3. a kind of device taking rice bran as raw material and extract phytic acid ca according to claim 2, it is characterized in that: the heavy part (2) of acid comprises acid heavy tank (201), sour storage tank (205) and urea storage tank (206), abrasive material import (202), slurry outlet (204) and solution inlet port (203) is provided with on tank (201) is sunk in acid, on tank (201) is sunk in acid, agitator (7) is installed, abrasive material import (202) be communicated with in one end of discharge nozzle (104), sour storage tank (205) and urea storage tank (206) by pipeline communication in solution inlet port (203).
4. a kind of device taking rice bran as raw material and extract phytic acid ca according to claim 3, it is characterized in that: first separate part (3) comprises disk plate centrifuge (301), heavy phase storage tank (302) and light phase temporary storage tank (303), the charging port of disk plate centrifuge (301) is communicated with slurry outlet (204) by pipeline, the heavy phase port of disk plate centrifuge (301) is communicated with heavy phase storage tank (302) by pipeline, the light phase port of disk plate centrifuge (301) is communicated with light phase temporary storage tank (303) by pipeline, light phase temporary storage tank (303) by pipeline communication on the entrance end of transferpump (6).
5. a kind of device taking rice bran as raw material and extract phytic acid ca according to claim 4, it is characterized in that: the heavy part (4) of alkali comprises alkali and sinks tank (401), first alkali storage tank (405) and the second alkali storage tank (406), the heavy liquid import (402) of acid is provided with on alkali sinks tank (401), alkali sink liquid outlet (404) and alkali lye import (403), agitator (7) and pH value survey meter (407) are installed on alkali sinks tank (401), first alkali storage tank (405) and the second alkali storage tank (406) by pipeline communication in alkali lye import (403), the exit end connection of transferpump (6) is sunk in liquid import (402) in acid.
6. a kind of device taking rice bran as raw material and extract phytic acid ca according to claim 5, it is characterized in that: last separate part (5) comprises tripod pendulum type batch centrifugal (501), the charging port of tripod pendulum type batch centrifugal (501) sinks liquid by pipeline and alkali and exports (404) and be connected.
7. a kind of device taking rice bran as raw material and extract phytic acid ca according to any one of claim 3 to 6, it is characterized in that: agitator (7) comprises one and is positioned at tank body (201,401) outer drive-motor (701), be connected with the torsion output terminal of one end with drive-motor (701), the other end extends to tank body (201,401) stir shaft (702) in, is connected with stirring rake (703) at the end winding support of one end that stir shaft (702) is positioned in tank body (201,401).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520907368.6U CN205115342U (en) | 2015-11-16 | 2015-11-16 | Use device of rice bran as raw material extraction phytic acid calcium |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520907368.6U CN205115342U (en) | 2015-11-16 | 2015-11-16 | Use device of rice bran as raw material extraction phytic acid calcium |
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| Publication Number | Publication Date |
|---|---|
| CN205115342U true CN205115342U (en) | 2016-03-30 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520907368.6U Expired - Fee Related CN205115342U (en) | 2015-11-16 | 2015-11-16 | Use device of rice bran as raw material extraction phytic acid calcium |
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| CN (1) | CN205115342U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107050922A (en) * | 2017-06-13 | 2017-08-18 | 江苏北松健康产业有限公司 | A kind of traditional Chinese medicine extraction alkali process device and traditional Chinese medicine extraction system |
-
2015
- 2015-11-16 CN CN201520907368.6U patent/CN205115342U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107050922A (en) * | 2017-06-13 | 2017-08-18 | 江苏北松健康产业有限公司 | A kind of traditional Chinese medicine extraction alkali process device and traditional Chinese medicine extraction system |
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| 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: 20160330 Termination date: 20181116 |