CN208724813U - A kind of system with peanut meal coproduction peanut polysaccharide and peanut concentrated protein - Google Patents
A kind of system with peanut meal coproduction peanut polysaccharide and peanut concentrated protein Download PDFInfo
- Publication number
- CN208724813U CN208724813U CN201820498694.XU CN201820498694U CN208724813U CN 208724813 U CN208724813 U CN 208724813U CN 201820498694 U CN201820498694 U CN 201820498694U CN 208724813 U CN208724813 U CN 208724813U
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- China
- Prior art keywords
- peanut
- polysaccharide
- protein
- pond
- dissolving tank
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- Expired - Fee Related
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- Peptides Or Proteins (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Abstract
The utility model belongs to agricultural engineering field, disclose a kind of system with peanut meal coproduction peanut polysaccharide and peanut concentrated protein, it is provided with dissolving tank, dissolving tank and flour mill are clamped, dissolving tank is welded with biological enzyme adding tube, switch valve, water inlet pipe, thermometer, and dissolution bottom of pond portion is connected with filter screen；Dissolution bottom of pond portion is connect by screw thread with conduit；Dissolution bottom of pond portion is welded with residue and filters out pipe；Polysaccharide concentration basin and polysaccharide crystallization bottom of pond portion have heater；Protein compression bottom of pond portion is provided with filter.Peanut meal is successively carried out two kinds of processing in the same apparatus and obtains the solution containing polysaccharide and polypeptide by the utility model, the efficiency that subsequent purification program substantially increases operation is carried out again, while can carry out individually control increase filter in extracting protein processes to each program can greatly improve Protein Extraction efficiency；Carry out degree is reacted equipped with thermometer monitors simultaneously, it is easy to clean to be equipped with water inlet pipe.
Description
Technical field
The utility model belongs to agricultural engineering field, more particularly to peanut meal coproduction peanut polysaccharide and peanut concentrated protein
System.
Background technique
Currently, the prior art commonly used in the trade is such that
Currently, peanut meal is the byproduct using the peanut that shells as raw material, after extracted grease, in filbert or deep brown
Color has light peanut fragrance, and shape is small bulk or powdered, contains a small amount of peanut shell.Its yield is big, and source is wide, and price is low,
And wherein containing 30%~50% peanut protein, and contain polysaccharide, most of peanut meal is used as feed, and some is even
It abandons as waste material, not only results in waste of resources, but also pollute environment.The extraction protein that peanut meal equipment can only be single at present
Or polysaccharide, extraction efficiency is low, and program is complicated during protein and polysaccharide are collected.
In conclusion problem of the existing technology is:
The extraction protein or polysaccharide that peanut meal equipment can only be single at present, extraction efficiency is low, in protein and polysaccharide
Program is complicated during collection.
Summary of the invention
In view of the problems of the existing technology, the utility model provides a kind of peanut meal coproduction peanut polysaccharide and peanut
The system of protein concentrate.
The utility model is realized in this way a kind of system with peanut meal coproduction peanut polysaccharide and peanut concentrated protein,
It is characterized in that, the system with peanut meal coproduction peanut polysaccharide and peanut concentrated protein includes: biological enzyme adding tube, chemistry
Reagent add pipe, polysaccharide crystallizing pond, heater, polysaccharide concentration basin, filter, protein be precipitated pond, protein compression pond, valve,
Conduit, dissolving tank, flour mill, filter screen, water inlet pipe, thermometer, switch valve, residue filter out pipe.
The dissolving tank and flour mill are clamped, and the dissolving tank is welded with biological enzyme adding tube, switch valve, water inlet pipe, temperature
Degree meter, the dissolution bottom of pond portion are connected with filter screen, and the dissolution bottom of pond portion is connect by screw thread with conduit；
The dissolution bottom of pond portion filters out pipe with residue by welding and connect；
The polysaccharide concentration basin and polysaccharide crystallization bottom of pond portion have heater；
The protein compression bottom of pond portion of working as is provided with filter；
The protein compression pond and polysaccharide concentration basin are connected with chemical reagent adding tube.
Further, valve is connected on each section of conduit.
Further, between the dissolving tank and protein compression pond, polysaccharide concentration basin, protein compression pond and protein are analysed
Out between pond, connected between polysaccharide concentration basin and polysaccharide crystallizing pond by conduit.
The advantages of the utility model and good effect are as follows:
Peanut meal is successively carried out two kinds of processing in the same apparatus and obtains the solution containing polysaccharide and polypeptide by the device, then
The efficiency that subsequent purification program substantially increases operation is carried out, while individually control can be carried out to each program and extracting protein
Protein Extraction efficiency can be greatly improved by increasing filter in the process.Carry out degree is reacted equipped with thermometer monitors simultaneously,
It is easy to clean that with residue pipe is filtered out equipped with water inlet pipe.
Detailed description of the invention
Fig. 1 is the system knot provided by the embodiment of the utility model with peanut meal coproduction peanut polysaccharide and peanut concentrated protein
Structure schematic diagram.
Fig. 2 is that the utility model embodiment provides filter screen connection schematic diagram.
In figure: 1, biological enzyme adding tube；2, chemical reagent adds pipe；3, polysaccharide crystallizing pond；4, heater；5, polysaccharide is concentrated
Pond；6, filter；7, pond is precipitated in protein；8, protein compression pond；9, valve；10, conduit；11, dissolving tank；12, it is milled
Machine；13, filter screen；14, water inlet pipe；15, thermometer；16, switch valve；17, residue filters out pipe.
Specific embodiment
For the invention, features and effects that can further appreciate that the utility model, the following examples are hereby given, and cooperates
Detailed description are as follows for attached drawing.
The structure of the utility model is explained in detail with reference to the accompanying drawing.
As depicted in figs. 1 and 2, provided by the embodiment of the utility model to use peanut meal coproduction peanut polysaccharide and peanut concentrate egg
White system includes: that biological enzyme adding tube 1, chemical reagent add pipe 2, polysaccharide crystallizing pond 3, heater 4, polysaccharide concentration basin 5, filtering
Pond 7, protein compression pond 8, valve 9, conduit 10, dissolving tank 11, flour mill 12, filter screen 13 is precipitated in device 6, protein；Water inlet
Pipe 14, thermometer 15, switch valve 16, residue filter out pipe 17.
The dissolving tank 11 is clamped with flour mill 12, the dissolving tank 11 be welded with biological enzyme adding tube 1, switch valve 16,
Water inlet pipe 14, thermometer 15,11 bottom of dissolving tank are connected with filter screen 13, and 11 bottom of dissolving tank passes through screw thread and leads
Pipe 10 connects；
11 bottom of dissolving tank filters out pipe 17 with residue by welding and connect；
The polysaccharide concentration basin 5 has heater 4 with 3 bottom of polysaccharide crystallizing pond；
8 bottom of protein compression pond of working as is provided with filter 6；
The protein compression pond 8 is connected with chemical reagent adding tube 2 with polysaccharide concentration basin 5.
Valve 9 is connected on each section of conduit 10.
Between the dissolving tank 1 and protein compression pond 8, polysaccharide concentration basin 5, protein compression pond 8 and protein are precipitated
Between pond 7, connected between polysaccharide concentration basin 5 and polysaccharide crystallizing pond 3 by conduit.
Working principle of the utility model is: peanut meal powder is broken into last investment dissolving tank by flour mill 12 by the present apparatus
11, biological enzyme adding tube 1 increase separately protease by solution filter screen 13 filtering after open valve 9 by conduit 10 into
Enter protein compression pond 8, is added after chemical reagent is added in pipe 2 by chemical reagent and improve protein concentration, subsequently into protein
Pond 7 is precipitated to be precipitated, protein is then extracted by filter 6 again, after releasing protein solution, polysaccharase is added.Make
It enters polysaccharide concentration basin 5, carries out heating concentration, final output to polysaccharide knot by chemical reagent reconciliation post-heater 4 is added
Brilliant pond 3 is crystallized after heating.Further, carry out degree is reacted by observation 15 temperature monitoring of thermometer, after completion of the reaction
It can be filled the water and be cleaned by water inlet pipe 14, unreacted residue, which is filtered out pipe 17 by residue, by turning on the switch valve 16 filters out.
Peanut meal is successively carried out two kinds of processing in the same apparatus and obtains the solution containing polysaccharide and polypeptide by the device, then
The efficiency that subsequent purification program substantially increases operation is carried out, while individually control can be carried out to each program and extracting protein
Protein Extraction efficiency can be greatly improved by increasing filter in the process.Carry out degree is reacted equipped with thermometer monitors simultaneously,
It is easy to clean that with residue pipe is filtered out equipped with water inlet pipe.
The above is only the preferred embodiment to the utility model, is not made in any form to the utility model
Limitation, it is all according to the technical essence of the utility model any simple modification made to the above embodiment, equivalent variations with
Modification, is all within the scope of the technical scheme of the utility model.
Claims (3)
1. a kind of system with peanut meal coproduction peanut polysaccharide and peanut concentrated protein, which is characterized in that the peanut meal joins
The system of yield peanut polysaccharide and peanut concentrated protein is provided with dissolving tank；
Dissolving tank and flour mill are clamped；Dissolving tank is welded with biological enzyme adding tube, switch valve, water inlet pipe, thermometer；Dissolving tank bottom
Portion is connected with filter screen；Dissolution bottom of pond portion is connect by screw thread with conduit；
Dissolution bottom of pond portion filters out pipe with residue by welding and connect；
Polysaccharide concentration basin and polysaccharide crystallization bottom of pond portion are equipped with heater；
When protein compression bottom of pond portion is equipped with filter；
Protein compression pond and polysaccharide concentration basin are connected with chemical reagent adding tube.
2. using the system of peanut meal coproduction peanut polysaccharide and peanut concentrated protein as described in claim 1, which is characterized in that each section
Valve is connected on the conduit.
3. using the system of peanut meal coproduction peanut polysaccharide and peanut concentrated protein as described in claim 1, which is characterized in that described
Between dissolving tank and protein compression pond, polysaccharide concentration basin, protein compression pond and protein are precipitated between pond, polysaccharide concentration basin
It is connect between polysaccharide crystallizing pond by conduit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820498694.XU CN208724813U (en) | 2018-04-10 | 2018-04-10 | A kind of system with peanut meal coproduction peanut polysaccharide and peanut concentrated protein |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820498694.XU CN208724813U (en) | 2018-04-10 | 2018-04-10 | A kind of system with peanut meal coproduction peanut polysaccharide and peanut concentrated protein |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208724813U true CN208724813U (en) | 2019-04-12 |
Family
ID=66021664
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820498694.XU Expired - Fee Related CN208724813U (en) | 2018-04-10 | 2018-04-10 | A kind of system with peanut meal coproduction peanut polysaccharide and peanut concentrated protein |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208724813U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111808163A (en) * | 2020-07-29 | 2020-10-23 | 江西天禹科技协同创新有限公司 | Purification equipment for protein polypeptide in peanut meal |
-
2018
- 2018-04-10 CN CN201820498694.XU patent/CN208724813U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111808163A (en) * | 2020-07-29 | 2020-10-23 | 江西天禹科技协同创新有限公司 | Purification equipment for protein polypeptide in peanut meal |
| CN111808163B (en) * | 2020-07-29 | 2021-12-07 | 江西天禹科技协同创新有限公司 | Purification equipment for protein polypeptide in peanut meal |
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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: 20190412 Termination date: 20200410 |