CN208050190U - A kind of maize germ piece-rate system - Google Patents
A kind of maize germ piece-rate system Download PDFInfo
- Publication number
- CN208050190U CN208050190U CN201721896167.6U CN201721896167U CN208050190U CN 208050190 U CN208050190 U CN 208050190U CN 201721896167 U CN201721896167 U CN 201721896167U CN 208050190 U CN208050190 U CN 208050190U
- Authority
- CN
- China
- Prior art keywords
- level
- cyclone
- germ
- pipe
- connect
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Landscapes
- Cyclones (AREA)
Abstract
The utility model is related to a kind of maize germ piece-rate systems, specially the discharge port of level-one degerming mill is connect with the main pipeline A of level-one germ cyclone, main pipeline A is equipped with main valve A, main pipeline A is connect by branch pipe A with the cyclone pipe A of level-one germ cyclone, branch pipe A is equipped with minor valve A, the overflow pipe A of level-one germ cyclone is connect with plumule collecting tank, the underflow pipe A of level-one germ cyclone is connect with the feed inlet of two level degerming mill, the discharge port of two level degerming mill is connect with the main pipeline B of two level germ cyclone, main pipeline B is equipped with main valve B, main pipeline B is connect by branch pipe B with the cyclone pipe B of two level germ cyclone, the overflow pipe B of two level germ cyclone is connect with the feed inlet of level-one germ cyclone, the underflow pipe B of two level germ cyclone is connect with fiber collection tank.The utility model improves the stability of germ cyclone, and eddy flow effect is good, and the plumule purity of extraction is high.
Description
Technical field
The utility model is related to a kind of maize germ piece-rate systems, belong to corn oil preparing technical field.
Background technology
Production of corn starch machining process includes：Purification of raw materials, immersion, broken, germ separation, fine grinding, fiber are washed
Wash, Protein Separation, dehydration, drying, packaging and storage.Plumule is broken apart general by two procedures, then carries out fine grinding again and adds
Work.Then existing germ separation broken process, usually level-one are broken to be detached, then two-stage crushing detaches again, level-one screening point
Slurry is directly entered next process under sieve from after, and plumule is broken apart to be not thorough, and the oil yield of plumule is reduced.
Utility model content
The utility model aims to solve the problem that the above problem, provides a kind of maize germ piece-rate system, and the utility model improves
The stability of germ cyclone, eddy flow effect is good, and the plumule purity of extraction is high.The technical solution of the utility model is as follows：
A kind of maize germ piece-rate system, including level-one degerming mill, level-one germ cyclone, two level degerming mill and two level embryo
Bud cyclone；The discharge port of level-one degerming mill is connect by pipeline with the main pipeline A of level-one germ cyclone, is set on main pipeline A
There are main valve A, main pipeline A to be connect with the cyclone pipe A of level-one germ cyclone by branch pipe A, branch pipe A is equipped with minor valve A, and one
The overflow pipe A of grade germ cyclone is connect by pipeline with plumule collecting tank, and the underflow pipe A of level-one germ cyclone passes through pipe
Road is connect with the feed inlet of two level degerming mill, the main pipeline that the discharge port of two level degerming mill passes through pipeline and two level germ cyclone
B connections, main pipeline B are equipped with main valve B, and main pipeline B is connect by branch pipe B with the cyclone pipe B of two level germ cyclone, two level
The overflow pipe B of germ cyclone is connect by pipeline with the feed inlet of level-one germ cyclone, the underflow of two level germ cyclone
Pipe B is connect with fiber collection tank.
Based on the above technical solution, the level-one germ cyclone is made of the cyclone pipe A of 2-5 parallel connections；It is preferred that
For 3 cyclone pipe A in parallel；This structure improves the separative efficiency of plumule.
Based on the above technical solution, the two level germ cyclone is made of the cyclone pipe B of 2-5 parallel connections；It is preferred that
For 2 cyclone pipe B in parallel；This structure makes the oil yield of the separation rate for improving plumule and corn.
Based on the above technical solution, between in the level-one degerming mill and two level degerming mill between Moving plate and quiet disk
Gap is 20-35mm；Preferably, gap 28mm；This structure is conducive to corn being crushed, and does not damage plumule.
The utility model has the following advantages that：
Corn can get more complete plumule, the supervisor of germ cyclone after degerming mill in the utility model is broken
Road is equipped with main valve, and each feed-inputing branched pipe when carrying out cyclonic separation, only need to debug main valve, by main valve to minor valve is equipped with
Door is uniformly controlled, and enhances the stability of germ cyclone, eddy flow effect is good；It is returned again by the plumule of two level germ cyclone
It is detached to level-one germ cyclone, improves the purity of plumule；The utility model improves the purity and corn of plumule
The oil yield of plumule.
Description of the drawings
FIG. 1 is a schematic structural view of the utility model.
Symbol description
1. level-one degerming mill, 2. level-one germ cyclones, 3. two level degerming mills, 4. two level germ cyclones, 5. main pipelines
A, 6. main valve A, 7. branch pipe A, 8. minor valve A, 9. cyclone pipe A, 10. overflow pipe A, 11. underflow pipe A, 12. main pipeline B, 13.
Main valve B, 14. branch pipe B, 15. minor valve B, 16. cyclone pipe B, 17. overflow pipe B, 18. underflow pipe B, 19. plumule collecting tanks,
20. fiber collection tank.
Specific implementation mode
The utility model is described in further detail with example below in conjunction with the accompanying drawings：
Embodiment 1
A kind of maize germ piece-rate system, as shown in Figure 1, piece-rate system includes level-one degerming mill 1, level-one plumule eddy flow
Device 2, two level degerming mill 3 and two level germ cyclone 4；The discharge port of level-one degerming mill 1 passes through pipeline and level-one germ cyclone 2
The connections of main pipeline A 5, main pipeline A 5 is equipped with main valve A 6, and main pipeline A 5 passes through branch pipe A 7 and level-one germ cyclone
2 connections of cyclone pipe A 9, branch pipe A 7 are equipped with minor valve A 8, and the overflow pipe A 10 of level-one germ cyclone 2 passes through pipeline
It is connect with plumule collecting tank 19, the underflow pipe A 11 of level-one germ cyclone 2 is connected by the feed inlet of pipeline and two level degerming mill 3
It connects, the discharge port of two level degerming mill 3 is connect by pipeline with the main pipeline B 12 of two level germ cyclone 4, on main pipeline B 12
Equipped with main valve B 13, main pipeline B 12 is connect by branch pipe B 14 with the cyclone pipe B 16 of two level germ cyclone 4, two level embryo
The overflow pipe B 17 of bud cyclone 4 is connect by pipeline with the feed inlet of level-one germ cyclone 2, two level germ cyclone 4
Underflow pipe B 18 is connect with fiber collection tank 20.
Embodiment 2
On the basis of embodiment 1, as shown in Figure 1, the level-one germ cyclone 2 is by 3 cyclone pipe A groups in parallel
At；The two level germ cyclone 4 is made of 2 cyclone pipe B in parallel；Moving plate in the level-one degerming mill 1 and two level degerming mill 3
Gap between quiet disk is 28mm.
The utility model is illustrated by way of example above, but the utility model is not limited to above-mentioned specific implementation
Example, all ranges that the requires of the utility model protection is belonged to based on any changes or modifications that the utility model is done.
Claims (7)
1. a kind of maize germ piece-rate system, which is characterized in that piece-rate system include level-one degerming mill, level-one germ cyclone,
Two level degerming mill and two level germ cyclone；The main pipeline that the discharge port of level-one degerming mill passes through pipeline and level-one germ cyclone
A connections, main pipeline A are equipped with main valve A, and main pipeline A is connect by branch pipe A with the cyclone pipe A of level-one germ cyclone, branch pipe
A is equipped with minor valve A, and the overflow pipe A of level-one germ cyclone is connect by pipeline with plumule collecting tank, level-one plumule eddy flow
The underflow pipe A of device is connect by pipeline with the feed inlet of two level degerming mill, and the discharge port of two level degerming mill passes through pipeline and two level
The main pipeline B connections of germ cyclone, main pipeline B are equipped with main valve B, and main pipeline B passes through branch pipe B and two level germ cyclone
Cyclone pipe B connections, the overflow pipe B of two level germ cyclone connect by pipeline with the feed inlet of level-one germ cyclone, two
The underflow pipe B of grade germ cyclone is connect with fiber collection tank.
2. a kind of maize germ piece-rate system according to claim 1, which is characterized in that the level-one germ cyclone by
The cyclone pipe A compositions of 2-5 parallel connections.
3. a kind of maize germ piece-rate system according to claim 2, which is characterized in that the level-one germ cyclone by
3 cyclone pipe A compositions in parallel.
4. a kind of maize germ piece-rate system according to claim 1, which is characterized in that the two level germ cyclone by
The cyclone pipe B compositions of 2-5 parallel connections.
5. a kind of maize germ piece-rate system according to claim 4, which is characterized in that the two level germ cyclone by
2 cyclone pipe B compositions in parallel.
6. a kind of maize germ piece-rate system according to claim 1, which is characterized in that the level-one degerming mill and two level
Gap in degerming mill between Moving plate and quiet disk is 20-35mm.
7. a kind of maize germ piece-rate system according to claim 1, which is characterized in that the level-one degerming mill and two level
Gap in degerming mill between Moving plate and quiet disk is 28mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721896167.6U CN208050190U (en) | 2017-12-29 | 2017-12-29 | A kind of maize germ piece-rate system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721896167.6U CN208050190U (en) | 2017-12-29 | 2017-12-29 | A kind of maize germ piece-rate system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208050190U true CN208050190U (en) | 2018-11-06 |
Family
ID=63995343
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721896167.6U Active CN208050190U (en) | 2017-12-29 | 2017-12-29 | A kind of maize germ piece-rate system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208050190U (en) |
-
2017
- 2017-12-29 CN CN201721896167.6U patent/CN208050190U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103554277B (en) | A kind of production loading method of W-Gum | |
| CN103691538B (en) | A kind of grinding classification system of Ore | |
| CN106861940A (en) | Multi-product water-only cyclone is selected in a kind of underflow again | |
| CN101838335B (en) | Starch separation method and device | |
| CN202105799U (en) | Drum-type grain winnowing machine | |
| CN1962072A (en) | Closed circuit grinding classification system consisting of cyclone and grate discharge ball mill | |
| CN204263398U (en) | A kind of Super Absorbent Polymer Particles tinuous production | |
| CN208050190U (en) | A kind of maize germ piece-rate system | |
| CN101863988B (en) | Method and equipment for improving starch quality and protein yield | |
| CN211587110U (en) | Fine sand extractor capable of improving fine sand dehydration efficiency | |
| CN105367671A (en) | Preparation method of potato starch | |
| CN204656753U (en) | A kind of system guaranteeing fine coal properties matter cyclone pan feeding flow and pressure stability | |
| CN202626070U (en) | Corn starch cleaning separator | |
| CN203540734U (en) | Recovery device of refractory coal slime with high ash content | |
| CN208482062U (en) | The pretreatment unit of weight granule foreign in feed processing waste water | |
| CN205146475U (en) | Concentrated swirler of screen cloth formula | |
| CN205146476U (en) | Corn germ's separation drying system | |
| CN201543579U (en) | Scrap-removing and impurity-extracting device of pulp in groove | |
| CN104623934A (en) | Pre-grading thickener | |
| CN204918455U (en) | Refined and classification equipment of starch | |
| CN200974038Y (en) | Hydrocyclone - lattice ball mill type graded closed circuit mine-grinding system | |
| CN104494001A (en) | Continuous production system of high-hydroscopicity resin particles | |
| CN210103802U (en) | Starch production corn pulp grinds sieve process secondary and carries thick liquid processing apparatus | |
| CN104098709B (en) | A kind of potato starch process for cleanly preparing | |
| CN103506212A (en) | Novel coarse coal interference bed separator |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |