CN204157588U - A kind of rice yeast albumen powder production line - Google Patents
A kind of rice yeast albumen powder production line Download PDFInfo
- Publication number
- CN204157588U CN204157588U CN201420615421.0U CN201420615421U CN204157588U CN 204157588 U CN204157588 U CN 204157588U CN 201420615421 U CN201420615421 U CN 201420615421U CN 204157588 U CN204157588 U CN 204157588U
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- charging aperture
- discharging opening
- machine
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- storehouse
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Abstract
A kind of rice yeast albumen powder production line, it comprises beater (3), conveying worm (4), wet feed storehouse (5), siccative storehouse (6), first blending bunker (7), bacterium flow container (8), mixer (9), fermentation cabin (10), fermenting and turning machine (11), fermentation discharging machine (13), belt conveyor (14), dryer (15), cooler (16), feeding machine (17), pulverizer (18) and packing machine (19), the discharging opening of beater (3) communicates with the charging aperture of conveying worm 4, the discharging opening of conveying worm 4 is positioned at above the charging aperture of wet feed storehouse (5), the discharge outlet of wet feed storehouse (5) and siccative storehouse (6) is respectively equipped with measuring pump (6-1), the utility model advantage is: the yeast albumen powder quality that this production line is produced is good, efficiency is high, large-scale production can be met.
Description
Technical field
The utility model relates to rice high protein production line field, is specifically related to a kind of rice yeast albumen powder production line.
Background technology
at present, rice is one of main meals of China, and its nutritional quality is lower.The rice protein extracted from rice has the features such as low allergy, amino acid balance, mainly comprises glutelin, alcohol soluble protein, albumin, globulin.Research shows, the bioavailable efficiency of protein depends primarily on its digestive efficiency in alimentary canal, and therefore, how improving rice protein content, strengthening its protein digestibility efficiency is improve the key point of rice protein quality and bioavailable efficiency thereof.And existing most rice high protein major part is on the market all import, edible cost is higher.
Utility model content
The purpose of this utility model is exactly at present, and rice is one of main meals of China, and its nutritional quality is lower.The rice protein extracted from rice has the features such as low allergy, amino acid balance, mainly comprises glutelin, alcohol soluble protein, albumin, globulin.Research shows, the bioavailable efficiency of protein depends primarily on its digestive efficiency in alimentary canal, and therefore, how improving rice protein content, strengthening its protein digestibility efficiency is improve the key point of rice protein quality and bioavailable efficiency thereof.And existing most rice high protein major part is on the market all import, the deficiency that edible cost is higher, and a kind of rice yeast albumen powder production line is provided.
The utility model comprises beater, conveying worm, wet feed storehouse, siccative storehouse, first blending bunker, bacterium flow container, mixer, fermentation cabin, fermenting and turning machine, fermentation discharging machine, belt conveyor, dryer, cooler, feeding machine, pulverizer and packing machine, the discharging opening of beater communicates with the charging aperture of conveying worm, the discharging opening of conveying worm is positioned at above the charging aperture in wet feed storehouse, the discharge outlet in wet feed storehouse and siccative storehouse is respectively equipped with measuring pump, the discharging opening in wet feed storehouse and siccative storehouse communicates with the charging aperture of first blending bunker, the discharging opening of first blending bunker and bacterium flow container communicates with the charging aperture of mixer, material is evacuated in fermentation cabin by high pressure positive blower by the discharging opening of mixer, fermenting and turning machine and fermentation discharging machine are arranged in fermentation cabin respectively, belt conveyor is positioned at the discharge outlet of fermentation cabin, the discharge end of belt conveyor is positioned at the charging aperture place of dryer, dryer discharging opening communicates with the charging aperture of cooler, the discharging opening of cooler communicates with the charging aperture of feeding machine, the discharging opening of feeding machine communicates with the charging aperture of pulverizer, the discharging opening of pulverizer communicates with the charging aperture of packing machine.
The utility model advantage is: this production line, and the yeast albumen powder quality produced is good, efficiency is high, can meet large-scale production.
accompanying drawing explanation
Fig. 1 is the utility model structural representation.
Detailed description of the invention
As shown in Figure 1, the utility model comprises beater 3, conveying worm 4, wet feed storehouse 5, siccative storehouse 6, first blending bunker 7, bacterium flow container 8, mixer 9, fermentation cabin 10, fermenting and turning machine 11, fermentation discharging machine 13, belt conveyor 14, dryer 15, cooler 16, feeding machine 17, pulverizer 18 and packing machine 19, the discharging opening of beater 3 communicates with the charging aperture of conveying worm 4, the discharging opening of conveying worm 4 is positioned at above the charging aperture in wet feed storehouse 5, the discharge outlet in wet feed storehouse 5 and siccative storehouse 6 is respectively equipped with measuring pump 6-1, the discharging opening in wet feed storehouse 5 and siccative storehouse 6 communicates with the charging aperture of first blending bunker 7, the discharging opening of first blending bunker 7 and bacterium flow container 8 communicates with the charging aperture of mixer 9, material is evacuated in fermentation cabin 10 by high pressure positive blower by the discharging opening of mixer 9, fermenting and turning machine 11 and fermentation discharging machine 13 are arranged in fermentation cabin 10 respectively, belt conveyor 14 is positioned at the discharge outlet of fermentation cabin 10, the discharge end of belt conveyor 14 is positioned at the charging aperture place of dryer 15, dryer 15 discharging opening communicates with the charging aperture of cooler 16, the discharging opening of cooler 16 communicates with the charging aperture of feeding machine 17, the discharging opening of feeding machine 17 communicates with the charging aperture of pulverizer 18, the discharging opening of pulverizer 18 communicates with the charging aperture of packing machine 19.
Working method: first, rice wet slag after immersion is squeezed into and breaks up to beater 3, after having broken up, the wet rice residue after breaing up is delivered in wet feed storehouse 5 by conveying worm 4, wet rice residue in wet feed storehouse 5 and the dry rice residue in siccative storehouse 6 add in fixing amount to first blending bunker 7 respectively by measuring pump 6-1, mixed rice in first blending bunker 7 and the bacterium liquid in bacterium flow container 8 are added to respectively in mixer 9 and are uniformly mixed, after stirring completes, ferment in the fermentation cabin 10 of the rice containing bacterium liquid in mixer 9 being pumped by high pressure positive blower, while fermentation, fermenting and turning machine 11 carries out turning, after having fermented (being now yeast albumen powder), yeast albumen powder is delivered on belt conveyor 14 by the discharging opening of fermentation cabin 10 by fermentation discharging machine 13, yeast albumen powder is delivered in dryer 15 and dries by belt conveyor 14 again, after oven dry completes, cool material is delivered in cooler 16, after having cooled, be delivered to pulverizer 18 by feeding machine 17 again to pulverize, finally, the yeast albumen powder pulverized is delivered in packing machine 19 and packs.
Claims (1)
1. a rice yeast albumen powder production line, it is characterized in that it comprises beater (3), conveying worm (4), wet feed storehouse (5), siccative storehouse (6), first blending bunker (7), bacterium flow container (8), mixer (9), fermentation cabin (10), fermenting and turning machine (11), fermentation discharging machine (13), belt conveyor (14), dryer (15), cooler (16), feeding machine (17), pulverizer (18) and packing machine (19), the discharging opening of beater (3) communicates with the charging aperture of conveying worm 4, the discharging opening of conveying worm 4 is positioned at above the charging aperture of wet feed storehouse (5), the discharge outlet of wet feed storehouse (5) and siccative storehouse (6) is respectively equipped with measuring pump (6-1), the discharging opening of wet feed storehouse (5) and siccative storehouse (6) communicates with the charging aperture of first blending bunker (7), the discharging opening of first blending bunker (7) and bacterium flow container (8) communicates with the charging aperture of mixer (9), material is evacuated in fermentation cabin (10) by high pressure positive blower by the discharging opening of mixer (9), fermenting and turning machine (11) and fermentation discharging machine (13) are arranged in fermentation cabin (10) respectively, belt conveyor (14) is positioned at the discharge outlet of fermentation cabin (10), the discharge end of belt conveyor (14) is positioned at the charging aperture place of dryer (15), dryer (15) discharging opening communicates with the charging aperture of cooler (16), the discharging opening of cooler (16) communicates with the charging aperture of feeding machine (17), the discharging opening of feeding machine (17) communicates with the charging aperture of pulverizer (18), the discharging opening of pulverizer (18) communicates with the charging aperture of packing machine (19).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420615421.0U CN204157588U (en) | 2014-10-23 | 2014-10-23 | A kind of rice yeast albumen powder production line |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420615421.0U CN204157588U (en) | 2014-10-23 | 2014-10-23 | A kind of rice yeast albumen powder production line |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204157588U true CN204157588U (en) | 2015-02-18 |
Family
ID=52531335
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420615421.0U Expired - Fee Related CN204157588U (en) | 2014-10-23 | 2014-10-23 | A kind of rice yeast albumen powder production line |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204157588U (en) |
-
2014
- 2014-10-23 CN CN201420615421.0U patent/CN204157588U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee |
Owner name: HUBEI JINGYUANSHAN BIOLOGICAL TECHNOLOGY CO., LTD. Free format text: FORMER NAME: HUBEI JINGYUANSHAN BIOLOGICAL TECHNOLOGY LTD. |
|
| CP01 | Change in the name or title of a patent holder |
Address after: 431800 Industrial Zone, Jingshan Economic Development Zone, Jingmen, Hubei Patentee after: Hubei Jingyuan mountain biological Polytron Technologies Inc Address before: 431800 Industrial Zone, Jingshan Economic Development Zone, Jingmen, Hubei Patentee before: HUBEI JINGYUANSHAN BIOLOGICAL TECHNOLOGY CO., LTD. |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150218 Termination date: 20181023 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |