CN101584379B - Fermentation process of bean dregs - Google Patents
Fermentation process of bean dregs Download PDFInfo
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- CN101584379B CN101584379B CN2009100648634A CN200910064863A CN101584379B CN 101584379 B CN101584379 B CN 101584379B CN 2009100648634 A CN2009100648634 A CN 2009100648634A CN 200910064863 A CN200910064863 A CN 200910064863A CN 101584379 B CN101584379 B CN 101584379B
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Abstract
The invention provides a fermentation process of bean dregs, the bean dregs fermented after pretreatment, the material after the fermentation is subjected to dehydration working section to obtain finished products, the dehydration working section comprises the following steps that: the material after the fermentation is extruded so that moisture content of the material can reduce to 30-40%; the material is continually fed into a tube bundle hot-air drier for drying, the temperature of the tube bundle hot-air drier is controlled in a range from 50 to 70 DEG C so that moisture content of the material can reduce to 25-30%; the material is then fed into the hot-air drier for drying so that moisture content of the material can reduce to 13-15%, at last, the material is cooled by cold wind so that moisture content of the material can reduce below 12%. The invention uses the method of stepped dehydration to thereby shorten the time for dehydration and uses different dehydration methods at stages in which different moisture contents are present to thereby avoid the problem that when being directly dried by hot wind for dehydration at relatively high moisture content, the material becomes sticky and is liable to block, and to thereby enable dehydration of the material to be more even.
Description
Technical field
The invention belongs to fermentation technical field, relate to a kind of fermentation process of bean dregs.
Background technology
At present, mostly the raw material of piling is cheated in utilization in the fermenting and producing of dregs of beans, adopt manual stirring or movable type to take off and expect that mechanism carries out the turning operation on the ground and finishes fermentation, this method floor space is big, and manually-operated labour intensity height needs fermentation vat is cleared up before the next time fermentation carrying out, again add the fermentation that dregs of beans and bacterial classification carry out next round then, but need waste the regular hour when clearing up last fermentation vat, not form continuous fermentation, production efficiency is lower.Product after fermentation finishes is directly spread airing in the sun out, and also there are many shortcomings in airing like this, and the time that for example needs is long, and the Signs of Mould that causes the local moisture height of product to cause easily.The temperature and humidity of adding in the sweat is wayward, finally causes product quality low and unstable.
Summary of the invention
The purpose of this invention is to provide a kind of fermentation process of bean dregs that can make the tunning efficient drying and can realize continuously fermenting.
For achieving the above object, the present invention is by the following technical solutions: fermentation process of bean dregs, dregs of beans ferments after preliminary treatment, the material after the fermentation through dehydration after the workshop section finished product, described dehydration workshop section may further comprise the steps: the material after the fermentation makes the material contained humidity reduce to 30～40% through extruding; Continuation is sent material into tube bank air drier drying, and the temperature of control bundle air drier is 50～70 ℃, makes the material contained humidity reduce to 25～30%; Send into the air flow dryer dried material then, make the material contained humidity reduce to 13～15%, after the cold wind cooling is reduced to below 12% moisture.
The dried material of described tube bank air drier is sent into air flow dryer again after dispersing device is broken up, the temperature in the control air flow dryer is 50～70 ℃.
Described sweat adopts the fermentation tower that is provided with the multilayer fermentation chamber, this fermentation tower comprises the fermentation tower housing, housing top is provided with charging aperture, be provided with the multilayer fermentation chamber in the housing, every layer of fermenting cellar rotates the turnover panel that is provided with by at least one group and forms on housing, be connected with turning device with turnover panel, the housing internal upper part is provided with flat materials device.
Described housing inner bottom part is provided with drawing mechanism.
Described drawing mechanism comprises discharging driving shaft, the discharging driven shaft that discharging drive motors and housing bottom be arranged in parallel, discharging driving shaft and discharging drive motors are in transmission connection, be respectively equipped with the discharging sprocket wheel at discharging driving shaft and discharging driven shaft two ends, the discharging sprocket wheel is provided with the output chain, is interval with the discharging scraper plate on the output chain.
Described flat materials device comprises flat material driving shaft, the flat material driven shaft that flat material drive motors and housing upper parallel are provided with, flat material driving shaft is in transmission connection with flat material drive motors, be respectively equipped with flat material sprocket wheel at flat material driving shaft peace material driven shaft two ends, flat material sprocket wheel is provided with flat material chain, be interval with flat material scraper plate on flat material chain, flat material scraper plate is provided with stand material cake tooth.
Described turning device comprises the hydraulic cylinder that is fixed on the housing crossbeam and the trip shaft at turnover panel two ends, be fixed with bearing on the crossbeam, trip shaft is located at the inner ring of bearing, and the hydraulic stem of hydraulic cylinder is hinged with the rocking arm that is installed on the trip shaft, and the angle on rocking arm and turnover panel plane is 45 °.
The outer corresponding every layer of fermenting cellar of described housing is provided with air inlet and exhaust outlet.
Corresponding every layer of fermenting cellar is provided with spray equipment in the described housing.
Described output chain below is provided with suitable with it wear-resisting slideway.
Dehydration of the present invention workshop section carries out step by step, earlier the material after the fermentation is pushed, because the moisture in the material is about 50% at this moment, moisture is easily separated, adopt free water in the method extruded material that pushes, moisture is dropped to about 35%, the problem that material is clamminess, easily lumps when adopting the heated-air drying dehydration for preventing that moisture is high; And then send into and restrain the air drier drying, moisture is reduced to below 30%, the tube bank heated-air drying strengthened material stir with hot blast fully contact the caking that has prevented material effectively, removed the moisture of material epidermis, make material viscosity reduce prevented from caking; Continue to adopt air flow dryer that material is carried out drying, hot blast makes material suspended, and the moisture diffusion with material inside arrives the outside simultaneously, and the moisture in the material is dropped to about 13% from 30%,, reach the requirement of product after the cold wind cooling makes in the material moisture reduce to below 12%.The dried material of tube bank air drier is sent into hot-air seasoning earlier again after dispersing device is broken up, material is broken up, and the dehydration of material is more even when making hot-air seasoning.The present invention adopts the installation for fermenting that is provided with the multilayer fermentation chamber, and every layer of fermenting cellar rotates the turnover panel that is provided with by at least one group on housing forms, and is connected with turning device with turnover panel, and the housing internal upper part is provided with flat materials device.To send on the ground floor turnover panel of installation for fermenting through pretreated material during concrete operations, after the certain hour fermentation, upset ground floor turnover panel makes material fall into second layer turnover panel, continues in the top fermentation of second layer turnover panel; And the while is sent into second batch fermentation materials again on the ground floor turnover panel, continue through after the fermentation of certain hour, upset second layer turnover panel makes material fall into the 3rd layer of turnover panel continuation fermentation, after second layer turnover panel resets, upset ground floor turnover panel makes second batch material fall into second layer turnover panel; After resetting, the ground floor turnover panel sends into the 3rd batch fermentation materials, so be concatenated to form continuous sweat, guarantee that the fermentation materials on every layer of turnover panel all is fermentation materials of different batches, the material on every layer of turnover panel ferments simultaneously, has guaranteed the continuity of producing.The outer corresponding every layer of fermenting cellar of housing is provided with air inlet and exhaust outlet, is used for ventilating in housing and outwards exhaust, and corresponding every layer of fermenting cellar is provided with spray equipment in the housing, is used for spray water or active bacterium liquid on material.Finish fermentation after drawing mechanism output is sent into dehydration workshop section and carried out drying when first batch material, product moisture is reduced to below 12%, meet the requirements, be packaged as finished product.The present invention adopts the substep dehydration method, shortened the time of dehydration, adopt different dewaterings in the different in moisture content stage, the problem that material is clamminess, easily lumps when avoiding directly carrying out the heated-air drying dehydration when contained humidity is higher makes the dehydration of material more even; The present invention adopts the fermentation tower that is provided with the multilayer fermentation chamber, has realized continuously fermenting, and can carry out the fermentation of different batches fermentation materials simultaneously, and production efficiency is improved greatly, has high economic benefit.
Description of drawings
Fig. 1 is the structural representation of the used fermentation tower of the present invention;
Fig. 2 is the A-A view among Fig. 1;
Fig. 3 is the B-B view among Fig. 1;
Fig. 4 is the structural representation of drawing mechanism among Fig. 1;
Fig. 5 is the D-D view among Fig. 4;
Fig. 6 is the structural representation of flat materials device among Fig. 1;
Fig. 7 is the C-C view among Fig. 6;
Fig. 8 is the structural representation of panel turnover device among Fig. 1;
Fig. 9 is that the E of Fig. 8 is to schematic diagram.
The specific embodiment
Embodiment 1: fermentation process of bean dregs, and dregs of beans ferments after mixing through water logging, interpolation bacterial classification, and the material of fermentation back moisture 50～70% pushes through extruder earlier and makes the material contained humidity reduce to 30%; Continuation is sent material into tube bank air drier drying, and the temperature of control bundle air drier is 50 ℃, makes the material contained humidity reduce to 25%, and material is broken up through dispersing device again; Send into the air flow dryer dried material then, the temperature in the control air flow dryer is 50 ℃, makes the material contained humidity reduce to 13%, after the cold wind cooling is reduced to below 12% moisture.
Used device is the fermentation tower that is provided with the multilayer fermentation chamber during fermentation, as Fig. 1, Fig. 2 and shown in Figure 3, this fermentation tower comprises fermentation tower housing 1, and housing 1 top is provided with charging aperture 2, the bottom is provided with discharging opening 10, be provided with 6 layers of fermenting cellar in the housing, i.e. 6 layers of turnover panel, every layer of fermenting cellar rotates the turnover panels 5 that are provided with by 6 and forms on housing 1, seamless cooperation between the turnover panel 5, be connected with turning device 6 on the turnover panel 5, housing 1 internal upper part is provided with flat materials device 3, and housing 1 inner bottom part is provided with drawing mechanism 9.Housing 1 outer corresponding every layer of fermenting cellar is provided with air inlet 8 and exhaust outlet 7, is used for ventilating in housing 1 and outwards exhaust, and corresponding every layer of fermenting cellar is provided with spray equipment 4 in the housing 1, is used for spray water or active bacterium liquid on material.
Drawing mechanism 9 as shown in Figure 4 and Figure 5, comprise the discharging driving shaft 92 that discharging drive motors 91 and housing 1 bottom be arranged in parallel, discharging driven shaft 97, discharging driving shaft 92 is connected with discharging drive motors transmission 91, be respectively equipped with discharging sprocket wheel 93 at discharging driving shaft 92 and discharging driven shaft 97 two ends, discharging sprocket wheel 93 is provided with output chain 94, on output chain 94, be interval with discharging scraper plate 95, discharging scraper plate 95 rotates with output chain 94, discharging scraper plate 95 pushes material to discharging opening 10 when rotating, output chain 94 belows are provided with suitable with it wear-resisting slideway 96, and output chain 94 and discharging scraper plate 95 are play the guiding role.
Flat materials device 3 as shown in Figure 6 and Figure 7, comprise the flat material driving shaft 32 that flat material drive motors 31 and housing 1 upper parallel are provided with, flat material driven shaft 37, flat material driving shaft 32 is in transmission connection with flat material drive motors 31, be respectively equipped with flat material sprocket wheel 33 at flat material driving shaft 32 peace material driven shafts 37 two ends, flat material sprocket wheel 33 is provided with flat material chain 34, on flat material chain 34, be interval with flat material scraper plate 35, flat material scraper plate 35 is when rotating with flat material chain 34, material on the turnover panel 5 is spread out, flat material scraper plate 35 is provided with stand material cake tooth 38, and material is evenly spread out on turnover panel 5.Flat material chain 34 belows are provided with suitable with it wear-resisting slideway 36, and flat material chain 34 and stand material cake tooth 38 are play the guiding role.
As Fig. 8 and turning device 6 shown in Figure 9, comprise and be fixed on housing 1 outer transverse beams 54 the hydraulic cylinder 81 and the trip shaft 52 at turnover panel 5 two ends, be fixed with bearing 55 on the crossbeam 54, trip shaft 52 is located at the inner ring of bearing 55, trip shaft 52 is provided with Rocker arm 56, turnover panel 5 comprises dull and stereotyped 51 and reinforcement 53, and the angle on Rocker arm 56 and turnover panel 5 planes is 45 ° and overturns in the 90 degree scopes between horizontal plane and vertical guide for ease of turnover panel 5; The hydraulic stem 82 of hydraulic cylinder 81 is hinged with Rocker arm 56, and the reciprocating motion by hydraulic stem 82 drives Rocker arm 56 and swings back and forth, and pendulum angle is 90 degree.
Concrete sweat is, dregs of beans is sent in the fermentation housing 1 from charging aperture 2 after water logging, interpolation bacterial classification mix, by flat materials device 5 material is evenly distributed on the ground floor turnover panel, after the certain hour fermentation, open the hydraulic cylinder 81 of ground floor turnover panel, upset ground floor turnover panel falls on the second layer turnover panel ground floor material, continues in the top fermentation of second layer turnover panel; And the ground floor turnover panel that resets simultaneously, on the ground floor turnover panel, send into second batch fermentation materials again through charging aperture, continue through after the fermentation of certain hour, open the hydraulic cylinder 81 of second layer turnover panel, upset second layer turnover panel makes second layer material fall into the 3rd layer of turnover panel continuation fermentation, after second layer turnover panel resetted, upset ground floor turnover panel made second batch material fall into second layer turnover panel; The ground floor turnover panel resets after charging aperture is sent into the 3rd batch fermentation materials, so be concatenated to form continuous sweat, guarantee that the fermentation materials on every layer of turnover panel all is fermentation materials of different batches, every layer of turnover panel top fermentation material ferments simultaneously, guaranteed the continuity of producing.Fall into orlop after first batch material is finished fermentation, open discharging drive motors 91 and drive output chain 94, output chain 94 drive discharging scraper plates 95 through discharging opening 10 output housings 1 outside, are sent into material dehydration workshop section and are carried out drying.
Embodiment 2: fermentation process of bean dregs, and dregs of beans ferments after mixing through water logging, interpolation bacterial classification, and the material after the fermentation makes the material contained humidity reduce to 35% through the extruder extruding earlier; Continuation is sent material into tube bank air drier drying, and the temperature of control bundle air drier is 60 ℃, makes the material contained humidity reduce to 27%; Send into the air flow dryer dried material then, the temperature in the control air flow dryer is 60 ℃, makes the material contained humidity reduce to 14%, after the cold wind cooling is reduced to below 12% moisture.
Installation for fermenting is identical with embodiment 1 with sweat.
Embodiment 3: fermentation process of bean dregs, and dregs of beans ferments after mixing through water logging, interpolation bacterial classification, and the material after the fermentation makes the material contained humidity reduce to 40% through the extruder extruding earlier; Continuation is sent material into tube bank air drier drying, and the temperature of control bundle air drier is 70 ℃, makes the material contained humidity reduce to 30%, and material is broken up through dispersing device again; Send into the air flow dryer dried material then, the temperature in the control air flow dryer is 70 ℃, makes the material contained humidity reduce to 15%, after the cold wind cooling is reduced to below 12% moisture.
Installation for fermenting is identical with embodiment 1 with sweat.
Claims (10)
1. fermentation process of bean dregs, dregs of beans ferments after preliminary treatment, the material after the fermentation after dehydration workshop section finished product, it is characterized in that described dehydration workshop section may further comprise the steps: the material after the fermentation makes the material contained humidity reduce to 30～40% through extruding; Continuation is sent material into tube bank air drier drying, and the temperature of control bundle air drier is 50～70 ℃, makes the material contained humidity reduce to 25～30%; Send into the air flow dryer dried material then, make the material contained humidity reduce to 13～15%, after the cold wind cooling is reduced to below 12% moisture.
2. fermentation process of bean dregs as claimed in claim 1 is characterized in that: the dried material of described tube bank air drier is sent into air flow dryer again after dispersing device is broken up, and the temperature in the control air flow dryer is 50～70 ℃.
3. fermentation process of bean dregs as claimed in claim 1 or 2, it is characterized in that: sweat adopts the fermentation tower that is provided with the multilayer fermentation chamber, this fermentation tower comprises the fermentation tower housing, housing top is provided with charging aperture, be provided with the multilayer fermentation chamber in the housing, every layer of fermenting cellar rotates the turnover panel that is provided with by at least one group on housing forms, and is connected with turning device with turnover panel, and the housing internal upper part is provided with flat materials device.
4. fermentation process of bean dregs as claimed in claim 3 is characterized in that: described housing inner bottom part is provided with drawing mechanism.
5. fermentation process of bean dregs as claimed in claim 4, it is characterized in that: described drawing mechanism comprises discharging driving shaft, the discharging driven shaft that discharging drive motors and housing bottom be arranged in parallel, discharging driving shaft and discharging drive motors are in transmission connection, be respectively equipped with the discharging sprocket wheel at discharging driving shaft and discharging driven shaft two ends, the discharging sprocket wheel is provided with the output chain, is interval with the discharging scraper plate on the output chain.
6. fermentation process of bean dregs as claimed in claim 5, it is characterized in that: described flat materials device comprises flat material driving shaft, the flat material driven shaft that flat material drive motors and housing upper parallel are provided with, flat material driving shaft is in transmission connection with flat material drive motors, be respectively equipped with flat material sprocket wheel at flat material driving shaft peace material driven shaft two ends, flat material sprocket wheel is provided with flat material chain, be interval with flat material scraper plate on flat material chain, flat material scraper plate is provided with stand material cake tooth.
7. fermentation process of bean dregs as claimed in claim 6, it is characterized in that: described turning device comprises the hydraulic cylinder that is fixed on the housing crossbeam and the trip shaft at turnover panel two ends, be fixed with bearing on the crossbeam, trip shaft is located at the inner ring of bearing, the hydraulic stem of hydraulic cylinder is hinged with the rocking arm that is installed on the trip shaft, and the angle on rocking arm and turnover panel plane is 45 °.
8. fermentation process of bean dregs as claimed in claim 7 is characterized in that: the outer corresponding every layer of fermenting cellar of housing is provided with air inlet and exhaust outlet.
9. fermentation process of bean dregs as claimed in claim 8 is characterized in that: corresponding every layer of fermenting cellar is provided with spray equipment in the housing.
10. fermentation process of bean dregs as claimed in claim 9 is characterized in that: described output chain below is provided with suitable with it wear-resisting slideway.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009100648634A CN101584379B (en) | 2009-05-12 | 2009-05-12 | Fermentation process of bean dregs |
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| Application Number | Priority Date | Filing Date | Title |
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| CN2009100648634A CN101584379B (en) | 2009-05-12 | 2009-05-12 | Fermentation process of bean dregs |
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| CN101584379A CN101584379A (en) | 2009-11-25 |
| CN101584379B true CN101584379B (en) | 2011-09-14 |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102823717B (en) * | 2012-09-14 | 2014-02-19 | 浙江诚元生物技术有限公司 | Preparation method of high-bioactivity fermented soybean meal |
| CN104946459B (en) * | 2015-06-30 | 2017-07-25 | 河南双成生物科技有限公司 | Liquid, solid-state biological raw material fermentation system |
| CN106180143B (en) * | 2016-07-25 | 2018-10-23 | 河南农业大学 | A kind of multistage turnover plate type biological decomposition cultivation apparatus |
| CN108129172A (en) * | 2018-01-20 | 2018-06-08 | 徐州市禾协肥业有限公司 | Opening solid belt Zymolysis Equipment |
| CN108433138A (en) * | 2018-03-26 | 2018-08-24 | 扬州福尔喜果蔬汁机械有限公司 | A kind of fruit and vegetable drying machine |
| CN110074261A (en) * | 2019-06-06 | 2019-08-02 | 湖南良平农牧发展有限公司 | A kind of processing technology of wet fresh fermented bean dregs |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1714668A (en) * | 2004-07-02 | 2006-01-04 | 荣华联合生物科技（深圳）有限公司 | Method for preparing biological active protein using bean dregs as main material |
| CN2789692Y (en) * | 2005-03-30 | 2006-06-21 | 宜兴市格兰特干燥浓缩设备有限公司 | Improved pipe bundle drying machine |
| CN1974782A (en) * | 2006-11-07 | 2007-06-06 | 江南大学 | Solid state fermentation process for producing product with rich probiotics polypeptide |
| CN2935046Y (en) * | 2006-08-01 | 2007-08-15 | 母立伟 | Pipe-cluster dryer |
| CN101019609A (en) * | 2007-03-22 | 2007-08-22 | 浙江大学 | Solid fermentation process for producing natto bacillus feed additive with bean dregs |
| CN101263865A (en) * | 2008-04-21 | 2008-09-17 | 浙江大学宁波理工学院 | Method for preparing biochemical soya bean watse by solid-state fermentation |
-
2009
- 2009-05-12 CN CN2009100648634A patent/CN101584379B/en not_active Expired - Fee Related
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1714668A (en) * | 2004-07-02 | 2006-01-04 | 荣华联合生物科技（深圳）有限公司 | Method for preparing biological active protein using bean dregs as main material |
| CN2789692Y (en) * | 2005-03-30 | 2006-06-21 | 宜兴市格兰特干燥浓缩设备有限公司 | Improved pipe bundle drying machine |
| CN2935046Y (en) * | 2006-08-01 | 2007-08-15 | 母立伟 | Pipe-cluster dryer |
| CN1974782A (en) * | 2006-11-07 | 2007-06-06 | 江南大学 | Solid state fermentation process for producing product with rich probiotics polypeptide |
| CN101019609A (en) * | 2007-03-22 | 2007-08-22 | 浙江大学 | Solid fermentation process for producing natto bacillus feed additive with bean dregs |
| CN101263865A (en) * | 2008-04-21 | 2008-09-17 | 浙江大学宁波理工学院 | Method for preparing biochemical soya bean watse by solid-state fermentation |
Non-Patent Citations (1)
| Title |
|---|
| 吴皓等.厚朴饮片干燥工艺的考察.《中药材》.2006,第29卷(第11期), * |
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