CN1114686A - A mobile solid fermentation method - Google Patents
A mobile solid fermentation method Download PDFInfo
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- CN1114686A CN1114686A CN94107801.9A CN94107801A CN1114686A CN 1114686 A CN1114686 A CN 1114686A CN 94107801 A CN94107801 A CN 94107801A CN 1114686 A CN1114686 A CN 1114686A
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Abstract
本发明公开了一种移动式固体发酵方法，包括菌种培养、培养基灭菌、接种、发酵、烘干、磨细，其特征在于培养基灭菌采用高压灭菌，蒸汽压为0.1～0.3MPa，时间为5～20分钟，培养基在封闭的发酵室内，沿环形路线行走，同时发酵，然后烘干，使含水量≤3％，磨细成粒度200～325目的粉剂，其毒力效价为8000～1600IU/mg。本发明工艺简单，使微生物的固体发酵按其规定工艺条件进行，实现无杂菌污染、优质高产、连续自动化生产。
The invention discloses a mobile solid fermentation method, which comprises strain cultivation, culture medium sterilization, inoculation, fermentation, drying and grinding, and is characterized in that the culture medium is sterilized by high pressure sterilization, and the steam pressure is 0.1-0.3 MPa, the time is 5-20 minutes, the culture medium walks along a circular route in a closed fermentation room, ferments at the same time, and then dries to make the water content ≤ 3%, and grinds it into a powder with a particle size of 200-325 mesh. The price is 8000～1600IU/mg. The process of the invention is simple, and the solid fermentation of microorganisms is carried out according to the specified process conditions, so that no bacteria pollution, high-quality, high-yield, and continuous automatic production are realized.
Description
The present invention relates to solid-fermented technique, specifically a kind of movable solid fermentation method.
Make a general survey of fermentation technology process, be divided into two big classes basically.One class is a liquid fermentation process, and a class is a solid fermentation method.Solid fermentation method normally is placed on solid medium on Da Chi, pallet, platform or the ground and ferments, and its substratum is transfixion or slightly stirs on the spot, can be called fixed fermentation process.This method exists, and temperature in the substratum, humidity are inhomogeneous during the fermentation, and it is inhomogeneous to ventilate, be difficult to regulate its temperature, humidity and oxygen requirement with fermentation diagram, exist dress discharge zone and proving room together, easily cause the shortcoming of living contaminants etc., so quality product is difficult to stablize.In addition, it is big also to exist labour intensity, and throughput is low, is difficult to the shortcoming of large-scale industrial production.
The object of the present invention is to provide a kind of movable solid fermentation method and device, to overcome above-mentioned shortcoming.
The present invention includes spawn culture, medium sterilization, inoculation, fermentation, oven dry, levigate, it is characterized in that:
1) said medium sterilization adopts autoclaving, vapor pressure 0.1～0.3MPa, 5～20 minutes time.
2) in the said fermentation procedure:
A. postvaccinal substratum is placed on the porous barrier 2 of the special-purpose rack that can ventilate in the bottom, there is seam in last bottom,
B. the rack lamination is placed on the running gear, in the proving room of sealing, and along ring-like route walking, fermentation simultaneously,
3) solid medium after fermentation is finished is made granularity 200～325 orders, the pulvis of water content≤3% by air stream drying and superfine grinding.
The present invention has overcome that existing solid fermentation method yields poorly, temperature, non-uniform temperature, ventilation are inhomogeneous, be difficult to characteristics such as automatic continuous production, the solid fermentation of microorganism is become to carrying out continuous production by its regulation processing condition from batch production, realize no living contaminants, high-quality, high yield, continuous automatic production.
The present invention has following accompanying drawing:
Fig. 1 process frame chart of the present invention
Fig. 2 autoclave structural representation
The special-purpose rack synoptic diagram of Fig. 3
Fig. 4 plane formula annular proving room synoptic diagram
The vertical annular proving room synoptic diagram of Fig. 5
Fig. 6 suspension type running gear synoptic diagram
Fig. 7 floor rail type moves the device synoptic diagram
Below in conjunction with accompanying drawing the present invention is described in detail.
Fig. 1 is a technical process schematic block diagram of the present invention, comprises spawn culture, medium sterilization, inoculation, fermentation, oven dry, levigate, and concrete grammar is as follows:
1. spawn culture.Can carry out spawn culture by the method that prior art provides.
2. medium sterilization.The present invention has adopted autoclaved method, sterilizes under vapor pressure 0.1MPa～0.3MPa 5～20 minutes, under agitation finishes sterilization, to guarantee that sterilization evenly, thoroughly.
Cook mode for the solid medium sterilization normal pressures that adopt in the former solid fermentation more, it cooks general employing of time and kept atmosphere 1.5～3 hours, having the people that this is improved to atmosphere afterwards steamed 15～60 minutes, though before reach same sterilising effect, reduced the saving of time that steams energy consumption (seeing patent 88101450.8), but still the time of steaming is longer, once Mie Jun quantity can not be too many, how many only is～tens jin, to amass wealth by heavy taxation support in the base nutrition destroy more, by known medium sterilization theory temperature as can be known, it is shown in the following table that time and nutrient destructive close:
| Sterilising temp (℃) | Sterilization time (minute) | Nutrition destruction amount (%) |
| ????100 | ????400 | ????99.3 |
| ????110 | ????36 | ????67 |
| ????115 | ????15 | ????50 |
| ????120 | ????4 | ????27 |
| ????130 | ????0.5 | ????8 |
As seen sterilization time is long more, and temperature is low more, and is unfavorable more.In order to adapt to requirements of large-scale production, the present invention gives a kind of special-purpose Sterilizers (can referring to Fig. 2), comprise motor 1, coupling shaft 2, housing 3, colter 4, support 5, charging opening 6 and discharge port 7, these all can be identical with known colter formula agitator, for to housing 3 preheatings, and in the insulation of reinforced back, to guarantee to have sterilising effect preferably, be provided with steam jacket 8 in the outside of housing 3, chuck 8 is provided with steam-in 9 and condensation-water drain 10.Chuck 8 can adopt steel plate to make, and can be welded on housing 3 outsides after reel, the moulding, should reserve the position of charging opening 6, discharge port 7, steam-in 11 and vapour outlet 12.In order to feed steam sterilizing, housing 3 is provided with steam-in 11 and vapour outlet 12, and even for air-flow, the vapour outlet 12 on the housing 3 can respectively be established one in top, the bottom of housing 3.The vapor pressure that feeds can be decided to be 0.1～0.3MPa, sterilization time 5～20 minutes, and sterilization is carried out under colter stirs, to guarantee the homogeneity and the thoroughness of sterilization.Because this Sterilizers is once feeded and can be reached 400 kilograms, and be provided with the colter whipping appts, under solid medium is constantly stirred, use high pressure steam sterilization, under vapor pressure 0.1～0.3MPa, sterilization time was at 5～20 minutes, not only can reach good sterilising effect, and short energy consumption of time is low, and little to substratum nutrition destruction, the primary treatment amount is big to be unprecedented.
3. inoculation.Inoculation can be undertaken by existing method.
4. fermentation.The solid fermentation method of prior art, substratum all are motionless, and it finishes fermenting process through after a while in the proving room of a sealing.The present invention has provided a kind of movable solid fermentation method, on the porous barrier of the special-purpose rack that can ventilate bottom postvaccinal substratum is placed on, there is seam in last bottom (referring to Fig. 3).
Rack comprises and has the up and down frame 1 of seam, and seam can design by prior art up and down, location when being used for lamination and placing, and can guarantee to stack stable, do not tilt.Porous barrier 2 on the frame 1 can have two kind schemes with the relative position of the pore of offering 3 all around, and a kind of scheme is the middle part that porous barrier 2 is located at frame 1, and top is for stacking the space of substratum, and pore 3 is opened in the bottom around the frame 1, is used for ventilation; Another kind of scheme is the bottom that porous barrier 2 is located at frame 1, and pore 3 is opened in the middle and upper part around the frame 1, is the space of stacking substratum between dividing plate 2 and the plane, pore 3 place.When the rack lamination was placed, there was good ventilation the locus that above-mentioned two kinds of schemes all can form substratum and pore apart from one another by arrangement during with the assurance fermentation.Rack overlays on the running gear, in the proving room of sealing, along the circuit walking, ferments simultaneously.Proving room has plane formula annular proving room and two kinds of designs of vertical annular proving room.Plane formula annular proving room is similar to the design of irradiation station, and vertical annular proving room is similar to the design of bucket elevator.
Fig. 4 is a plane formula annular proving room synoptic diagram, comprises loading area 11, discharge zone 7 and fermentation zone 33, and fermentation zone 33 was opened with the dress discharge zone in 11,7 minutes, isolates with mechanical type or wind curtain type therebetween, and 2 for isolating air curtain among Fig. 4, and 10 is transfer door.Be provided with air channel 6, rack 4, drive unit 8, tightening device 9 and track 12 in the fermentation zone 33.Running gear can have two kinds of suspension type (referring to Fig. 6) and floor rail types (referring to Fig. 7), and suspension bracket 14 hangs in orbit through suspender 13, and rack 4 overlays on the suspension bracket 14; Carriage 16 is placed on the track 12, and rack 4 overlays on the carriage 16.
Fig. 5 is vertical annular proving room, and loading area 11, discharge zone 7 isolated by air curtain 2 with fermentation zone 33, suspender 13, suspension bracket 14, rack 4 is suspended on the track 12, carries out circulatory motion under the effect of drive unit 8.
Proving room can be divided into 3～5 sections according to processing condition and by the feature of growing of organism of fermentation.According to the zymotechnique requirement, airborne temperature, humidity, the oxygen level of each section is controlled to be different amounts.For example, fermentation to Bacillus thuringiensis can be divided into three districts, district 3 and fermentation end district 1 in i.e. fermentation initial stage district 5, the fermentation, each district is by an independent air conditioner system air blast, isolate with air curtain between each district or isolate with the soft curtain of plastics, the temperature in three districts is controlled to be 26～34 ℃, 22～30 ℃ and 24～32 ℃ respectively, and humidity is controlled to be 75～95%, 80～100%, 70～95%.Airborne oxygen level generally is to regulate by advancing in the air draft fresh air proportion, generally 18～21%, can feed pure oxygen during for special requirement and make oxygen level in the air＞21% become oxygen-rich air.
It can be slowly to move that solid medium is walked in fermentation, for example with 0.03～0.1 meter/minute row of not stopping transport continuously, also can be to loiter, for example walked 1～2 hour, stop 1～2 hour then, went further 1～2 hour with 0.6～0.8. rice/minute speed, stopped again 1～2 hour, so repeatedly, end up to fermentation, will be as for choosing the sort of form according to specifically being determined by the fermentation period of culturing micro-organisms and designed productive capacity.
5. dry.Solid medium after fermentation is finished makes its water content≤3% by air stream drying or other drying mode, and its preservation period can be lengthened to 2 years like this.
6. levigate.Adopt superfine grinding, making granularity is 200～325 purpose pulvis or wettable powders.These granularity 100 orders than traditional zymotic have improved a lot, thereby its suspensibility can bring up to 70% from traditional 30%, has improved the use properties of product greatly.
When the present invention was used for the production of Bacillus thuringiensis, the toxicity evaluation of products obtained therefrom was 8000～16000IU/mg, and the toxicity evaluation of existing method only is 100～1000IU/mg.
Claims (7)
1. a movable solid fermentation method comprises spawn culture, medium sterilization, inoculation, fermentation, oven dry, levigate, it is characterized in that:
1) said medium sterilization adopts autoclaving, vapor pressure 0.1～0.3MPa, and the time is 5～20 minutes,
2) in the said fermentation procedure:
A. postvaccinal substratum is placed on the porous barrier of the special-purpose rack that can ventilate in the bottom, there is seam in last bottom,
B. the rack lamination is placed on the running gear, in the proving room of sealing, and along the circuit walking, fermentation simultaneously,
3) solid medium after fermentation is finished is made the pulvis of granularity 200～325 orders, water content≤3% by dry and pulverizing.
2. solid fermentation method as claimed in claim 1, the indoor air temperature that it is characterized in that fermenting, humidity, oxygen level move towards subregion control along it, are divided into three districts by the processing requirement of fermented bacterium is minimum.
3. solid fermentation method as claimed in claim 2, it is characterized in that said three sections are fermentation initial stage district 5, ferment middle district 3 and the phase district 1 of fermenting not, corresponding temperature is respectively: 26～34 ℃, 22～30 ℃ and 24～32 ℃, corresponding humidity is: 75～95%, 80～100% and 70～95%.
4. as the solid fermentation method of claim 1 or 2 or 3, it is characterized in that said sealing proving room, circuit are plane formula annular proving room.
5. as the solid fermentation method of claim 1 or 2 or 3, it is characterized in that said sealing proving room, circuit are vertical annular proving room.
6. solid fermentation method as claimed in claim 4 is characterized in that said plane annular proving room adopts the suspension type operation.
7. solid fermentation method as claimed in claim 4 is characterized in that said plane annular proving room adopts the floor rail type operation.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN94107801A CN1044721C (en) | 1994-07-08 | 1994-07-08 | Movable solid fermentation method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN94107801A CN1044721C (en) | 1994-07-08 | 1994-07-08 | Movable solid fermentation method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1114686A true CN1114686A (en) | 1996-01-10 |
| CN1044721C CN1044721C (en) | 1999-08-18 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN94107801A Expired - Fee Related CN1044721C (en) | 1994-07-08 | 1994-07-08 | Movable solid fermentation method |
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| Country | Link |
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| CN (1) | CN1044721C (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2001012774A1 (en) * | 1999-08-16 | 2001-02-22 | David Grant Piggott | Method and apparatus for culturing microorganisms |
| US7183074B2 (en) | 2002-01-22 | 2007-02-27 | Institute Of Process Engineering, Chinese Academy Of Sciences | Gas dual-dynamic solid state fermentation technique and apparatus |
| CN101974414A (en) * | 2010-10-18 | 2011-02-16 | 东北农业大学 | Solid ventilation pure culture device and method for microorganisms |
| CN102443535A (en) * | 2011-05-10 | 2012-05-09 | 中国科学院过程工程研究所 | Solid fermentation bioreactor |
| CN105462813A (en) * | 2016-01-05 | 2016-04-06 | 贵州省轻工业科学研究所 | Combined mechanical ventilation fermenting and drying dual-purpose tank |
| CN107410670A (en) * | 2017-05-09 | 2017-12-01 | 中科天华生物科技有限公司 | Protein feed containing fermented papermulberry tree and preparation method thereof |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1056983A (en) * | 1990-06-02 | 1991-12-18 | 周振文 | A kind of production method and equipment of thuringiensis insecticide |
| CN1047201C (en) * | 1991-08-14 | 1999-12-08 | 北京农业大学 | Production-increasing bacteria solid fermentation process and its special fermentation equipment |
| CN1077988A (en) * | 1992-04-23 | 1993-11-03 | 刘永平 | Commercial solid fermentation production process of bacillus thuringiensis |
| CN1074240A (en) * | 1992-09-08 | 1993-07-14 | 新乡市酿造厂 | Tunnel-type continuously ventilating yeast-making process |
-
1994
- 1994-07-08 CN CN94107801A patent/CN1044721C/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2001012774A1 (en) * | 1999-08-16 | 2001-02-22 | David Grant Piggott | Method and apparatus for culturing microorganisms |
| US7183074B2 (en) | 2002-01-22 | 2007-02-27 | Institute Of Process Engineering, Chinese Academy Of Sciences | Gas dual-dynamic solid state fermentation technique and apparatus |
| CN101974414A (en) * | 2010-10-18 | 2011-02-16 | 东北农业大学 | Solid ventilation pure culture device and method for microorganisms |
| CN102443535A (en) * | 2011-05-10 | 2012-05-09 | 中国科学院过程工程研究所 | Solid fermentation bioreactor |
| CN102443535B (en) * | 2011-05-10 | 2013-05-01 | 中国科学院过程工程研究所 | Solid fermentation bioreactor |
| CN105462813A (en) * | 2016-01-05 | 2016-04-06 | 贵州省轻工业科学研究所 | Combined mechanical ventilation fermenting and drying dual-purpose tank |
| CN107410670A (en) * | 2017-05-09 | 2017-12-01 | 中科天华生物科技有限公司 | Protein feed containing fermented papermulberry tree and preparation method thereof |
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| Publication number | Publication date |
|---|---|
| CN1044721C (en) | 1999-08-18 |
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