CN201010643Y - Solid materials fermenting device - Google Patents
Solid materials fermenting device Download PDFInfo
- Publication number
- CN201010643Y CN201010643Y CN 200720100648 CN200720100648U CN201010643Y CN 201010643 Y CN201010643 Y CN 201010643Y CN 200720100648 CN200720100648 CN 200720100648 CN 200720100648 U CN200720100648 U CN 200720100648U CN 201010643 Y CN201010643 Y CN 201010643Y
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- fermentation
- tank
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M21/00—Bioreactors or fermenters specially adapted for specific uses
- C12M21/16—Solid state fermenters, e.g. for koji production
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/06—Nozzles; Sprayers; Spargers; Diffusers
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/18—External loop; Means for reintroduction of fermented biomass or liquid percolate
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- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Wood Science & Technology (AREA)
- Engineering & Computer Science (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Organic Chemistry (AREA)
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- Genetics & Genomics (AREA)
- Biomedical Technology (AREA)
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- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Molecular Biology (AREA)
- Fertilizers (AREA)
Abstract
The utility model relates to fermentation technical field, specifically to a solid state fermentation device for food brewing, biological and chemical medicine manufacturing and solid waste treatment. The utility model is to solve problem that when solid materials are degraded in the existing fermentation tank, the distribution of bacterial solution and materials is uneven and the temperature is the sealed tank is not easy to control. The utility model comprises a fermentation tank, wherein at least a spraying pipe is provided in the fermentation tank, a spray header is connected with the end of the spraying pipe, and an ejector is arranged at the top of the fermentation tank. The utility model is equipped with a spraying device in the fermentation tank for periodically and quantitatively spraying pre-prepared bacteria solution and additive, so that the distribution of the bacteria and additive in the material is uniform and the fermentation time of the solid material is shortened, and the temperature rising of the material in the degradation tank can be controlled by spraying liquid, and the circulating tank and circulating pump can make the spayed substrate liquid in the fermentation tank recycled. The utility model has the advantages of simple structure and convenient installation; and can be widely used for solid material fermentation, such as food brewing, biological and chemical medicine manufacturing and solid waste treatment.
Description
Technical field
The utility model relates to fermentation technical field, be specially a kind ofly be used for that food is brewageed, solid substances fermentation unit that solid fermentation is carried out in biochemical pharmacy and solid waste processing etc.
Background technology
In existing solid substances fermenting process, generally be that solid substances is deposited in ground or fermentation vat, the fermenter, take the nature stack retting to add then and adopt modes such as artificial or mechanical turning to solve the too high and uneven problem of fermentation of temperature in airy way or the stack retting process, its shortcoming is: 1, the time of pile fermentation is longer, need charging constantly, discharging and overturning in the stack retting process, time-consuming; 2, temperature, humidity should not be controlled, and raw material stack retting attenuation degree is inhomogeneous, and acidizing degree differs, and cause raw material availability not thorough, increase unfavorable factor to subsequent disposal; 3, floor space is big, and it is big that stink and dust are removed difficulty, easily causes secondary pollution.At above-mentioned shortcoming, people have developed fermentor tank, solid substances is placed in the sealed shell of tank, add a certain amount of bacterium liquid and additive then, though efficiently solve problems such as floor space is big in the aforesaid method, dust removal difficulty is big, fermentation time is long, but because bacterium liquid and additive are by manually directly adding, can make bacterium liquid and solid substances skewness like this, and the intravital temperature of sealed can being wayward.
Summary of the invention
When the utility model decomposed in fermentor tank in order to solve existing solid substances, problem such as the interior temperature of bacterium liquid and material skewness and sealed shell of tank is wayward provided a kind of solid substances fermentation unit.
The utility model is to adopt following technical scheme to realize: the solid substances fermentation unit, comprise fermentor tank, and be provided with a shower in the fermentor tank at least, the shower end is connected with spray header.The number of the spray header of shower described in the utility model and end thereof, shape are required to decide by material properties and decomposition.During use, a certain amount of bacterium liquid and additive are flowed in the fermentor tank by shower, and be sprinkled upon on the material through spray header, uniform distribution in material, shortened the fermentation time of solid substances, and behind the biochemical reaction that carries out for some time, temperature will rise in the fermentor tank, remain in the suitable scope by temperature in the regular spray liquid also may command fermentor tank.Regular, the quantitative spray of bacterium liquid described in the utility model and additive can be accomplished in several ways, and is that those of ordinary skill in the art is easy to realize.
Ejector also is equipped with at fermentor tank described in the utility model top, be existing known products, normally form by nozzle, suction chamber, diffuser pipe three parts, it is a kind of multi-usage aeration mode that utilizes the jet flow negative pressure principle to grow up, the dissolved oxygen efficiency height, circulate more air in the liquid that microbial inoculum and additive are formed, guarantee the dissolved oxygen amount in the liquid, provide suitable oxygen source for aerobic material decomposes flora.
How bacterium liquid described in the utility model and additive flow into shower, be that those of ordinary skill in the art is easy to realize, the utility model only provides a solution, simultaneously in order to reuse liquid under the pouring after bacterium liquid, additive and material react, fermentor tank one side described in the utility model also is provided with circulation tank, circulation tank is connected with fermentor tank bottom, shower upper end respectively by circulating line, and recycle pump is housed on the circulating line.
Compared with prior art, the utility model adopts installs spray equipment in fermentor tank, the bacterium liquid and the additive that can regular quantitative spray prepare in advance, flora and additive are evenly distributed in material, the solid substances fermentation time shortens, and the liquid may command is decomposed jar intensification of interior material under passing through to drench, circulation tank and recycle pump can make that substrate liquid obtains recycling under the pouring of fermentor tank, this apparatus structure is simple, easy for installation, can be widely used in that food is brewageed, the fermentation of solid substances such as biochemical pharmacy and solid waste processing.
Description of drawings
Fig. 1 is a structural representation of the present utility model
Among the figure: 1-fermentor tank 2-shower 3-spray header 4-ejector 5-circulation tank 6,7-circulating line 8-recycle pump
Embodiment
The solid substances fermentation unit, comprise fermentor tank 1, at least be provided with a shower 2 in the fermentor tank 1, shower 2 ends are connected with spray header 3, ejector 4 also is equipped with at fermentor tank 1 top, fermentor tank 1 one sides also are provided with circulation tank 5, and circulation tank 5 is connected with fermentor tank 1 bottom, shower 2 upper ends respectively by circulating line 6,7, and recycle pump 8 is housed on the circulating line 7.During use, earlier a certain amount of bacterium liquid and additive are prepared and put into circulation tank, bacterium liquid then, additive is under the effect of recycle pump, pump in the shower by circulation tank, and be sprinkled upon on the material through spray header, uniform distribution in material, shortened the fermentation time of solid substances, and behind the biochemical reaction that carries out for some time, temperature will rise in the fermentor tank, in suitable scope, the ejector at fermentor tank top can guarantee to spray the dissolved oxygen amount in the liquid simultaneously by temperature in the regular spray liquid also may command fermentor tank, provides suitable oxygen source for aerobic material decomposes flora; Liquid can flow in the circulation tank again by circulating line under the pouring after bacterium liquid, additive and material react simultaneously, reaches the purpose of recycling.
Claims (3)
1. a solid substances fermentation unit comprises fermentor tank (1), it is characterized in that: be provided with a shower (2) in the fermentor tank (1) at least, shower (2) end is connected with spray header (3).
2. solid substances fermentation unit according to claim 1 is characterized in that fermentor tank (1) top also is equipped with ejector (4).
3. solid substances fermentation unit according to claim 1 and 2, it is characterized in that fermentor tank (1) one side also is provided with circulation tank (5), circulation tank (5) is connected with fermentor tank (1) bottom, shower (2) upper end respectively by circulating line (6,7), and recycle pump (8) is housed on the circulating line (7).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200720100648 CN201010643Y (en) | 2007-02-13 | 2007-02-13 | Solid materials fermenting device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200720100648 CN201010643Y (en) | 2007-02-13 | 2007-02-13 | Solid materials fermenting device |
Publications (1)
Publication Number | Publication Date |
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CN201010643Y true CN201010643Y (en) | 2008-01-23 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN 200720100648 Expired - Fee Related CN201010643Y (en) | 2007-02-13 | 2007-02-13 | Solid materials fermenting device |
Country Status (1)
Country | Link |
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CN (1) | CN201010643Y (en) |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2011072539A1 (en) * | 2009-12-17 | 2011-06-23 | 中国南方航空工业(集团)有限公司 | Circulation apparatus for complete mix anaerobic reaction and method for circulation of biogas reaction feedstock |
CN101671625B (en) * | 2009-09-28 | 2012-08-15 | 厦门北大泰普科技有限公司 | Method and device for preparing trichoderma conidium by liquid state submerged fermentation |
CN104478188A (en) * | 2015-01-22 | 2015-04-01 | 潘磊 | Biogas generation method of biogas generation system with strain distribution achieved under driving of biogas slurry flowing promoted by air pressure |
CN104478186A (en) * | 2015-01-22 | 2015-04-01 | 潘磊 | Biogas generation method of biogas generation system for improving biogas slurry turbulence flow through biogas pressure |
CN104512991A (en) * | 2015-01-22 | 2015-04-15 | 潘磊 | Ultra-efficient marsh gas generation system with bacterium distribution device promoting uniform distribution of bacteria |
CN104556614A (en) * | 2015-01-22 | 2015-04-29 | 潘磊 | Method for producing methane by using methane fermentation generator based on one-way flowing of biomass fluid to promote uniform distribution of strains |
CN107793181A (en) * | 2017-12-23 | 2018-03-13 | 河北省农民合作社行业协会 | A kind of chicken droppings deodorant is dehydrated bio-fertilizer process line |
CN108795746A (en) * | 2018-07-26 | 2018-11-13 | 河南丰源和普农牧有限公司 | The independent segmented solid-state continuous fermentation system of aerobic-anaerobic and fermentation process |
CN109502202A (en) * | 2017-09-15 | 2019-03-22 | 上海寰球工程有限公司 | A kind of storage tank for preventing sticky material rotten |
CN114395455A (en) * | 2022-01-19 | 2022-04-26 | 四川轻化工大学 | Bottom liquid circulating spraying device of solid-state fermentation system |
-
2007
- 2007-02-13 CN CN 200720100648 patent/CN201010643Y/en not_active Expired - Fee Related
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101671625B (en) * | 2009-09-28 | 2012-08-15 | 厦门北大泰普科技有限公司 | Method and device for preparing trichoderma conidium by liquid state submerged fermentation |
WO2011072539A1 (en) * | 2009-12-17 | 2011-06-23 | 中国南方航空工业(集团)有限公司 | Circulation apparatus for complete mix anaerobic reaction and method for circulation of biogas reaction feedstock |
CN104478188A (en) * | 2015-01-22 | 2015-04-01 | 潘磊 | Biogas generation method of biogas generation system with strain distribution achieved under driving of biogas slurry flowing promoted by air pressure |
CN104478186A (en) * | 2015-01-22 | 2015-04-01 | 潘磊 | Biogas generation method of biogas generation system for improving biogas slurry turbulence flow through biogas pressure |
CN104512991A (en) * | 2015-01-22 | 2015-04-15 | 潘磊 | Ultra-efficient marsh gas generation system with bacterium distribution device promoting uniform distribution of bacteria |
CN104556614A (en) * | 2015-01-22 | 2015-04-29 | 潘磊 | Method for producing methane by using methane fermentation generator based on one-way flowing of biomass fluid to promote uniform distribution of strains |
CN104556614B (en) * | 2015-01-22 | 2016-06-01 | 班乐平 | The biogas fermentation device that natural pond liquid uniflux promotes bacterial classification uniform produces biogas method |
CN109502202A (en) * | 2017-09-15 | 2019-03-22 | 上海寰球工程有限公司 | A kind of storage tank for preventing sticky material rotten |
CN107793181A (en) * | 2017-12-23 | 2018-03-13 | 河北省农民合作社行业协会 | A kind of chicken droppings deodorant is dehydrated bio-fertilizer process line |
CN108795746A (en) * | 2018-07-26 | 2018-11-13 | 河南丰源和普农牧有限公司 | The independent segmented solid-state continuous fermentation system of aerobic-anaerobic and fermentation process |
CN114395455A (en) * | 2022-01-19 | 2022-04-26 | 四川轻化工大学 | Bottom liquid circulating spraying device of solid-state fermentation system |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080123 Termination date: 20110213 |