CN201420071Y - Solid state fermentation device - Google Patents
Solid state fermentation device Download PDFInfo
- Publication number
- CN201420071Y CN201420071Y CN 200920107689 CN200920107689U CN201420071Y CN 201420071 Y CN201420071 Y CN 201420071Y CN 200920107689 CN200920107689 CN 200920107689 CN 200920107689 U CN200920107689 U CN 200920107689U CN 201420071 Y CN201420071 Y CN 201420071Y
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- grate plate
- telescopic shaft
- fermentation
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- 238000010563 solid-state fermentation Methods 0.000 title claims abstract description 25
- 239000000463 material Substances 0.000 claims abstract description 39
- 238000000855 fermentation Methods 0.000 claims abstract description 35
- 230000004151 fermentation Effects 0.000 claims abstract description 35
- 238000009434 installation Methods 0.000 claims description 20
- 238000011081 inoculation Methods 0.000 claims description 16
- 238000007599 discharging Methods 0.000 claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- 230000005540 biological transmission Effects 0.000 claims description 6
- 238000004887 air purification Methods 0.000 claims description 4
- 230000033228 biological regulation Effects 0.000 claims description 4
- 238000010899 nucleation Methods 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 238000002156 mixing Methods 0.000 abstract description 2
- 238000009423 ventilation Methods 0.000 abstract description 2
- 230000002349 favourable effect Effects 0.000 abstract 1
- 230000003068 static effect Effects 0.000 abstract 1
- 230000001954 sterilising effect Effects 0.000 description 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 238000010564 aerobic fermentation Methods 0.000 description 4
- 238000004659 sterilization and disinfection Methods 0.000 description 4
- 230000001580 bacterial effect Effects 0.000 description 3
- 108090000790 Enzymes Proteins 0.000 description 2
- 102000004190 Enzymes Human genes 0.000 description 2
- 241000209149 Zea Species 0.000 description 2
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 2
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 235000005822 corn Nutrition 0.000 description 2
- 229940088598 enzyme Drugs 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 238000011169 microbiological contamination Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 229920002379 silicone rubber Polymers 0.000 description 2
- 239000004945 silicone rubber Substances 0.000 description 2
- 238000009827 uniform distribution Methods 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 108010059892 Cellulase Proteins 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229940106157 cellulase Drugs 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000012262 fermentative production Methods 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Classifications
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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
-
- 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
- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/02—Form or structure of the vessel
- C12M23/04—Flat or tray type, drawers
-
- 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
-
- 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
- C12M29/26—Conditioning fluids entering or exiting the reaction vessel
-
- 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
- C12M47/00—Means for after-treatment of the produced biomass or of the fermentation or metabolic products, e.g. storage of biomass
- C12M47/18—Gas cleaning, e.g. scrubbers; Separation of different gases
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- Life Sciences & Earth Sciences (AREA)
- Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Wood Science & Technology (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Organic Chemistry (AREA)
- Zoology (AREA)
- Biotechnology (AREA)
- Genetics & Genomics (AREA)
- Sustainable Development (AREA)
- Microbiology (AREA)
- Biochemistry (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Molecular Biology (AREA)
- Clinical Laboratory Science (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
The utility model provides a solid state fermentation device, which comprises a solid state fermentation tank, wherein the solid state fermentation tank mainly comprises the following components, namely, a hollow telescopic shaft in the middle of the tank body, at least two layers of grid plates fixed in the tank body through the air to bear the fermentation materials, scrapers arranged above eachlayer of grid plates, and nozzles arranged above each layer of grid plates. Various layers of grid plates as well as scrappers are arranged in the fermentation tank to realize the optimum blending ofthe fermentation materials, which is favorable for fermentation rate improvement; through controlling the thickness of the fermentation material layer and utilizing air cleaner for ventilation, the fermentation strain can breath in the atmosphere freely, thereby realizing the aerobic static culture, and reducing the investment and energy consumption, which can be applied to large-scale industrialized production.
Description
Technical field
The utility model relates to a kind of biological fermentation device, particularly a kind of solid-state fermentation installation.
Background technology
The way of stirring is stirred in existing solid-state aerobic fermentation device or employing makes material contact oxygen supply and heat radiation with air, can not satisfy the aerobic fermentation that some can only leave standstill cultivation; Adopt the pressurized air oxygen supply heat dissipation, energy consumption height, investment are bigger than normal; Adopt artificial or the so-called tray cultivation of semi-mechanization, dangerous, the microbiological contamination probability is big, and labour productivity is low, the incompatibility large-scale commercial production.
The utility model content
The purpose of this utility model is the shortcomings and deficiencies that exist at above-mentioned prior art, provides a kind of can be used in to leave standstill aerobic fermentation, energy consumption is low and efficient is high solid-state fermentation installation.For achieving the above object, the utility model provides a kind of solid-state fermentation installation, comprises solid-state fermenter, and this solid-state fermenter mainly comprises following assembly:
Tank body is fixed with hollow telescopic shaft in described jar of intravital central authorities, and described hollow telescopic shaft is sleeved on the Hollow Transmission Shafts that is connected with motor, and seals for running fit and by silicone rubber between Hollow Transmission Shafts; At least two-layer grate plate, described grate plate are sieve-plate structure, can see through air, have valve, be fixed in the tank body, and and tank body between do not have the gap, be used to carry fermentation materials, its number of plies depends on the thickness of tank body height and fermentation materials; Scraper plate is positioned at every layer of grate plate top, for flat straight oar formula structure, is fixed on the hollow telescopic shaft, is used for fermentation materials is evenly distributed to each layer grate plate; And nozzle, be positioned at every layer of grate plate top, be fixed on the hollow telescopic shaft and and communicate with its hollow passageway, be used for inoculation, steam sterilizing and adjusting humidity etc.
The shape and size of described grate plate are identical with the tank body cross section.
Described grate plate is the sieve-plate structure that the aperture is preferably 0.04～1.5mm, and its aperture is less than the smallest particles particle diameter of fermentation materials.
Described valve is that the circle of grate plate lacks, and its size is preferably 1/24～1/8 of this layer grate plate area, and fermentation materials can be distributed to lower floor's grate plate by valve.
The diameter of described scraper plate is identical with grate plate.
Described nozzle is the hollow tubular structures that has shower nozzle, and its shower nozzle is towards grate plate.
Distance between described scraper plate and nozzle and the grate plate can be by hollow telescopic shaft adjustment.
The charging valve is equipped with on the top of described solid-state fermenter, and it can link to each other with blender.
The inoculation valve is equipped with on the top of described solid-state fermenter, and it communicates with tank body by hollow telescopic shaft.
Described solid-state fermenter can link to each other with seeding tank by the inoculation valve.
The steam admission valve is equipped with on the top of described solid-state fermenter, and it communicates with tank body by hollow telescopic shaft.
The sterilized water valve is equipped with on the top of described solid-state fermenter, and it communicates with tank body by hollow telescopic shaft.
The top of described solid-state fermenter is connected with strainer by the emptying valve.
The bottom of described solid-state fermenter communicates with the air purification and regulation device by air intake valve.
Emptying auger is equipped with in the bottom of described solid-state fermenter, and it passes through the bleeder valve gate open to groove.
The bottom of described solid-state fermenter is provided with adjustment mechanism, in order to the adjustment level.
The technical process that utilizes above-mentioned solid-state fermentation installation to ferment is as follows:
Open the charging valve, make material to be fermented enter solid-state fermenter, adjust hollow telescopic shaft, make the thickness of the fermentation materials that the distance between scraper plate and nozzle and the grate plate equals to suit, and start hollow telescopic shaft and rotate, when treating that scraper plate is evenly distributed on fermentation materials on each layer grate plate, close the hollow telescopic shaft of charging valve and stall;
Adjust the emptying valve opening, open the steam admission valve, logical steam sterilizing sterilization, steam off admission valve after sterilization finishes is opened air intake valve and emptying valve, and cooling solid-state fermenter and fermentation materials ventilate;
Open the inoculation valve after reaching the temperature condition of inoculation, start hollow telescopic shaft rotation, by nozzle bacterial classification is evenly sprayed in material to be fermented, after inoculation is finished, close inoculation valve and the hollow telescopic shaft of stall, ferment, in the fermenting process, can open the sterilized water valve and start hollow telescopic shaft rotation, by nozzle sterilized water be sprayed in each layer fermentation materials, with the required moisture of afterfermentation process;
Treat that fermentation finishes, adjust hollow telescopic shaft, make scraper plate be adjacent to grate plate, and start hollow telescopic shaft, open discharging valve and each layer valve, open emptying auger simultaneously, the material in the solid-state fermenter is entered groove.
The utility model solid-state fermentation installation realizes that by multilayer grate plate and blade structure control bed thickness is set the best of fermentation materials is mixed and uniform distribution in tank body, help improving fermentation production rate; Its emptying valve communicates with strainer, greatly reduces the microbiological contamination probability; Thickness by the control fermented product bed of material and utilize air purifier ventilation oxygen supply, allow fermented bacterium freely breathe and get oxygen, less investment, energy consumption is low, running cost is low, thereby realized the aerobic space of having cultivated and made full use of fermentation of leaving standstill, added configurations such as mechanical input and output material, improved the efficient that leaves standstill aerobic fermentation to greatest extent, reduce production costs, can be applied to large-scale industrial production.
Description of drawings
Fig. 1 is the structural representation of the utility model solid-state fermentation installation embodiment.
Among the figure: 1, blender; 2, sterilized water valve; 3, steam admission valve; 4, inoculation valve; 5, seeding tank; 6, strainer; 7, emptying valve; 8, hollow telescopic shaft; 9, grate plate; 10, scraper plate; 11, nozzle; 12, tank body; 13, emptying auger; 14, discharging valve; 15, groove; 16, air purification and regulation device; 17, air intake valve; 18, charging valve; 19, adjustment mechanism.
Embodiment
Below in conjunction with drawings and Examples, embodiment of the present utility model done describing in further detail, but be not used for limiting scope of the present utility model.
The structural representation of a kind of embodiment of the utility model solid-state fermentation installation as shown in Figure 1, it comprises solid-state fermenter, this solid-state fermenter mainly comprises following assembly:
Tank body 12, central authorities in tank body 12 are fixed with hollow telescopic shaft 8, its up and down two ends by bearing fixing in the tank body upper and lower surface, hollow telescopic shaft 8 is sleeved on the Hollow Transmission Shafts that is positioned at tank body 12 tops, and seal for running fit and by silicone rubber between Hollow Transmission Shafts, Hollow Transmission Shafts is connected with motor;
Multilayer grate plate 9, grate plate 9 can see through air, be sieve-plate structure, the aperture is 0.04mm, the aperture should can be adjusted in 0.04～1.5mm scope by it less than the grain diameter of fermentation materials, and it is fixed in the tank body 12, shape and size are identical with tank body 12 cross sections, and do not have the gap between the tank body 12, be used to carry fermentation materials, its number of plies is by the decisions such as thickness of tank body height and fermentation materials, grate plate 9 has valve, valve is that the circle of grate plate lacks, and its size is 1/8 of this layer grate plate area, can select arbitrarily in 1/24～1/8 scope, be used for fermentation materials is distributed to lower floor's grate plate, be provided with valve in a side of the tank body 12 of every layer of grate plate correspondence and open Closing Switch;
Scraper plate 10 is positioned at every layer of grate plate 9 tops, is flat straight oar formula structure, is fixed on the hollow telescopic shaft 8, can be with hollow telescopic shaft 8 rotations, and its length is identical with the diameter of grate plate 9, is used for fermentation materials is evenly distributed to each layer grate plate 9;
Nozzle 11 is positioned at every layer of grate plate 9 tops, for having the hollow tubular structures of shower nozzle, communicate with the hollow passageway in the hollow telescopic shaft 8, its shower nozzle is fixed on the hollow telescopic shaft 8 towards grate plate 9, can be used for inoculation, steam sterilizing and adjusting humidity etc. with hollow telescopic shaft 8 rotations.
Charging valve 18, emptying valve 7 and the sterilized water valve 2 that communicates with hollow telescopic shaft 8, steam admission valve 3 and inoculation valve 4 are equipped with in the top of solid-state fermenter, and link to each other with blender 1 by charging valve 18, link to each other with seeding tank 5 by inoculation valve 4, thereby realize power feed and inoculation; Link to each other with strainer 6 by emptying valve 17, thereby preventing that outside air from entering pollutes.Air intake valve 17 is equipped with in the bottom of solid-state fermenter, and links to each other with air purification and regulation device 16 by air intake valve 17, is used for ventilating during the fermentation oxygen supply.Emptying auger 13 is equipped with in the bottom of solid-state fermenter, and leads to groove 15 by discharging valve 14, thereby realizes mechanical discharging.
The bottom of solid-state fermenter also is provided with adjustment mechanism 19, so that it is placed in the production site place reposefully.
Below be main raw material with the ground corn core, utilize above-mentioned solid-state fermentation installation fermentative production cellulase, further specify and utilize the utility model solid-state fermentation installation to carry out the method for solid state fermentation:
(1) adjust hollow telescopic shaft 8, making the vertical range between scraper plate 10 and the grate plate 9 is bed thickness; Again the top adding of ground corn core (treating fermentation materials) from blender 1 mixed, open charging valve 18 after thorough mixing is even, make and treat that fermentation materials enters in the solid-state fermenter 12; Open Closing Switch by valve then and open each layer valve successively, start hollow telescopic shaft 8 rotations, scraper plate 10 rotates thereupon, earlier with the even cloth of material on the superiors' grate plate, along with material constantly enter scraper plate 10 with the valve uniform distribution cloth of unnecessary material by grate plate to lower floor's grate plate, and the like be covered with all grate plates; Observe by visor and to treat that material is evenly distributed to the orlop grate plate, close the last layer valve, and the like when treating that material is evenly distributed on each layer grate plate, close charging valve 18 and top layer valve, the hollow telescopic shaft 8 of stall when treating that top layer grate plate material is evenly distributed;
(2) aperture of adjustment emptying valve 7, open steam admission valve 3, about about 1 minute of aperture adjusting discharging valve 14 is so that after discharging freezing air, close discharging valve 14, logical steam sterilizing sterilization, 121 ℃ of sterilizations be after 1 hour, steam off admission valve 3, open air intake valve 17 and emptying valve 7, cooling solid-state fermenter and fermentation materials ventilate;
When (3) treating that temperature is reduced to 35 ℃ in the fermentor tank, open inoculation valve 4, start hollow telescopic shaft 8 rotations, by nozzle 11 bacterial classification is evenly sprayed in material to be fermented, inoculative proportion is 1m
3Treat fermentation materials/0.1～0.5m
3Seed liquor after inoculation is finished, is closed inoculation valve 4 and the hollow telescopic shaft 8 of stall, ferments; During the fermentation, opened sterilized water valve 2 and hollow telescopic shaft 8 every 8～24 hours once, by nozzle 11 sterilized water evenly is sprayed at and carries out the growth that moisture control is beneficial to bacterial classification in the material that is fermenting;
(4) fermentation was adjusted hollow telescopic shaft 8 after 10 days, made scraper plate 10 be adjacent to grate plate 9, started hollow telescopic shaft 8 rotations then, and opened valve, discharging valve 14 and emptying auger 13, and the material that fermentation in the solid-state fermenter is finished enters groove 15.
From the material that fermentation finishes,, can get the dry cellulosic enzyme 2.8m of 185Iu/g with the method oven dry of cryodrying
3(1.15 tons), dried enzyme current consumption per ton is less than 150KWh.
Certainly; the utility model also can have other embodiment; under the situation of the utility model spirit and essence thereof; those of ordinary skill in the art can make various corresponding changes and distortion according to the utility model, but these corresponding changes and distortion all should belong to the protection domain of claim of the present utility model.
Claims (10)
1, a kind of solid-state fermentation installation is characterized in that, comprises solid-state fermenter, and this solid-state fermenter mainly comprises following assembly:
Tank body is fixed with hollow telescopic shaft in described jar of intravital central authorities, and described hollow telescopic shaft is sleeved on the Hollow Transmission Shafts that is connected with motor;
At least two-layer grate plate, described grate plate are sieve-plate structure, can see through air, have valve, be fixed in the tank body, and and tank body between do not have the gap;
Scraper plate is positioned at every layer of grate plate top, for flat straight oar formula structure, is fixed on the hollow telescopic shaft; With
Nozzle is positioned at every layer of grate plate top, is fixed on the hollow telescopic shaft and with its hollow passageway to communicate.
2, solid-state fermentation installation as claimed in claim 1 is characterized in that, described grate plate is that the aperture is the sieve-plate structure of 0.04～1.5mm, and its shape and size are identical with the tank body cross section.
3, solid-state fermentation installation as claimed in claim 1 is characterized in that, described valve is that the circle of grate plate lacks, and its size is 1/24～1/8 of a described grate plate area, and fermentation materials can be distributed to lower floor's grate plate by valve.
4, solid-state fermentation installation as claimed in claim 1 is characterized in that, the diameter of described scraper plate is identical with grate plate.
5, solid-state fermentation installation as claimed in claim 1 is characterized in that, described nozzle is the hollow tubular structures that has shower nozzle, and its shower nozzle is towards grate plate.
6, solid-state fermentation installation as claimed in claim 1 is characterized in that, the distance between described scraper plate and nozzle and the grate plate can be by hollow telescopic shaft adjustment.
7, solid-state fermentation installation as claimed in claim 1 is characterized in that, charging valve and emptying valve are equipped with in the top of described solid-state fermenter, link to each other with blender by the charging valve, link to each other with strainer by the emptying valve.
8, solid-state fermentation installation as claimed in claim 1 is characterized in that, inoculation valve, steam admission valve and sterilized water valve are equipped with in the top of described solid-state fermenter, and it communicates with tank body by hollow telescopic shaft, wherein inoculates valve and links to each other with seeding tank.
9, solid-state fermentation installation as claimed in claim 1 is characterized in that, air intake valve and discharging valve are equipped with in the bottom of described solid-state fermenter, communicate with the air purification and regulation device by air intake valve, by the bleeder valve gate open to groove.
10, as each described solid-state fermentation installation of claim 1～9, it is characterized in that the bottom of described solid-state fermenter is provided with adjustment mechanism.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200920107689 CN201420071Y (en) | 2009-05-08 | 2009-05-08 | Solid state fermentation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200920107689 CN201420071Y (en) | 2009-05-08 | 2009-05-08 | Solid state fermentation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201420071Y true CN201420071Y (en) | 2010-03-10 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200920107689 Expired - Lifetime CN201420071Y (en) | 2009-05-08 | 2009-05-08 | Solid state fermentation device |
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| CN (1) | CN201420071Y (en) |
Cited By (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101978874A (en) * | 2010-10-09 | 2011-02-23 | 中国轻工业武汉设计工程有限责任公司 | Multi-layer soy sauce starter-making tower device |
| CN102776123A (en) * | 2012-07-13 | 2012-11-14 | 中国科学院过程工程研究所 | Waste continuous solid fermenting reacting device and solid fermenting method |
| CN102839112A (en) * | 2012-08-30 | 2012-12-26 | 浙江森力机械科技有限公司 | Vertical continuous fermentation tank set |
| CN103103066A (en) * | 2013-02-02 | 2013-05-15 | 孙祯芳 | Combined type solid fermenting device |
| CN103627622A (en) * | 2012-08-23 | 2014-03-12 | 广西力源宝农林科技发展有限责任公司 | Helical flipping and stirring shaft of helical fermentation flipping and stirring machine |
| TWI472612B (en) * | 2012-12-12 | 2015-02-11 | ||
| CN104603257A (en) * | 2012-06-06 | 2015-05-06 | 诺维信生物农业公司 | Solid state bioreactor adapted for automation |
| CN104697358A (en) * | 2013-12-05 | 2015-06-10 | 北新集团建材股份有限公司 | Vertical-type powder cooler |
| CN104845877A (en) * | 2015-04-17 | 2015-08-19 | 南京工业大学 | Solid-state fermentation reactor and application thereof |
| CN104928169A (en) * | 2015-06-24 | 2015-09-23 | 南安市绿野沼气技术开发研究所 | Simple methane fermenting device |
| CN105349409A (en) * | 2015-11-25 | 2016-02-24 | 清华大学 | Device for continuously producing biogas by means of solid-state fermentation |
| CN106381267A (en) * | 2016-08-31 | 2017-02-08 | 西安若翰生物饲料有限公司 | Simple efficient solid fermentation device |
| CN106916730A (en) * | 2017-03-24 | 2017-07-04 | 招商局生态环保科技有限公司 | Batch-type microorganism incubator |
| CN107955777A (en) * | 2017-12-13 | 2018-04-24 | 广西南宁秀珀生物科技有限公司 | Rotary solid material fermentation device |
| CN108102895A (en) * | 2017-12-13 | 2018-06-01 | 广西南宁秀珀生物科技有限公司 | Multiple field solid material installation for fermenting |
| CN109182017A (en) * | 2018-09-29 | 2019-01-11 | 湖南黄氏蜂业有限公司 | A kind of wasp liquor brewing stowage arrangement |
| CN111268874A (en) * | 2019-12-30 | 2020-06-12 | 西安金清泰环境科技有限公司 | Leveling structure of sludge treatment tank |
| CN112314333A (en) * | 2019-07-16 | 2021-02-05 | 郝天顺 | Fermentation equipment and fermentation method for edible fungus cultivation material |
-
2009
- 2009-05-08 CN CN 200920107689 patent/CN201420071Y/en not_active Expired - Lifetime
Cited By (24)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101978874A (en) * | 2010-10-09 | 2011-02-23 | 中国轻工业武汉设计工程有限责任公司 | Multi-layer soy sauce starter-making tower device |
| CN104603257A (en) * | 2012-06-06 | 2015-05-06 | 诺维信生物农业公司 | Solid state bioreactor adapted for automation |
| CN102776123A (en) * | 2012-07-13 | 2012-11-14 | 中国科学院过程工程研究所 | Waste continuous solid fermenting reacting device and solid fermenting method |
| CN102776123B (en) * | 2012-07-13 | 2014-06-04 | 中国科学院过程工程研究所 | Waste continuous solid fermenting reacting device and solid fermenting method |
| CN103627622A (en) * | 2012-08-23 | 2014-03-12 | 广西力源宝农林科技发展有限责任公司 | Helical flipping and stirring shaft of helical fermentation flipping and stirring machine |
| CN102839112A (en) * | 2012-08-30 | 2012-12-26 | 浙江森力机械科技有限公司 | Vertical continuous fermentation tank set |
| TWI472612B (en) * | 2012-12-12 | 2015-02-11 | ||
| CN103103066B (en) * | 2013-02-02 | 2014-09-03 | 孙祯芳 | Combined type solid fermenting device |
| CN103103066A (en) * | 2013-02-02 | 2013-05-15 | 孙祯芳 | Combined type solid fermenting device |
| CN104697358B (en) * | 2013-12-05 | 2018-04-20 | 北新集团建材股份有限公司 | A kind of vertical powder cooler |
| CN104697358A (en) * | 2013-12-05 | 2015-06-10 | 北新集团建材股份有限公司 | Vertical-type powder cooler |
| CN104845877A (en) * | 2015-04-17 | 2015-08-19 | 南京工业大学 | Solid-state fermentation reactor and application thereof |
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