CN2535414Y - Straw solid state fermenting alcoho reactor - Google Patents
Straw solid state fermenting alcoho reactor Download PDFInfo
- Publication number
- CN2535414Y CN2535414Y CN 02209272 CN02209272U CN2535414Y CN 2535414 Y CN2535414 Y CN 2535414Y CN 02209272 CN02209272 CN 02209272 CN 02209272 U CN02209272 U CN 02209272U CN 2535414 Y CN2535414 Y CN 2535414Y
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- CN
- China
- Prior art keywords
- tank body
- solid state
- utility
- model
- alcohol
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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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
- C12M21/12—Bioreactors or fermenters specially adapted for specific uses for producing fuels or solvents
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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
- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/38—Caps; Covers; Plugs; Pouring means
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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
- C12M33/00—Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus
- C12M33/14—Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus with filters, sieves or membranes
Abstract
The utility model discloses a straw solid state fermentation alcohol reactor. The purpose of the utility model is to provide a device for meeting the requirement of producing alcohol via the solid state fermentation of straw in great scale. The utility model has the technical proposal that the utility model comprises a tank body 16 and a tank cover 7; the utility model is characterized in that a moveable arm 9 is arranged above the tank body 16, a straw dividing device 10, a yeast inoculation spray head 8 and a water spray head 11 are arranged on the arm 9, and an extraction basket 12 is arranged in the tank body; a steam hole 19, a sterile air hole 18 and an alcohol reclamation hole 17 are arranged on the tank body. The utility model has the functions of sterilization of a tank body, inactivation of waste straw and coarse extraction of alcohol; the utility model has the advantages of reasonable structural design, large capacity of fermentation, simple and convenient operation, high productive efficiency, etc.
Description
Technical field
It is the bio-reactor that raw material by solid fermentation is produced alcohol with stalk that the utility model relates to a kind of.
Background technology
China is agriculture production big country, nearly 600,000,000 tons of the wastes straw of annual all kinds of farm crop, aboundresources, cheap.The process that transforms for cellulosic material has two kinds of approach, i.e. liquid state fermentation and solid state fermentation, but have the problem of environmental pollution that is difficult for overcoming because alcohol is produced in liquid state fermentation, solid state fermentation more and more obtains people's attention in recent years.Solid bio-reactor is suitable growing environment to be provided or to carry out the equipment of specific biochemical reaction for specific cell or enzyme.Its form has six classes: disc type, and filling bed type, rotary drum, swing, the stirred vessel formula, gas-solid fluid bed formula reactor also has the report that utilizes fermentation vat to produce.The filling bed type of practical application at present, rotary drum, swing, the stirred vessel formula, though gas-solid fluid bed formula solid-state fermentation reactor can effectively keep gnotobasis and carry out complicated control, it is little that these a few class reactor ubiquities are produced volume, the equipment manufacturing cost height, the shortcoming that moving parts is easy to wear, especially because of its actual yielding poorly, the fermenting process low for value of the product can not obtain satisfied economic benefit with their.Existing large-scale disc type reactor and fermentation vat production, though can a lot of fermented material of primary treatment, because its design is rough, fermentation parameter is wayward, and fermented material directly contacts the bacterium difficulty of mixing of going out with air.The another one problem is that the charging and the discharging of disc type reactor and fermentation vat production needs artificial to participate in, and it is long that input and output material takies man-hour, operational difficulty, and incompatible extensive efficient industrial production requirement.
Summary of the invention
The objective of the invention is to provide a kind of stalk solid state fermentation alcohol reactor, and make its adaptation and satisfy the particular requirement that utilizes stalk solid state fermentation large-scale production alcohol.
Comprise tank body 16, cover 7 in order to reach the technical scheme that the purpose of this utility model takes, it is characterized in that, above tank body 16, be provided with moveable arm 9, material-homogenating device 10, yeast-inoculated shower nozzle 8 and sprinkler head 11 are installed on this moveable arm 9, hand basket 12 is housed in tank body 16; On tank body 16, can establish logical steam hole 19, sterile air hole 18 and alcohol recovery holes 17, on cover 7, establish alcohol recovery holes 6.
Above-mentioned stalk solid state fermentation alcohol reactor is characterized in that, is provided with lifting gear 2 above cover 7.
Above-mentioned stalk solid state fermentation alcohol reactor is characterized in that, is provided with controller 3, gaseous constituent measuring element 4 and detector unit 5 on cover 7.
Above-mentioned stalk solid state fermentation alcohol reactor is characterized in that, is provided with packing ring and hold-down gear 13 between tank body 16 and cover 7.
Above-mentioned stalk solid state fermentation alcohol reactor is characterized in that yeast-inoculated shower nozzle 8 and sprinkler head 11 have several, circumferentially is uniformly distributed in the side top of material-homogenating device 10.
The advantage that solid-state fermentation reactor had that possesses above constitutional features is as follows:
Because the utility model has adopted the basket type structure, and is furnished with lifting gear 2, realized input and output material operation easily and fast, shortened the production cycle greatly; Being equipped with of material-homogenating device 10 and yeast-inoculated shower nozzle 8 and sprinkler head 11 makes base-material can mix preferably with additives such as yeast; Because the setting of moveable arm 9, outside the extensible tank body of material-homogenating device, thereby guaranteed effective fermenting space of tank body, help the maximization of realization response device; Controller 3, gaseous constituent measuring element 4 and detector unit 5 the good control that has guaranteed reaction process is set, make this device more convenient to operate; The configuration of logical steam hole 19, sterile air hole 18 and alcohol recovery holes 17 has realized that alcohol heats up in a steamer to get and waste material deactivation work, makes production technique be integrated, and has improved production efficiency and has reduced production cost.So, the sterilization of the utility model collection tank body, waste material deactivation, product alcohol slightly be extracted as one, have reasonable in design, the fermentation capacity is big, and is simple to operation, the production efficiency advantages of higher.
Description of drawings
Fig. 1 is the structural representation of the utility model stalk solid state fermentation alcohol reactor;
Fig. 1 is the working state schematic representation of the utility model stalk solid state fermentation alcohol reactor.
Specific embodiments
Below in conjunction with accompanying drawing embodiment of the present utility model is described.
As shown in Figure 1,1 is support, which is provided with lifting gear 2 and moveable arm 9, it is controller that moveable arm 9 is provided with material-homogenating device 10, yeast-inoculated shower nozzle 8 and sprinkler head 11,3, and 4 is the gaseous constituent measuring element, 5 is detector unit, and 6 and 17 are the alcohol recovery holes, and 7 is cover, 12 is hand basket, and 13 is packing ring and hold-down gear, and 14 is thermal insulation layer, 15 are the hand basket support, 16 is tank body, and 18 is the sterile air hole, and 19 are logical steam hole.
Cover 7 that can promote and fixed tank body 16 constitute the agent structure of reactor; The lifting gear 2 of reactor head is used to promote cover or hand basket to certain altitude, so that charging and discharging; Material-homogenating device 10 is fixed on the moveable arm 9, is in the tank body top during charging, shifts out in the fermenting process, is used to realize the enzyme song, the mixing of straw powder, and be uniformly distributed in the reactor hand basket; Inoculation of yeast spray-type and the adjustment of base-material moisture are finished in cloth by yeast-inoculated shower nozzle 8 and sprinkler head 11; Gaseous constituent measuring element 4 on the cover (monitoring gas phase CO
2And alcoholic content) and detector unit 5, and by auxiliary Controlling System (among the figure 3) solid ferment process is controlled; Alcohol recovery holes 6 be used for reclaiming heat up in a steamer alcohol; Excellent sealing between cover and tank body is realized by packing ring and hold-down gear 13; Hand basket 12 is used to carry base-material, and its outer wall is a metal mesh material, and is gapped between it and the reactor wall, in order to ventilated, after fermentation is finished and is led to steam and carry out alcoholic extraction and waste material deactivation, can waste material be taken out by lifting gear, carry out continuously in order to producing; The hand basket of tank base supports 15 can make hand basket keep stable; There are certain interval in basket fabric and reactor wall, in order to ventilation; The work of ventilation, humidification, adjusting Qu Wen is finished in the logical sterile air hole 18 of reactor bottom; Logical steam hole 19 is finished alcohol and is heated up in a steamer and get and waste material deactivation work; Distilled alcohol mother liquor can directly be entered by alcohol recovery holes 17 and carry out rectifying in the alcohol distillation tower.
Claims (5)
1, a kind of stalk solid state fermentation alcohol reactor, comprise tank body (16), cover (7), it is characterized in that, be provided with moveable arm (9) in the top of tank body (16), material-homogenating device (10), yeast-inoculated shower nozzle (8) and sprinkler head (11) are installed on this moveable arm (9), hand basket (12) is housed in tank body (16); On tank body (16), can establish logical steam hole (19), sterile air hole (18) and alcohol recovery holes (17), on cover (7), establish alcohol recovery holes (6).
2, stalk solid state fermentation alcohol reactor according to claim 1 is characterized in that, is provided with lifting gear (2) in the top of cover (7).
3, stalk solid state fermentation alcohol reactor according to claim 1 and 2 is characterized in that, is provided with controller (3), gaseous constituent measuring element (4) and detector unit (5) on cover (7).
4, stalk solid state fermentation alcohol reactor according to claim 1 and 2 is characterized in that: be provided with packing ring and hold-down gear (13) between tank body (16) and cover (7).
5, stalk solid state fermentation alcohol reactor according to claim 1 and 2, it is characterized in that: yeast-inoculated shower nozzle (8) and sprinkler head (11) have several, circumferentially are uniformly distributed in the side top of material-homogenating device (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 02209272 CN2535414Y (en) | 2002-04-12 | 2002-04-12 | Straw solid state fermenting alcoho reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 02209272 CN2535414Y (en) | 2002-04-12 | 2002-04-12 | Straw solid state fermenting alcoho reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2535414Y true CN2535414Y (en) | 2003-02-12 |
Family
ID=33689731
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 02209272 Expired - Fee Related CN2535414Y (en) | 2002-04-12 | 2002-04-12 | Straw solid state fermenting alcoho reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2535414Y (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101130791B (en) * | 2006-08-25 | 2010-05-12 | 中国科学院过程工程研究所 | Device and method for solid-state fermentation and preparation of alcohol using sorgo stalk |
| CN101085995B (en) * | 2007-06-08 | 2010-05-26 | 清华大学 | Method and system for separating ethanol based on sweet sorghum stalk solid ferment material |
| CN101948874A (en) * | 2010-09-15 | 2011-01-19 | 西北农林科技大学 | Method for solving problems of direct fermentation and suspension of straw for rural household biogas digesters |
| CN101235391B (en) * | 2008-02-01 | 2011-08-17 | 清华大学 | Method and system for continuously separating ethanol and utilizing residual heat based on solid-state fermentation material |
| CN101503713B (en) * | 2009-03-11 | 2011-12-28 | 清华大学 | Fermentation / distillation integrated technique apparatus for producing alcohol from sugar |
| CN101724661B (en) * | 2008-10-24 | 2013-06-26 | 天津实发中科百奥工业生物技术有限公司 | Process and system for producing ethanol through solid-state continuous fermentation and distillation of sorgo straws |
| CN105460456A (en) * | 2015-12-17 | 2016-04-06 | 乌毡帽酒业有限公司 | Convenient type tank cover opening structure |
| CN106974298A (en) * | 2017-05-23 | 2017-07-25 | 成都衔石科技有限公司 | It is easy to export the explosion mechanism of filter residue |
-
2002
- 2002-04-12 CN CN 02209272 patent/CN2535414Y/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101130791B (en) * | 2006-08-25 | 2010-05-12 | 中国科学院过程工程研究所 | Device and method for solid-state fermentation and preparation of alcohol using sorgo stalk |
| CN101085995B (en) * | 2007-06-08 | 2010-05-26 | 清华大学 | Method and system for separating ethanol based on sweet sorghum stalk solid ferment material |
| CN101235391B (en) * | 2008-02-01 | 2011-08-17 | 清华大学 | Method and system for continuously separating ethanol and utilizing residual heat based on solid-state fermentation material |
| CN101724661B (en) * | 2008-10-24 | 2013-06-26 | 天津实发中科百奥工业生物技术有限公司 | Process and system for producing ethanol through solid-state continuous fermentation and distillation of sorgo straws |
| CN101503713B (en) * | 2009-03-11 | 2011-12-28 | 清华大学 | Fermentation / distillation integrated technique apparatus for producing alcohol from sugar |
| CN101948874A (en) * | 2010-09-15 | 2011-01-19 | 西北农林科技大学 | Method for solving problems of direct fermentation and suspension of straw for rural household biogas digesters |
| CN105460456A (en) * | 2015-12-17 | 2016-04-06 | 乌毡帽酒业有限公司 | Convenient type tank cover opening structure |
| CN106974298A (en) * | 2017-05-23 | 2017-07-25 | 成都衔石科技有限公司 | It is easy to export the explosion mechanism of filter residue |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |