CN101768542A - Peristaltic anaerobic solid-state fermentation device used for organic acid fermentation - Google Patents
Peristaltic anaerobic solid-state fermentation device used for organic acid fermentation Download PDFInfo
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- CN101768542A CN101768542A CN 201010113580 CN201010113580A CN101768542A CN 101768542 A CN101768542 A CN 101768542A CN 201010113580 CN201010113580 CN 201010113580 CN 201010113580 A CN201010113580 A CN 201010113580A CN 101768542 A CN101768542 A CN 101768542A
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- organic acid
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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
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/12—Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
- C12M41/18—Heat exchange systems, e.g. heat jackets or outer envelopes
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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
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/30—Means for regulation, monitoring, measurement or control, e.g. flow regulation of concentration
- C12M41/34—Means for regulation, monitoring, measurement or control, e.g. flow regulation of concentration of gas
Abstract
The invention discloses a peristaltic anaerobic solid-state fermentation device used for organic acid fermentation. The invention is characterized in that a stub driven by electricity and connected on a fixed shaft can sway along the axle center to strengthen the motion of the solid-state material in a reactor, thereby improving the mass and heat transfer in the reactor and reducing the energy consumption; a filter layer is arranged in the device for realizing the solid-liquid separation of the material; acidizing fluid rich in thalluses stored under the filter layer is conveyed to the top of a pot body by a peristaltic pump and then sprayed on the material uniformly by a spraying head for secondary fermentation, thereby being favorable for further shortening the fermentation period and saving water and energy.
Description
[technical field]
The invention belongs to the organic acid fermentation field, specially refer to creeping type anaerobic solid-state fermentation organic acid device.
[background technology]
Along with the development of socio-economic activity and production, the human living standard is able to rapid raising, but thereupon many environmental problems also occurred, and increasing solid waste is one of them.Be rich in degradable organism mostly as agricultural wastes, daily life rubbish etc. in the solid waste, through microbiological deterioration, can be converted into valuable product, can reduce environmental pollution, can bring certain economic benefits again, so the anaerobic fermentation technology of solid waste is a technology that has a extensive future.
In the whole technique link of anaerobic solid-state fermentation, the acidication of solid waste is one of its rate-limiting step, and the acidication of therefore strengthening solid waste is to shorten the solid waste anaerobic digestion cycle, improves an emphasis of digestive efficiency.A difficult point in the solid waste acidication process is exactly the inequality of heat transfer, mass transfer, traditional mode is by add agitator in reactor solid substances to be stirred, come enhancement of heat transfer, mass transfer, but, cause stirring operation energy consumption height, weak effect, its shearing force again to consequences such as microbial growth work the mischief because fermentation materials is highly filled.
[summary of the invention]
At the deficiency that exists in the above-mentioned solid waste anaerobic acidification process, the present invention has proposed following scheme for solving this difficult problem: utilize bionics technical modelling food limit wriggling in stomach and intestine, the process of limit digestion has designed the anaerobic solid-state fermentation device that a kind of creeping motion type is used for organic acid fermentation.Its feature is as follows: this device comprises tank body, opening for feed, discharge port, venting port, stationary shaft, stub, spray thrower, peristaltic pump, filtering layer etc., be provided with four groups of stubs that are vertical arrangement in tank interior, stub is that axial motion is done in the center of circle with the stationary shaft, drives the motion of reactor internal solid material, and material is wriggled on the inside reactor limit, the limit digests, thereby has strengthened mass transfer, the heat transfer of inside reactor solid substances.By filtering layer solid substances is trapped in the filtering layer place, the acidizing fluid that produces is stayed in lower floor's jar, to be rich in the zymophyte acidizing fluid from what filtering layer was stored down, be back to reactor head by peristaltic pump, and evenly be sprayed on the solid substances through spray thrower, carry out Secondary Fermentation, this can not only effectively accelerate the acidication speed of solid substances, and need not additionally to add water and make organic acid keep higher concentration.
Reinforcement organic acid solid-state fermentation installation according to technical scheme provides is characterized in that: have four row stubs in the tank body and fix on it by stationary shaft, every an angle of 90 degrees row of arranging, every row are made up of 3-20 stub;
Reinforcement organic acid solid-state fermentation installation according to technical scheme provides is characterized in that: at equally distributed 4 stubs of the sustained height of tank body, be that swing with horizontal direction work ± miter angle in the axle center with the stationary shaft;
Reinforcement organic acid solid-state fermentation installation according to technical scheme provides is characterized in that: stub length is 1 with the ratio of reactor diameter: 10-1: 100.
[advantage of the present invention]
The present invention compares with existing conventional solid waste anaerobic digestion organic acid device and has the following advantages: (1) structure of reactor is simple, by the swing of stub, solid substances is pushed, rubs, thereby strengthened mass transfer, the heat transfer of solid substances; (2) improved the stability of system, and effectively shortened the solid substances anaerobic digestion organic acid cycle, cut down the consumption of energy, thereby improved production efficiency.
[description of drawings]
Fig. 1 is this schematic representation of apparatus
Fig. 2 is the A-A sectional view of this device
1 is venting hole among the figure, and 2 is opening for feed, and 3 is spray thrower, and 4 is axial brake device, and 5 is stationary shaft, and 6 is tank wall, and 7 is stub, and 8 is filtering layer, and 9 is discharge port, and 10 is peristaltic pump.
[specific implementation method]
Embodiment 1
Will be through the quick-fried pretreated maize straw of vapour and daily life rubbish thorough mixing outside jar, the anaerobic sludge of sewage work is taken from inoculation, moves in the reactor sealing, the fermentation of beginning organic acid then in the lump from opening for feed.Cycle is 10 days, temperature is controlled at 35-40 ℃, during the fermentation, the stub of inside reactor is done ± the miter angle swing for the axle center along continuous straight runs with the stationary shaft, every 30min once, being in symmetric two stubs of sustained height during swing is one group, and with another the group alternating action on material, by the crisscross motion between stub, the motion of enhanced reactor internal solid material.In the fermenting process, every 8 hours, the acidizing fluid with being stored under the filtering layer was transported to the tank top through peristaltic pump, evenly was sprayed onto the material top by spray header, realized its internal recycling, kept and produced sour dominant microflora, quickened the acidifying of solid substances.After the fermentation ends, collect acidizing fluid.
Claims (5)
1. a creeping motion type is used for anaerobic solid-state fermentation organic acid device, comprise tank body, opening for feed, discharge port, venting port, stationary shaft, stub, spray thrower, peristaltic pump, filtering layer are provided with four groups of stubs that are vertical arrangement in tank interior, stub is that axial motion is done in the center of circle with the stationary shaft, drives the motion of reactor internal solid material.
2. a kind of creeping motion type as claimed in claim 1 is used for solid state fermentation organic acid device, it is characterized in that: the stub that is installed in tank interior is that the axle center swings back and forth with the stationary shaft.
3. a kind of creeping motion type as claimed in claim 1 is used for solid state fermentation organic acid device, it is characterized in that: have four row stubs in the tank body and fix on it by stationary shaft, every an angle of 90 degrees row of arranging, every row are made up of 3-20 stub.
4. a kind of creeping motion type as claimed in claim 1 is used for solid state fermentation organic acid device, it is characterized in that: stub is that swing with horizontal direction work ± miter angle in the axle center with the stationary shaft.
5. a kind of creeping motion type as claimed in claim 1 is used for solid state fermentation organic acid device, it is characterized in that: stub length is 1 with the ratio of reactor diameter: 10-1: 100.
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CN 201010113580 CN101768542B (en) | 2010-02-24 | 2010-02-24 | Peristaltic anaerobic solid-state fermentation device used for organic acid fermentation |
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CN 201010113580 CN101768542B (en) | 2010-02-24 | 2010-02-24 | Peristaltic anaerobic solid-state fermentation device used for organic acid fermentation |
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CN101768542B CN101768542B (en) | 2012-10-24 |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109384363A (en) * | 2018-10-31 | 2019-02-26 | 山东大学 | A kind of Gao Hangu anaerobic digestion reaction unit and its working method |
CN110484436A (en) * | 2019-09-05 | 2019-11-22 | 四川火尔赤清洁能源有限公司 | Bionical dry-type anaerobic fermentation device |
WO2021227282A1 (en) * | 2020-05-15 | 2021-11-18 | 同济大学 | Device and method for enhancing anaerobic digestion of sludge based on conical-serpentine tube coupling |
Citations (4)
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---|---|---|---|---|
DE3341691A1 (en) * | 1983-11-18 | 1985-05-30 | Walter 8531 Schauerheim Feilhauer | Process and apparatus for the anaerobic treatment of organic substances |
CN1904031A (en) * | 2006-08-08 | 2007-01-31 | 吉林大学 | Fermentation tank |
CN101182457A (en) * | 2007-11-29 | 2008-05-21 | 南京工业大学 | Device for high-density production of organic acid by combination of fibrous bed bioreactor and membrane separation technology |
JP2008161071A (en) * | 2006-12-27 | 2008-07-17 | Toray Ind Inc | Method for operating membrane bioreactor |
-
2010
- 2010-02-24 CN CN 201010113580 patent/CN101768542B/en not_active Expired - Fee Related
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3341691A1 (en) * | 1983-11-18 | 1985-05-30 | Walter 8531 Schauerheim Feilhauer | Process and apparatus for the anaerobic treatment of organic substances |
CN1904031A (en) * | 2006-08-08 | 2007-01-31 | 吉林大学 | Fermentation tank |
JP2008161071A (en) * | 2006-12-27 | 2008-07-17 | Toray Ind Inc | Method for operating membrane bioreactor |
CN101182457A (en) * | 2007-11-29 | 2008-05-21 | 南京工业大学 | Device for high-density production of organic acid by combination of fibrous bed bioreactor and membrane separation technology |
Non-Patent Citations (3)
Title |
---|
《化工科技市场》 20010228 陈洪章,李佐虎 微生物固态发酵反应器 25-27 1-5 , 第2期 * |
《化工进展》 20020131 陈洪章,李佐虎 固态发酵新技术及其反应器的研制 37-42 1-5 第21卷, 第1期 * |
《食品与发酵工业》 20090131 俞志敏等 农用废弃物固态发酵生产衣康酸工艺研究 99-102 1-5 第35卷, 第1期 * |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109384363A (en) * | 2018-10-31 | 2019-02-26 | 山东大学 | A kind of Gao Hangu anaerobic digestion reaction unit and its working method |
CN110484436A (en) * | 2019-09-05 | 2019-11-22 | 四川火尔赤清洁能源有限公司 | Bionical dry-type anaerobic fermentation device |
CN110484436B (en) * | 2019-09-05 | 2022-09-27 | 四川火尔赤清洁能源有限公司 | Bionic dry anaerobic fermentation device |
WO2021227282A1 (en) * | 2020-05-15 | 2021-11-18 | 同济大学 | Device and method for enhancing anaerobic digestion of sludge based on conical-serpentine tube coupling |
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