CN202322832U - Soft garage type anaerobic dry fermentation device - Google Patents
Soft garage type anaerobic dry fermentation device Download PDFInfo
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- CN202322832U CN202322832U CN2011204885612U CN201120488561U CN202322832U CN 202322832 U CN202322832 U CN 202322832U CN 2011204885612 U CN2011204885612 U CN 2011204885612U CN 201120488561 U CN201120488561 U CN 201120488561U CN 202322832 U CN202322832 U CN 202322832U
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- 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
- C12M21/04—Bioreactors or fermenters specially adapted for specific uses for producing gas, e.g. biogas
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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
- C12M29/02—Percolation
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- 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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- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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Abstract
The utility model belongs to the technical field of microbial fermentation, and relates to a soft garage type anaerobic dry fermentation device which consists of a garage type fermentation bin (1), a soft sealing membrane (5), a biogas outlet (4), a leachate spraying head (3), a leachate collection groove (6), a leachate collection tank (8), a water pump (12), a liquid pumping port (11), a liquid inlet (14) and an inoculation port (9). The device provided by the utility model has the advantages of fast fermentation speed, high gas production efficiency and the like, realizes convenient material feed and discharge, avoids aftertreatment of waste liquid, and is simple to construct, safe and reliable and easy to realize large-scale production.
Description
Technical field
The utility model belongs to the microbial fermentation technology field, relates to the anaerobic ferment devices that biomass wastes such as utilizing agricultural crop straw, fowl and animal excrement, domestic organic garbage is produced biogas energy, particularly a kind of software garage type anaerobic dry fermentation device.
Background technology
The mass-producing methane engineering technology has become the important support of China's energy resource supply and environment protection in the application of renewable energy source and field of environment protection.At present, methane engineering technology can be divided into wet fermentation of anaerobism and anaerobic dry fermentation two big classes.At present; The wet fermentation technique of anaerobism has been widely used in culturing the biogas fermentation production of lower concentration materials such as manure of livestock and poultry dirt, various organic waste waters; The cogeneration because China's biogas engineering is unrealized mostly; The wet fermentation technique of anaerobism is implemented to want consumes energy to be used to keep suitable leavening temperature at cold district, and is low in economic efficiency even unable to make ends meet, big limitations wet the applying of fermenting of anaerobism at north cold area.And the wet fermentation materials concentration of anaerobism is low, and water loss is big, utilization ratio of device is low, and the biogas residue and biogas liquid aftertreatment is with high costs.And anaerobic dry fermentation material concentration TS can reach more than 20%; It is solid-state that material is, when carrying out biogas fermentation production, because its material concentration height can reduce and heat power consumption; Material anaerobically fermenting aerobic fermentation in early stage also capable of using simultaneously heats up, and reduces the power consumption that heats under the low-temp anaerobic fermentation greatly.Anaerobic dry fermentation does not have natural pond liquid and produces, and fermentation residue is the fine solid organic fertilizer, and fertilizer efficiency is high, can realize zero disposal of pollutants basically.Therefore, along with the increase day by day of China's energy and environmental protection pressure, anaerobic dry fermentation has become the focus of present development research.
In recent years, carried out the research and development of a large amount of anaerobic dry fermentation technology both at home and abroad, wherein fermentation unit is the emphasis of research and development, and vertical tank type and garage type are two kinds of type of device that current anaerobic dry fermentation technology adopts usually.Vertical tank type structure generally adopts the continuous feeding and discharging operation, and technology is too complicated, and equipment price is expensive, and the running maintenance rate is high and complicated, applies difficulty.Garage type structure generally adopts intermittent type input and output material operation in batches, also can carry out continuous biogas fermentation production through several same garage type fermentation unit is set.From present whole research and development level and development prospect, garage type dry fermentation device will become the developing direction of the tool prospect in anaerobic dry fermentation field.But garage type dry fermentation device also exists construction cost high at present, the sealing difficulty, and the mass-and heat-transfer weak effect, acid accumulation is poisoned easily, and fermenting process is easy-regulating not, problems such as input and output material difficulty.
Based on above-mentioned situation, the application provides a kind of software garage type anaerobic dry fermentation device, and it is high that emphasis solves garage type anaerobic dry fermentation construction cost, sealing difficulty, mass-and heat-transfer weak effect, problems such as input and output material difficulty.
Summary of the invention
The utility model technical problem to be solved is: high to the existing garage existing construction cost of type anaerobic dry fermentation device, and the sealing difficulty, the mass-and heat-transfer weak effect, acid accumulation is poisoned easily, and fermenting process is easy-regulating not, problems such as input and output material difficulty.A kind of novel software garage type anaerobic dry fermentation device is provided; This plant construction is simple, cost is low and the sealing easy; Input and output material efficiently and easily; The measure that can also add through digestion percolate pump around circuit and bacterial classification solves mass-and heat-transfer weak effect, acid accumulation poisoning and fermenting process problem such as easy-regulating not easily.
The technical scheme of the utility model is achieved in that a kind of software garage type anaerobic dry fermentation apparatus main body is made up of software garage type fermentation system and percolate pump around circuit system.Software garage type fermentation system comprises garage type fermentation cabin, software sealing membrane, methane outlet, percolate spray header and leachate collection system; The software sealing membrane is installed in type fermentation cabin side, garage and end face open-mouth; Adopt inflatable flexible pipe-C type groove sealing between software sealing membrane and garage type fermentation cabin body of wall; Methane outlet is located at the top of software sealing membrane, and the percolate spray header is located at the top of garage type fermentation cabin, and leachate collection system is located at the bottom of garage formula fermentation cabin; The percolate circulation reflux device comprises leachate collection jar and the water pump that is provided with liquid pumping hole and fluid inlet and inoculation mouth; Fluid inlet is located at the bottom of leachate collection jar; Liquid pumping hole and inoculation mouth are located at the middle and lower part of leachate collection jar respectively, and water pump is contained between liquid pumping hole and the spray header.Spray header in the garage type fermentation cabin is connected with the water pump of percolate reflux through pipeline, and the filtrate collection system of garage type fermentation cabin is connected with the fluid inlet that is located at the leachate collection pot bottom.During the device operation, open a side software sealing membrane, carry out the batch charging, after the completion of waiting to feed, the sealing of inflatable flexible pipe, the charging stage accomplishes; Get into fermentation stage, open the percolate circulation reflux device, realize evenly inoculating, after fermentation is normal, regularly opens the percolate circulation reflux device and carry out the percolate spray cycle, reach the purpose that efficient mass transfer conducts heat and removes acid accumulation poisoning and regulation and control fermenting process.
In order to control the leavening temperature in the garage type fermentation cabin, in garage type fermentation cabin body of wall, heating tube and thermal insulation layer are housed, at the different positions of body of wall TP is housed.
In order to control the percolate temperature in the percolate circulation reflux device, at leachate collection jar inner bottom part heating system is housed, in the tank body middle and lower part TP is housed.
In order to guarantee production safety, the gaseous tension SV is housed respectively at software sealing membrane top and leachate collection tank top.
The positively effect of the utility model is, the design of the garage type fermentation cabin through three enclosure wall sides and opened top can realize conveniently input and output material.Inflatable flexible pipe-C type groove sealing is adopted in end face and side, can realize building simple, sealingly secure is reliable and effective explosion-proof purpose.Spray cycle through the percolate circulation reflux device; Can realize that efficient mass transfer conducts heat and the releasing acid accumulation is poisoned and the regulation and control fermenting process; It is fast to reach fermenting speed, the effect that methane gas producing efficient is high, and it is high and do not have an advantage such as waste liquid aftertreatment also to have simple and compact for structure, natural pond slag fertilizer efficiency simultaneously; Be a kind of device that can be widely used in biomass waste anaerobically fermenting production biogas, can satisfy the large-scale production requirement.
Description of drawings
Below in conjunction with accompanying drawing utility model is further specified.
Fig. 1 is the theory structure synoptic diagram of the utility model.
Fig. 2 is the stereographic map of the garage type fermentation cabin of the utility model.
1. garage type fermentation cabin among the figure, 2. heating tube, 3. spray header, 4. methane outlet, 5. software sealing membrane; 6. leachate collection groove, 7. TP, 8. leachate collection jar, 9. inoculation mouthful, 10. pneumatic outlet; 11. liquid pumping hole, 12. water pumps, 13. heating systems, 14. fluid inlets; 15. leakage fluid dram, 16. TPs, 17. gaseous tension SV, 18. gaseous tension SV.
Embodiment
In the accompanying drawings, open software sealing membrane (5), be charged to garage type fermentation cabin (1) in batches, after charging was accomplished, sealing software sealing membrane (5) got into fermentation stage; Open inoculation mouthful (9), in good quality strain inoculum to the leachate collection jar (8) of packing into, open liquid pumping hole (11), fluid inlet (14) is opened leachate collection groove (6) and water pump (12) and spray header (3), carries out circulation inoculation; After fermentation is normal, regularly open the percolate circulation reflux device, carry out the even spray cycle of percolate.
In order to control the leavening temperature in the garage type fermentation cabin, heating tube (2) is housed in the fermentation cabin body of wall, at the different positions of body of wall TP (7) is housed.
In order to control the percolate temperature in the percolate circulation reflux device, at leachate collection jar inner bottom part heating system (13) is housed, TP (16) is housed in the tank body middle and lower part.
In order to guarantee production safety, gaseous tension SV (17) and (18) are housed respectively in leachate collection tank top and software sealing membrane top.
Claims (4)
1. software garage type anaerobic dry fermentation device, it is characterized in that: main body is made up of software garage type fermentation system and percolate pump around circuit system; Software garage type fermentation system comprises garage type fermentation cabin (1), software sealing membrane (5), methane outlet (4), percolate spray header (3) and leachate collection groove (6); Software sealing membrane (5) is installed in type fermentation cabin (1) side, garage and end face open-mouth; Adopt inflatable flexible pipe-C type groove sealing between software sealing membrane (5) and garage type fermentation cabin (1) body of wall; Methane outlet (4) is located at the top of software sealing membrane (5); Percolate spray header (3) is located at the top of garage type fermentation cabin (1), and leachate collection groove (6) is located at the bottom of garage type fermentation cabin (1); Percolate pump around circuit system comprises leachate collection jar (8) and water pump (12); Leachate collection jar (8) is provided with liquid pumping hole (11) and fluid inlet (14) and inoculation mouthful (9); Fluid inlet (14) is located at the bottom of leachate collection jar (8); Liquid pumping hole (11) and inoculation mouthful (9) are located at the middle and lower part of leachate collection jar (8) respectively; Water pump (12) is contained between liquid pumping hole (11) and the spray header (3), and percolate spray header (3) is connected with the water pump (12) of percolate reflux through pipeline, and leachate collection groove (6) is connected with fluid inlet (14).
2. like claim 1 described software garage type anaerobic dry fermentation device, it is characterized in that: heating tube (2) and TP (7) are housed in garage type fermentation cabin (1) body of wall.
3. like claim 1 described software garage type anaerobic dry fermentation device, it is characterized in that: leachate collection jar (8) inner bottom part is equipped with heating system (13), and TP (16) is equipped with in the tank body middle and lower part.
4. like claim 1 described software garage type anaerobic dry fermentation device, it is characterized in that: gaseous tension SV (17) and (18) are housed respectively at leachate collection jar (8) top and software sealing membrane (5) top.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204885612U CN202322832U (en) | 2011-11-30 | 2011-11-30 | Soft garage type anaerobic dry fermentation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204885612U CN202322832U (en) | 2011-11-30 | 2011-11-30 | Soft garage type anaerobic dry fermentation device |
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| Publication Number | Publication Date |
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| CN202322832U true CN202322832U (en) | 2012-07-11 |
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| CN2011204885612U Expired - Fee Related CN202322832U (en) | 2011-11-30 | 2011-11-30 | Soft garage type anaerobic dry fermentation device |
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Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103667027A (en) * | 2013-11-20 | 2014-03-26 | 青岛天人环境股份有限公司 | Dry-wet combined anerobic fermentation reactor |
| CN103789200A (en) * | 2014-01-27 | 2014-05-14 | 北京金宇蓝天生态能源科技开发有限公司 | Dry type fermentation system |
| CN104328041A (en) * | 2014-11-21 | 2015-02-04 | 黑龙江省科学院科技孵化中心 | Dry-type anaerobic fermentation device capable of spraying straw with recycled biogas slurry |
| CN105349406A (en) * | 2015-11-10 | 2016-02-24 | 四川蒙特新能源科技有限公司 | Membrane fermentation system |
| CN105886385A (en) * | 2014-12-09 | 2016-08-24 | 北京建筑大学 | Municipal solid waste dry type anaerobic-aerobic combined treatment reactor and process |
| CN107099460A (en) * | 2017-05-03 | 2017-08-29 | 浙江大学 | Spray the enriching apparatus and its method of gas-lifting type anaerobic methane oxidation microorganism |
| CN107937253A (en) * | 2017-12-01 | 2018-04-20 | 农业部规划设计研究院 | It is a kind of to have the function of to strengthen the batch-type anaerobic dry fermentation method heated and its device |
| CN108642093A (en) * | 2018-06-27 | 2018-10-12 | 陈盛联 | The method that solid state fermentation kitchen garbage produces biogas |
| CN110004036A (en) * | 2019-04-30 | 2019-07-12 | 沈阳明晔能源科技股份有限公司 | A kind of continuous feeding and discharging organic solid castoff dry-type methane fermentation system |
| CN112500983A (en) * | 2020-06-28 | 2021-03-16 | 农业农村部规划设计研究院 | Cultivation combined type dry-wet coupling biogas production fermentation equipment |
-
2011
- 2011-11-30 CN CN2011204885612U patent/CN202322832U/en not_active Expired - Fee Related
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103667027A (en) * | 2013-11-20 | 2014-03-26 | 青岛天人环境股份有限公司 | Dry-wet combined anerobic fermentation reactor |
| CN103789200A (en) * | 2014-01-27 | 2014-05-14 | 北京金宇蓝天生态能源科技开发有限公司 | Dry type fermentation system |
| CN104328041A (en) * | 2014-11-21 | 2015-02-04 | 黑龙江省科学院科技孵化中心 | Dry-type anaerobic fermentation device capable of spraying straw with recycled biogas slurry |
| CN105886385B (en) * | 2014-12-09 | 2018-02-23 | 北京建筑大学 | A kind of domestic waste dry type anaerobic-aerobic combined treatment reactor and technique |
| CN105886385A (en) * | 2014-12-09 | 2016-08-24 | 北京建筑大学 | Municipal solid waste dry type anaerobic-aerobic combined treatment reactor and process |
| CN105349406A (en) * | 2015-11-10 | 2016-02-24 | 四川蒙特新能源科技有限公司 | Membrane fermentation system |
| CN107099460A (en) * | 2017-05-03 | 2017-08-29 | 浙江大学 | Spray the enriching apparatus and its method of gas-lifting type anaerobic methane oxidation microorganism |
| CN107099460B (en) * | 2017-05-03 | 2023-09-22 | 浙江大学 | Enrichment device and method for spraying airlift anaerobic methane oxidizing microorganisms |
| CN107937253A (en) * | 2017-12-01 | 2018-04-20 | 农业部规划设计研究院 | It is a kind of to have the function of to strengthen the batch-type anaerobic dry fermentation method heated and its device |
| CN107937253B (en) * | 2017-12-01 | 2021-03-23 | 农业部规划设计研究院 | Sequencing batch anaerobic dry fermentation method with enhanced temperature rise function and device thereof |
| CN108642093A (en) * | 2018-06-27 | 2018-10-12 | 陈盛联 | The method that solid state fermentation kitchen garbage produces biogas |
| CN110004036A (en) * | 2019-04-30 | 2019-07-12 | 沈阳明晔能源科技股份有限公司 | A kind of continuous feeding and discharging organic solid castoff dry-type methane fermentation system |
| CN112500983A (en) * | 2020-06-28 | 2021-03-16 | 农业农村部规划设计研究院 | Cultivation combined type dry-wet coupling biogas production fermentation equipment |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120711 Termination date: 20161130 |
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| CF01 | Termination of patent right due to non-payment of annual fee |