CN103865781B - Domestic refuse and farm crop straw organism dry fermentation treatment unit - Google Patents
Domestic refuse and farm crop straw organism dry fermentation treatment unit Download PDFInfo
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- 238000000855 fermentation Methods 0.000 title claims abstract description 87
- 230000004151 fermentation Effects 0.000 title claims abstract description 82
- 239000010902 straw Substances 0.000 title claims abstract description 32
- 238000003860 storage Methods 0.000 claims abstract description 28
- 239000010865 sewage Substances 0.000 claims abstract description 26
- 239000007921 spray Substances 0.000 claims abstract description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 19
- 238000010438 heat treatment Methods 0.000 claims abstract description 12
- 238000004519 manufacturing process Methods 0.000 claims abstract description 12
- 239000007788 liquid Substances 0.000 claims description 26
- 238000007789 sealing Methods 0.000 claims description 13
- 238000011084 recovery Methods 0.000 claims description 11
- 239000010791 domestic waste Substances 0.000 claims description 10
- 241001148471 unidentified anaerobic bacterium Species 0.000 claims description 9
- 238000002955 isolation Methods 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 8
- 239000011368 organic material Substances 0.000 claims description 2
- 238000004064 recycling Methods 0.000 claims description 2
- 238000003756 stirring Methods 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims 1
- 239000010813 municipal solid waste Substances 0.000 abstract description 20
- 239000002002 slurry Substances 0.000 abstract description 7
- 239000002994 raw material Substances 0.000 abstract description 6
- 238000005507 spraying Methods 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 17
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 9
- 239000003337 fertilizer Substances 0.000 description 7
- 229910001385 heavy metal Inorganic materials 0.000 description 6
- 241000894006 Bacteria Species 0.000 description 5
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 5
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 5
- 238000011081 inoculation Methods 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- 230000015556 catabolic process Effects 0.000 description 3
- 238000006731 degradation reaction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 241000255925 Diptera Species 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 239000003673 groundwater Substances 0.000 description 2
- 239000010815 organic waste Substances 0.000 description 2
- 238000000197 pyrolysis Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- 238000009264 composting Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 210000003608 fece Anatomy 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 239000010871 livestock manure Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000020477 pH reduction Effects 0.000 description 1
- 244000144977 poultry Species 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000012958 reprocessing Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 238000003900 soil pollution Methods 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
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- 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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- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/02—Form or structure of the vessel
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- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
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- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/06—Nozzles; Sprayers; Spargers; Diffusers
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- 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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- 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
一种生活垃圾与农作物秸秆生物干式厌氧发酵处理装置,包括发酵池,喷淋管,回流污水电泵,喷淋污水电泵,渗沥液贮罐,加热盘管;发酵池的一端设有锥形口门洞,另一端设有排空阀;若干个沼气收集管与沼气贮柜相连通;所述的发酵池是干式发酵池,发酵不用水,没有沼液排出;所述的发酵池建成拱形顶,便于收集沼气;干式发酵池建成模块式若干个循环使用,实现了垃圾与农作物秸秆处理和产气的连续性;干式发酵25-30天为一个周期,经过35-38℃中温发酵,在冬季与气温低的季节,采用热水盘管加热;在产气周期前排出酸化气,干式发酵所产沼气纯度比湿式所产沼气硫化氢含量低,沼气纯度高,CH4≥65%,H2S≤12ppm,每吨垃圾和秸秆混合原料产沼气120-150m3。
A bio-dry anaerobic fermentation treatment device for domestic garbage and crop straws, comprising a fermentation tank, a spray pipe, an electric pump for returning sewage, an electric pump for spraying sewage, a leachate storage tank, and a heating coil; one end of the fermentation tank is equipped with There is a tapered door opening, and the other end is equipped with an emptying valve; several biogas collection pipes are connected with the biogas storage cabinet; the fermentation tank is a dry fermentation tank, no water is used for fermentation, and no biogas slurry is discharged; The tank is built with a vaulted roof to facilitate the collection of biogas; the dry fermentation tank is built into a modular type for several cycles, which realizes the continuity of garbage and crop straw treatment and gas production; dry fermentation takes 25-30 days as a cycle, and after 35- Medium-temperature fermentation at 38°C. In winter and low-temperature seasons, hot water coils are used for heating; acidified gas is discharged before the gas production cycle. The purity of biogas produced by dry fermentation is lower than that of wet-type biogas, and the purity of biogas is high. CH4 ≥ 65%, H2S ≤ 12ppm, 120-150m3 biogas per ton of mixed raw materials of garbage and straw.
Description
技术领域 technical field
本发明涉及一种生活垃圾与农作物秸秆处理装置,尤其涉及一种垃圾与秸秆混合生物干式厌氧发酵产生沼气的资源化利用、无害化处理的装置。 The invention relates to a domestic garbage and crop straw treatment device, in particular to a device for resource utilization and harmless treatment of methane generated by mixed biological dry anaerobic fermentation of garbage and straw.
背景技术 Background technique
据报道截至2010年底全国城市生活垃圾年清运量2.12亿吨,乡村每年垃圾排放量3亿吨。畜禽粪便的排放量约为30亿吨,农作物秸秆年产生量约为7亿吨。城市的垃圾出现了围城现象,19.6%的焚烧发电,77%简单的填埋处理。农村的垃圾堆积如山,秸秆乱堆乱放、随意焚烧,没有得到有效的治理。 According to reports, as of the end of 2010, the annual removal and transportation of domestic waste in cities across the country was 212 million tons, and the annual waste discharge in rural areas was 300 million tons. The discharge of livestock and poultry manure is about 3 billion tons, and the annual production of crop straw is about 700 million tons. City garbage has been besieged, 19.6% of which is incinerated to generate electricity, and 77% is simply landfilled. The rubbish in the countryside is piled up like a mountain, and the straw is piled up randomly and burned at will, which has not been effectively treated.
目前城市生活垃圾77%填埋占用了80万亩的土地,污染填埋场周边的环境,引起居民的强烈不满,并严重的污染地下水,不但浪费了的大量的资源,并带来的长远的危害;19.6%的焚烧或焚烧发电,由于我国垃圾含水量高,焚烧温度低,达不到450℃易产生“二噁英”有害气体;且垃圾发电厂投资巨大,一般每百吨处理规模投资1亿元以上,严重制约了其发展。堆肥工艺具有简单、投资少、易操作的优点,但是现场蚊蝇滋生、臭气和甲烷气严重污染环境,有机物降解不彻底,肥料重金属含量高。水洗热解处理需要耗用大量的水和热能,产生大量的有害气体和污水,再处理量大成本高,不处理势必会产生二次污染。湿法厌氧发酵产生沼气,浓度一般TS≈5-10%处理1吨垃圾需要10~12吨水,发酵需要温度在35-38%℃,耗用大量的热能,用水量巨大,沼液消纳困难,制约了推广实施。 At present, 77% of urban domestic waste is landfilled and occupies 800,000 mu of land, polluting the environment around the landfill, causing strong dissatisfaction among residents, and seriously polluting groundwater, which not only wastes a lot of resources, but also brings long-term consequences. Hazards: 19.6% of incineration or incineration power generation, due to the high water content of garbage in our country, the incineration temperature is low, and it is easy to produce "dioxin" harmful gases if it does not reach 450 °C; and the investment in waste power plants is huge, generally per 100 tons of treatment scale investment More than 100 million yuan, seriously restricting its development. The composting process has the advantages of simplicity, low investment, and easy operation, but the breeding of mosquitoes and flies on site, odor and methane gas seriously pollute the environment, the degradation of organic matter is not complete, and the content of heavy metals in fertilizers is high. Washing and pyrolysis treatment requires a large amount of water and heat energy, and produces a large amount of harmful gas and sewage. The reprocessing volume is large and the cost is high. If it is not treated, it will inevitably cause secondary pollution. Wet anaerobic fermentation produces biogas, the concentration is generally TS ≈ 5-10%, 10-12 tons of water is required to treat 1 ton of garbage, and the fermentation requires a temperature of 35-38% ℃, which consumes a lot of heat energy and huge water consumption. Difficulties in accepting and restricting promotion and implementation.
综上所述,当前生活垃圾及农作物秸秆现有的处理尚未实现真正的无害化处理,资源化利用。一些处理技术仍局限于水洗、热解、高耗能、高耗水极易产生二次污染。 To sum up, the current treatment of domestic waste and crop straw has not yet achieved true harmless treatment and resource utilization. Some treatment technologies are still limited to water washing, pyrolysis, high energy consumption, high water consumption and easy to produce secondary pollution.
发明内容 Contents of the invention
本发明所解决的技术问题是克服现有技术的缺陷,提供一种能够避免垃圾填埋占用大量土地,严重污染地下水和土壤;避免垃圾与秸秆焚烧污染环境的生物处理装置。本发明所提供的装置不需要任何添加剂,投资运行费用低,沼气纯度高,没有沼液排放,避免二次污染。 The technical problem solved by the present invention is to overcome the defects of the prior art, and provide a biological treatment device that can avoid land occupation of a large amount of land by landfill, serious pollution of groundwater and soil, and environmental pollution by garbage and straw incineration. The device provided by the invention does not need any additives, has low investment and operation costs, high biogas purity, no biogas liquid discharge, and avoids secondary pollution.
为了实现上述目的,本发明是通过以下技术方案实现的: In order to achieve the above object, the present invention is achieved through the following technical solutions:
一种生活垃圾与农作物秸秆生物干式发酵处理装置,包括发酵池,锥形门洞,密封门,开关门装置,喷淋管,排空阀,隔离篦子,回流污水电泵,喷淋污水电泵,渗沥液贮罐,加热盘管;其特征在于:发酵池的一端设有锥形口洞,密封条贴在密封门的周边,密封门安装在开关门装置上,开关门装置通过门绞轴作为支点转动,若干个沼气收集管与沼气贮柜相连通;所述的发酵池是干式发酵池;所述的发酵池建成拱形顶,便于收集沼气;所述的开关门装置是液压开关门装置;发酵池的底部设有渗沥液回收管和加热盘管、隔离篦子;发酵池封闭的一端设有排空阀;渗沥液回收管通过回流连接管连接回流污水电泵的进液口,回流污水电泵的出液口通过渗沥液进罐管连接渗沥液贮罐的进液口,渗沥液贮罐的进液口在渗沥液贮罐的上部,渗沥液贮罐的下部开有出液口,渗沥液贮罐的出液口通过渗沥液出罐管连接喷淋污水电泵的进液口,喷淋污水电泵的出液口,通过出水连接管连接渗沥液管; A biological dry fermentation treatment device for domestic garbage and crop straw, including a fermentation tank, a tapered door opening, a sealed door, a door opening and closing device, a spray pipe, an emptying valve, an isolation grate, an electric pump for returning sewage, and an electric pump for spraying sewage , leachate storage tank, heating coil; it is characterized in that: one end of the fermentation tank is provided with a tapered hole, the sealing strip is attached to the periphery of the sealing door, the sealing door is installed on the opening and closing device, and the opening and closing device passes through the door hinge The shaft rotates as a fulcrum, and several biogas collection pipes are connected with the biogas storage cabinet; the fermentation tank is a dry fermentation tank; the fermentation tank is built with a vaulted roof to facilitate the collection of biogas; Opening and closing device; the bottom of the fermentation tank is equipped with leachate recovery pipe, heating coil, and isolation grate; the closed end of the fermentation tank is equipped with an emptying valve; the leachate recovery pipe is connected to the inlet of the return sewage electric pump through the return connection pipe Liquid port, the liquid outlet of the backflow sewage electric pump is connected to the liquid inlet of the leachate storage tank through the leachate tank inlet pipe. The liquid inlet of the leachate storage tank is on the upper part of the leachate storage tank. The lower part of the storage tank has a liquid outlet, and the liquid outlet of the leachate storage tank is connected to the liquid inlet of the spray sewage electric pump through the leachate outlet pipe, and the liquid outlet of the spray sewage electric pump is connected to the water outlet through the water outlet. The pipe is connected to the leachate pipe;
干式发酵25-30天为一个周期,经过35-38℃中温发酵,在冬季等气温低的季节,采用热水盘管加热,每吨垃圾和秸秆混合原料产沼气120-150m3,生活垃圾与农作物秸秆生物发酵时间长,降解彻底、发酵前分选出了磁性金属物质和电池类重金属,沼渣肥效高、重金属含量低; Dry fermentation takes 25-30 days as a cycle. After fermentation at 35-38°C at medium temperature, in winter and other seasons when the temperature is low, hot water coils are used to heat, and 120-150m3 of biogas is produced per ton of mixed raw materials of garbage and straw. The biofermentation time of crop straw is long, the degradation is complete, the magnetic metal substances and battery heavy metals are sorted out before fermentation, the biogas residue has high fertilizer efficiency and low heavy metal content;
干式发酵池建成模块式若干个循环使用,实现了垃圾与农作物秸秆处理和产气的连续性;在产气周期前排出酸化气,干式发酵所产沼气纯度比湿法所产沼气硫化氢含量低,沼气纯度高,CH4≥65%,H2S≤12ppm;干式发酵不用水,产生的沼液少,沼液用于生物厌氧菌群接种使用,没有沼液排出; The dry-type fermentation tank is built into a modular system for several cycles, realizing the continuity of waste and crop straw treatment and gas production; the acidified gas is discharged before the gas production cycle, and the purity of the biogas produced by dry fermentation is higher than that produced by the wet method. Hydrogen sulfide Low biogas content, high purity of biogas, CH4≥65%, H2S≤12ppm; dry fermentation does not use water, and produces less biogas slurry, biogas slurry is used for inoculation of biological anaerobic flora, and no biogas slurry is discharged;
发酵池建成模块化若干个循环使用不间断垃圾与秸秆处理和连续供沼气,适于规模化处理。 The fermentation tank is built into modularized several cycles for uninterrupted garbage and straw treatment and continuous biogas supply, which is suitable for large-scale treatment.
根据所述的生活垃圾与农作物秸秆生物干式发酵处理装置,其特征在于:所述的干式发酵池,干式发酵不用水,产生的沼液少,沼液用于生物厌氧菌群接种使用,没有沼液排出。 According to the biological dry-type fermentation treatment device for domestic waste and crop straw, it is characterized in that: the dry-type fermentation tank does not use water for dry-type fermentation, and produces less biogas slurry, which is used for inoculation of biological anaerobic flora use, no biogas slurry is discharged.
附图说明 Description of drawings
图1是本发明的生物厌氧干式发酵池主剖视图 Fig. 1 is the main sectional view of the biological anaerobic dry fermentation tank of the present invention
图2是本发明的生物厌氧干式发酵池四分之一剖视图 Fig. 2 is a quarter sectional view of the biological anaerobic dry fermentation tank of the present invention
图3是本发明生活垃圾与农作物秸秆干式生物发酵处理装置的总工艺流程图 Fig. 3 is the overall process flow diagram of the domestic waste and crop straw dry type biological fermentation treatment device of the present invention
附图中:1、发酵池2、锥形门洞3、密封条4、密封门5、门绞轴 In the accompanying drawings: 1, fermentation tank 2, tapered door opening 3, sealing strip 4, sealing door 5, door hinge shaft
6、开关门装置7、沼气收集管8、渗沥液管9、喷淋管10、排空阀 6. Door switch device 7, biogas collection pipe 8, leachate pipe 9, spray pipe 10, emptying valve
11、隔离篦子12、渗沥液回收管13、出水连接管14、回流连接管 11. Isolation grate 12. Leachate recovery pipe 13. Outlet connection pipe 14. Return connection pipe
15、回流污水电泵16、喷淋污水电泵17、渗沥液出罐管18、渗沥液进罐管 15. Return sewage electric pump 16. Spray sewage electric pump 17. Leachate outlet pipe 18. Leachate inlet pipe
19、渗沥液贮罐20、门压紧器21、加热盘管。 19. Leachate storage tank 20, door presser 21, heating coil.
具体实施方式 detailed description
下面结合附图和实施例对本发明做进一步说明: Below in conjunction with accompanying drawing and embodiment the present invention will be further described:
如图1、图2和图3所示,包括发酵池1,锥形门洞2,密封条3,密封门4,门绞轴5,开关门装置6,沼气收集管7,渗沥液管8,喷淋管9,排空阀10,隔离篦子11,渗沥液回收管12,出水连接管13,回流连接管14,回流污水电泵15,喷淋污水电泵16,渗沥液出罐管17,渗沥液进罐管18,渗沥液贮罐19,门压紧器20,加热盘管21。 As shown in Figure 1, Figure 2 and Figure 3, it includes a fermentation tank 1, a tapered door opening 2, a sealing strip 3, a sealing door 4, a door hinge shaft 5, a door opening and closing device 6, a biogas collection pipe 7, and a leachate pipe 8 , spray pipe 9, emptying valve 10, isolation grate 11, leachate recovery pipe 12, outlet connection pipe 13, return connection pipe 14, return sewage electric pump 15, spray sewage electric pump 16, leachate out of the tank Pipe 17, leachate inlet pipe 18, leachate storage tank 19, door presser 20, heating coil 21.
装配关系: Assembly relationship:
建设在地平面以上的混凝土长方形拱形顶式发酵池1,在发酵池1的一端设有锥形口洞2,密封条3贴在密封门4的周边,密封门4安装在开关门装置6上,开关门装置6与发酵池1通过门绞轴5作为支点相连接,安装在发酵池1上的门压紧器20将密封门4压紧。在发酵池1的顶部设置渗沥液管8,渗沥液管8与喷淋管9连接,并设置若干个沼气收集管7与沼气贮柜相连通。在发酵池1的底部设有渗沥液回收管12和加热盘管21、隔离篦子11,发酵池1封闭的一端设有开门时排空阀10。渗沥液回收管12通过回流连接管14连接回流污水电泵15的进液口,回流污水电泵15的出液口通过渗沥液进罐管18连接渗沥液贮罐19的进液口,渗沥液贮罐19的进液口在渗沥液贮罐19的上部,渗沥液贮罐19的下部开有出液口,渗沥液贮罐19的出液口通过渗沥液出罐管17连接喷淋污水电泵16的进液口,喷淋污水电泵16的出液口,通过出水连接管13连接渗沥液管8。 Concrete rectangular arch-top fermentation tank 1 built above the ground level, with a tapered opening 2 at one end of the fermentation tank 1, a sealing strip 3 attached to the periphery of the airtight door 4, and the airtight door 4 is installed on the opening and closing device 6 Above, the door opening and closing device 6 is connected with the fermentation tank 1 through the door hinge shaft 5 as a fulcrum, and the door presser 20 installed on the fermentation tank 1 compresses the airtight door 4 tightly. A leachate pipe 8 is arranged on the top of the fermentation tank 1, and the leachate pipe 8 is connected with a spray pipe 9, and several biogas collection pipes 7 are arranged to communicate with the biogas storage tank. A leachate recovery pipe 12, a heating coil 21, and an isolation grate 11 are provided at the bottom of the fermentation tank 1, and an emptying valve 10 is provided at the closed end of the fermentation tank 1 when the door is opened. The leachate recovery pipe 12 is connected to the liquid inlet of the backflow sewage electric pump 15 through the return connection pipe 14, and the liquid outlet of the backflow sewage electric pump 15 is connected to the liquid inlet of the leachate storage tank 19 through the leachate tank inlet pipe 18 The liquid inlet of the leachate storage tank 19 is on the top of the leachate storage tank 19, and the bottom of the leachate storage tank 19 has a liquid outlet, and the liquid outlet of the leachate storage tank 19 passes through the leachate outlet. The tank pipe 17 is connected to the liquid inlet of the spray sewage electric pump 16 , the liquid outlet of the spray sewage electric pump 16 , and is connected to the leachate pipe 8 through the water outlet connecting pipe 13 .
本发明的优点效果: Advantageous effect of the present invention:
本发明的生活垃圾与农作物秸秆生物干式发酵处理装置,所述的发酵池建成拱形顶,便于收集沼气;所述的开关门装置是液压开关门装置,所述的开关门装置带动密封门围绕门绞轴做相对旋转,实现密封门与锥形口洞的开与关,在关门状态时,密封条贴紧在锥形口洞的周边实现密封作用,在开门时排空阀打开,发酵池与大气相通,减小发酵池内的气压,排除发酵池内的气体;所述的发酵池是干式发酵池。 In the bio-dry fermentation treatment device for domestic garbage and crop straws of the present invention, the fermentation tank is built with a vaulted roof to facilitate the collection of biogas; the door opening and closing device is a hydraulic door opening and closing device, and the door opening and closing device drives the airtight door Make relative rotation around the door hinge shaft to realize the opening and closing of the airtight door and the conical opening. When the door is closed, the sealing strip is tightly attached to the periphery of the conical opening to realize the sealing effect. When the door is opened, the emptying valve is opened, and the fermentation The tank communicates with the atmosphere, reduces the air pressure in the fermentation tank, and removes the gas in the fermentation tank; the fermentation tank is a dry fermentation tank.
干式发酵池建成模块式若干个循环使用,实现了垃圾与农作物秸秆处理和产气的连续性。由于每个产气周期前的酸化气被排出,这也是干式发酵所产沼气纯度比湿法所产沼气硫化氢含量低的根本所在。 The dry-type fermentation tank is built into several modules for recycling, which realizes the continuity of garbage and crop straw treatment and gas production. Since the acidified gas before each gas production cycle is discharged, this is also the fundamental reason why the purity of biogas produced by dry fermentation is lower than that of biogas produced by wet method.
干式发酵不用水就没有沼液排放,无二次污染。 Dry fermentation does not use water, so there is no discharge of biogas slurry and no secondary pollution.
每吨垃圾与农作物秸秆产沼气120-150㎡,资源化利用率高、效益好。 Each ton of garbage and crop straw produces 120-150 m2 of biogas, with high resource utilization and good benefits.
因为干式发酵池间歇式使用提前排出酸化气,沼气纯度高,CH4≥65%,H2S≤12ppm。 Because the dry-type fermentation tank is used intermittently to discharge the acidified gas in advance, the purity of the biogas is high, CH4≥65%, H2S≤12ppm.
干式发酵25-30天为一个周期生活垃圾与农作物秸秆生物发酵时间长,降解彻底、发酵前分选出了磁性金属物质和电池类重金属,沼渣肥效高、重金属含量低。 Dry fermentation takes 25-30 days as a cycle. The biological fermentation time of domestic waste and crop straw is long, and the degradation is complete. Magnetic metal substances and battery heavy metals are sorted out before fermentation. The biogas residue has high fertilizer efficiency and low heavy metal content.
发酵池建成模块化若干个循环使用不间断垃圾与秸秆处理和连续供沼气,适于规模化处理。 The fermentation tank is built into modularized several cycles for uninterrupted garbage and straw treatment and continuous biogas supply, which is suitable for large-scale treatment.
生物干式厌氧发酵用沼渣和渗沥液接种生物菌不需要任何添加剂和水,占地少运行成本低。 Biological dry anaerobic fermentation uses biogas residue and leachate to inoculate biological bacteria without any additives and water, and occupies less land and has low operating costs.
适用于有机固体垃圾单独处理及与农作物秸秆混合处理,适应范围广。 It is suitable for separate treatment of organic solid waste and mixed treatment with crop straw, and has a wide range of applications.
本发明的设计原理如下: Design principle of the present invention is as follows:
初次使用没有含生物厌氧菌的沼渣和渗沥液接种时,应进行培菌驯化接种生物厌氧菌;产生的渗沥液通过干式发酵池底部的回收管网,由回流污水电泵,把所述的渗沥液回收到渗沥液贮罐与生物厌氧菌群接种循环使用;生活垃圾分选出来的有机物料与切碎的农作物秸秆各50%,再加入25-30%上批次出池含生物厌氧菌的沼渣,用铲车混合均匀起到接种生物厌氧菌的作用,并装入干式发酵池内容积的65-75%,关闭密封门;开启与渗沥液贮罐连接的喷淋系统,所述的喷淋系统包括出水连接管、喷淋污水电泵、渗沥液管、喷淋管;通过所述的喷淋系统喷入含有生物厌氧菌的渗沥液,起到调湿接种生物厌氧菌的作用,使原料保持65-75%的水份,由于垃圾及农作物秸秆入发酵池前均匀的混合了沼渣接种再喷淋含有生物厌氧菌的渗沥液,省去了发酵过程的搅拌工序,所述的回收管网包括隔离篦子、渗沥液回收管、回流连接管、回流污水电泵。原料发酵初的48-72小时为酸化阶段,打开沼气收集管网上的分路管阀门将酸化气送入紫外线除臭设备净化排放;72小时后产生沼气,然后关闭硫化氢排气阀门,打开通往沼气贮柜的阀门,沼气进贮气柜。原料在发酵池内发酵25-30天为一个处理周期,每吨有机垃圾与农作物秸秆产沼气120-150m3;干式发酵池建成模块式若干个循环使用,实现了垃圾与农作物秸秆处理和产气的连续性。由于每个产气周期前的酸化气被排出,这也是干式发酵所产沼气纯度比湿法所产沼气硫化氢含量低的根本所在。沼渣出池前打开排空阀通风排净残存的甲烷气,防止操作人员中毒,用铲车运出沼渣。由于干式发酵肥效全部保留在沼渣中,在入池前已分选出了磁性金属物和硬物质,因此沼渣是肥效极高的生物肥。生活有机垃圾及农作物秸秆通过沼渣混合接种生物厌氧菌以及在发酵池内喷淋渗沥液调湿接种厌氧菌,经过25-30天的35-38℃中温发酵,若用53-55℃高温发酵,发酵速度快、效率高,但在冬季等气温低的季节,供温成本高不划算,冬季采用布置在发酵池内的热水盘管加热,用沼气炉加热仅耗用自身产能的3-5%,采用分选出的可燃物供暖就不耗用自身的产能,每吨垃圾和秸秆混合原料产沼气120-150m3,CH4≥65%,H2S≤12ppm。沼渣为高效生物有机肥和电池类重金属物,实现了无害化处理、资源化利用。 When the biogas residue and leachate without bioanaerobic bacteria are used for inoculation for the first time, the bacteria should be cultivated and acclimated to inoculate the bioanaerobic bacteria; the leachate produced passes through the recovery pipe network at the bottom of the dry fermentation tank, and is returned by the sewage electric pump , recycle the leachate to the leachate storage tank and inoculate the biological anaerobic flora; 50% of the organic materials sorted out from domestic waste and 50% of the chopped crop straw, and then add 25-30% Batches of biogas residue containing biological anaerobic bacteria are mixed evenly with a forklift to inoculate biological anaerobic bacteria, and filled into 65-75% of the internal volume of the dry fermentation tank, and the sealed door is closed; opening and leaching A spray system connected to the liquid storage tank, the spray system includes a water outlet connection pipe, a spray sewage electric pump, a leachate pipe, and a spray pipe; The leachate plays the role of humidity control and inoculation of biological anaerobic bacteria, so that the raw material maintains a moisture content of 65-75%. Because the garbage and crop straw are mixed evenly before entering the fermentation tank, the biogas residue is inoculated and then sprayed with biological anaerobic bacteria. Bacteria leachate, eliminating the stirring process of the fermentation process, the recovery pipe network includes isolation grate, leachate recovery pipe, return connection pipe, return sewage electric pump. The first 48-72 hours of raw material fermentation is the acidification stage. Open the branch pipe valve on the biogas collection pipe network to send the acidified gas to the ultraviolet deodorization equipment for purification and discharge; after 72 hours to generate biogas, then close the hydrogen sulfide exhaust valve and open the channel. The valve to the biogas storage tank, the biogas enters the gas storage tank. The raw materials are fermented in the fermentation tank for 25-30 days as a treatment cycle, and each ton of organic waste and crop straw produces biogas of 120-150m3; the dry fermentation tank is built into a modular system for several cycles, realizing the combination of garbage and crop straw treatment and gas production continuity. Since the acidified gas before each gas production cycle is discharged, this is also the fundamental reason why the purity of biogas produced by dry fermentation is lower than that of biogas produced by wet method. Before the biogas residue is discharged from the pond, open the exhaust valve to ventilate and exhaust the remaining methane gas to prevent the operator from being poisoned, and use a forklift to transport the biogas residue. Because the fertilizer effect of dry fermentation is all retained in the biogas residue, and the magnetic metal objects and hard substances have been sorted out before entering the pond, so the biogas residue is a biological fertilizer with extremely high fertilizer efficiency. Domestic organic waste and crop straw are inoculated with biological anaerobic bacteria by mixing biogas residues and spraying leachate in the fermentation tank to adjust humidity and inoculate anaerobic bacteria. High-temperature fermentation has fast fermentation speed and high efficiency. However, in winter and other seasons when the temperature is low, the heating cost is high and it is not cost-effective. In winter, the hot water coil arranged in the fermentation tank is used for heating, and the biogas furnace only consumes 3% of its own production capacity. -5%, the use of sorted combustibles for heating does not consume its own production capacity, and the mixed raw materials of garbage and straw produce 120-150m3 of biogas per ton, CH4≥65%, H2S≤12ppm. Biogas residues are high-efficiency bio-organic fertilizers and battery-like heavy metals, which have achieved harmless treatment and resource utilization.
最后应说明的是:以上实施例仅用于说明本发明而并非限制本发明所描述的技术方案;因此,尽管本说明书参照上述的各个实施例对本发明已进行了详细的说明,但是,本领域的普通技术人员应当理解,仍然可以对本发明进行修改或等同替换;而一切不脱离本发明的精神和范围的技术方案及其改进,其均应涵盖在本发明的权利要求范围中。 Finally, it should be noted that: the above embodiments are only used to illustrate the present invention rather than limit the technical solutions described in the present invention; Those of ordinary skill in the art should understand that the present invention can still be modified or equivalently replaced; and all technical solutions and improvements that do not depart from the spirit and scope of the present invention should be covered by the claims of the present invention.
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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 |
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CN106439829B (en) * | 2016-11-11 | 2019-08-27 | 中冶焦耐(大连)工程技术有限公司 | A system and method for thawing waste in winter in a domestic waste incineration power plant |
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