CN201224729Y - Methane two-phase anaerobic fermentation gas stirring system - Google Patents
Methane two-phase anaerobic fermentation gas stirring system Download PDFInfo
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- CN201224729Y CN201224729Y CNU2008200898908U CN200820089890U CN201224729Y CN 201224729 Y CN201224729 Y CN 201224729Y CN U2008200898908 U CNU2008200898908 U CN U2008200898908U CN 200820089890 U CN200820089890 U CN 200820089890U CN 201224729 Y CN201224729 Y CN 201224729Y
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- 238000000855 fermentation Methods 0.000 title claims abstract description 22
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title description 16
- 238000003756 stirring Methods 0.000 title description 9
- 230000020477 pH reduction Effects 0.000 claims abstract description 40
- 238000004519 manufacturing process Methods 0.000 claims abstract description 32
- 230000003301 hydrolyzing effect Effects 0.000 claims abstract description 15
- 230000007062 hydrolysis Effects 0.000 claims description 24
- 238000006460 hydrolysis reaction Methods 0.000 claims description 24
- 239000007789 gas Substances 0.000 description 60
- 229910052739 hydrogen Inorganic materials 0.000 description 12
- 239000001257 hydrogen Substances 0.000 description 12
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 11
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 description 8
- 238000000034 method Methods 0.000 description 8
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 6
- 230000004151 fermentation Effects 0.000 description 6
- 230000008569 process Effects 0.000 description 6
- 235000019260 propionic acid Nutrition 0.000 description 4
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 description 4
- 239000000463 material Substances 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 2
- 238000013019 agitation Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 230000000696 methanogenic effect Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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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
- C12M23/36—Means for collection or storage of gas; Gas holders
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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
- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/58—Reaction vessels connected in series or in parallel
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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
- C12M29/24—Recirculation of gas
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- 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
Description
技术领域 technical field
本发明创造属于沼气发生设备,主要涉及一种生物能源沼气两相厌氧发酵的气体搅拌系统。The invention belongs to biogas generating equipment, and mainly relates to a gas stirring system for two-phase anaerobic fermentation of bioenergy biogas.
背景技术 Background technique
能源和环境问题已经成为当今社会两大突出问题,在不可再生能源日益减少和成本日益升高的情况下,人们开始最大限度的利用生物质资源补充能源的不足,并且可以在利用生物质资源的同时消除对环境的污染,而厌氧发酵则是一种能将农牧业等废弃物变为能源并进行无害化处理的技术。因此,为了提高厌氧发酵系统的效率和稳定性,人们研究了各种各样的方法和措施。目前,采用的厌氧发酵技术主要有单相厌氧发酵技术和两相厌氧发酵技术两种,而两相厌氧发酵技术与单相厌氧发酵技术相比具有发酵速度快和系统运行稳定等优点,但这种工艺也存在一些亟待解决的问题,如在现有的两相厌氧发酵系统中,由于采用了水解酸化罐、产气罐、集气罐之间简单的管路直连结构,即由同一根管路将水解酸化罐、产气罐、集气罐连通,在水解酸化罐内进行水解酸化过程要产生大量的氢气,而水解酸化罐内的产甲烷菌又非常少,产生的氢气降解量很少,使水解酸化罐内的氢分压逐渐升高,而氢分压的升高则直接导致丙酸发生积累,进而影响水解酸化罐的稳定性和后续产甲烷过程的顺利进行;此外,在发酵过程中,为了使发酵物料与菌种充分接触以及防止发酵物料顶部结壳,还必须定期的对水解酸化罐和产气罐的罐体内的物料进行搅拌,操作过程复杂。Energy and environmental issues have become two prominent issues in today's society. Under the circumstances of decreasing non-renewable energy sources and increasing costs, people began to maximize the use of biomass resources to supplement energy shortages, and they can use biomass resources At the same time, it eliminates pollution to the environment, and anaerobic fermentation is a technology that can turn agricultural and animal husbandry waste into energy and perform harmless treatment. Therefore, in order to improve the efficiency and stability of the anaerobic fermentation system, various methods and measures have been studied. At present, the anaerobic fermentation technology used mainly includes single-phase anaerobic fermentation technology and two-phase anaerobic fermentation technology. Compared with single-phase anaerobic fermentation technology, two-phase anaerobic fermentation technology has faster fermentation speed and stable system operation. and other advantages, but this process also has some problems to be solved urgently. For example, in the existing two-phase anaerobic fermentation system, due to the simple direct connection of pipelines between the hydrolysis acidification tank, the gas production tank and the gas collection tank structure, that is, the hydrolytic acidification tank, gas production tank, and gas collection tank are connected by the same pipeline. The hydrolytic acidification process in the hydrolytic acidification tank will generate a large amount of hydrogen, and the methanogenic bacteria in the hydrolysis acidification tank are very few. The generated hydrogen degradation is very small, which gradually increases the hydrogen partial pressure in the hydrolytic acidification tank, and the increase of hydrogen partial pressure directly leads to the accumulation of propionic acid, which in turn affects the stability of the hydrolytic acidification tank and the subsequent methane production process. In addition, during the fermentation process, in order to make the fermentation material fully contact with the bacteria and prevent the top of the fermentation material from crusting, it is necessary to regularly stir the materials in the hydrolysis acidification tank and the gas production tank, and the operation process is complicated. .
发明内容 Contents of the invention
本发明创造的目的就是针对上述已有技术存在的问题,设计提供一种新结构的沼气两相厌氧发酵气体搅拌系统,达到提高沼气产量、保证发酵过程稳定快速运行的目的。The purpose of the invention is to solve the problems existing in the above-mentioned prior art, and to design and provide a biogas two-phase anaerobic fermentation gas stirring system with a new structure, so as to increase the biogas output and ensure the stable and rapid operation of the fermentation process.
本发明创造的基本设计是,沼气两相厌氧发酵气体搅拌系统包括水解酸化罐、产气罐、集气罐及配连在水解酸化罐、产气罐、集气罐之间上的集气管,在水解酸化罐与产气罐之间配连安装回气管和进气管,其回气管两端分别与水解酸化罐上部和产气罐下部连接,进气管两端分别与水解酸化罐下部和产气罐上部连接,在进气管上配装气泵和单向阀,常开电磁阀安装在集气管上,位于水解酸化罐与产气罐之间的集气管部位处。The basic design of the present invention is that the biogas two-phase anaerobic fermentation gas mixing system includes a hydrolysis acidification tank, a gas production tank, a gas collection tank and a gas collection pipe connected between the hydrolysis acidification tank, the gas production tank and the gas collection tank , between the hydrolytic acidification tank and the gas production tank, a gas return pipe and an air intake pipe are installed in connection. The upper part of the gas tank is connected, an air pump and a one-way valve are installed on the intake pipe, and the normally open solenoid valve is installed on the gas collecting pipe, which is located at the gas collecting pipe between the hydrolysis acidification tank and the gas production tank.
本发明创造具有以下特点:①、在对水解酸化罐体进行气体搅拌的同时,对产气罐体也完成气体搅拌过程;②、用产气罐内甲烷含量较高的气体对水解酸化罐进行气体搅拌,这样甲烷含量较高的气体将水解酸化罐内氢气含量较高的气体置换出来,使水解酸化罐内的氢分压降低,因为丙酸只有在氢分压较低时才能向乙酸转化,所以氢分压降低增加了水解酸化罐内的乙酸含量,减少了丙酸含量,避免丙酸在水解酸化罐内发生积累,增加了水解酸化罐运行的稳定性,同时也有利于后续的产甲烷过程顺利进行;③、在用产气罐内的气体对水解酸化罐进行气体搅拌的同时,水解酸化罐内氢气含量较高的气体进入到产气罐内,对产气罐进行搅拌,因为氢气和二氧化碳相互作用也是产生甲烷的一个途径,所以进入产气罐内氢气含量较高的气体中的氢气也参与产甲烷过程,使甲烷的产生量升高;④、结构简单,操作简便,作业质量好,作业可靠,故障少。The present invention has the following characteristics: ①. While performing gas agitation on the hydrolysis acidification tank body, the gas agitation process is also completed on the gas production tank body; ②. Gas stirring, so that the gas with higher methane content will replace the gas with higher hydrogen content in the hydrolysis acidification tank, so that the hydrogen partial pressure in the hydrolysis acidification tank will be reduced, because propionic acid can only be converted to acetic acid when the hydrogen partial pressure is low , so the reduction of hydrogen partial pressure increases the content of acetic acid in the hydrolytic acidification tank, reduces the content of propionic acid, avoids the accumulation of propionic acid in the hydrolytic acidification tank, increases the stability of the operation of the hydrolysis acidification tank, and is also conducive to subsequent production The methane process goes smoothly; ③. While the gas in the gas production tank is used to stir the hydrolysis acidification tank, the gas with high hydrogen content in the hydrolysis acidification tank enters the gas production tank and stirs the gas production tank, because The interaction between hydrogen and carbon dioxide is also a way to produce methane, so the hydrogen in the gas with high hydrogen content in the gas production tank also participates in the process of producing methane, which increases the production of methane; ④, Simple structure, easy operation, easy operation Good quality, reliable operation, less faults.
附图说明 Description of drawings
附图是沼气两相厌氧发酵气体搅拌系统总体配装结构示意图;The accompanying drawing is a schematic diagram of the overall assembly structure of the biogas two-phase anaerobic fermentation gas mixing system;
图中件号说明:Description of part number in the figure:
1、水解酸化罐、2、常开电磁阀、3、集气管、4、回气管、5、产气罐、6、气泵、7、集气罐、8、单向阀、9、进气管。1. Hydrolysis and acidification tank, 2. Normally open solenoid valve, 3. Air collecting pipe, 4. Air return pipe, 5. Gas production tank, 6. Air pump, 7. Gas collecting tank, 8. One-way valve, 9. Intake pipe.
具体实施方式 Detailed ways
下面结合附图对本发明创造实施例进行详细描述。沼气两相厌氧发酵气体搅拌系统包括水解酸化罐1、产气罐5、集气罐7及配连在水解酸化罐1、产气罐5、集气罐7之间上的集气管3,在水解酸化罐1与产气罐5之间配连安装回气管4和进气管9,其回气管4两端分别与水解酸化罐1上部和产气罐5下部连接,进气管9两端分别与水解酸化罐1下部和产气罐5上部连接,在进气管9上配装气泵6和单向阀8,常开电磁阀2安装在集气管3上,位于水解酸化罐1与产气罐5之间的集气管3部位处。Embodiments of the present invention will be described in detail below in conjunction with the accompanying drawings. The biogas two-phase anaerobic fermentation gas mixing system includes a
发酵作业不进行气体搅拌时,水解酸化罐1内产生的气体通过常开电磁阀2进入到集气罐7内,产气罐5内的气体则直接通过顶部的集气管3进入到集气罐7内;当进行气体搅拌时,气泵6启动,将产气罐5内甲烷含量较高的气体从水解酸化罐1底部送入水解酸化罐1内,同时常开电磁阀2关闭,进而使水解酸化罐1内的气压升高,水解酸化罐1内的气体在气压的作用下从产气罐5底部返回产气罐5内,搅拌一段时间后,关掉气泵6,同时常开电磁阀2恢复到常开状态。When the fermentation operation does not carry out gas stirring, the gas generated in the
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101265447B (en) * | 2008-05-04 | 2011-04-27 | 东北农业大学 | Biogas two-phase anaerobic fermentation gas mixing system |
| CN102965278A (en) * | 2012-11-28 | 2013-03-13 | 华南理工大学 | Efficient two-phase anaerobic fermentation device |
| CN104450514A (en) * | 2014-11-18 | 2015-03-25 | 中国石油大学(北京) | Anaerobic vertical plug-flow reactor |
| CN108728336A (en) * | 2018-07-10 | 2018-11-02 | 中国农业大学 | A kind of superhigh temperature biological hydrolysis synchronizes the anaerobic fermentation processing system and method for deamination |
| TWI882326B (en) * | 2023-04-28 | 2025-05-01 | 財團法人紡織產業綜合研究所 | Artificial leather and manufacture method thereof |
-
2008
- 2008-05-04 CN CNU2008200898908U patent/CN201224729Y/en not_active Expired - Lifetime
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101265447B (en) * | 2008-05-04 | 2011-04-27 | 东北农业大学 | Biogas two-phase anaerobic fermentation gas mixing system |
| CN102965278A (en) * | 2012-11-28 | 2013-03-13 | 华南理工大学 | Efficient two-phase anaerobic fermentation device |
| CN102965278B (en) * | 2012-11-28 | 2014-05-07 | 华南理工大学 | A high-efficiency two-phase anaerobic fermentation device |
| CN104450514A (en) * | 2014-11-18 | 2015-03-25 | 中国石油大学(北京) | Anaerobic vertical plug-flow reactor |
| CN104450514B (en) * | 2014-11-18 | 2016-03-16 | 中国石油大学(北京) | The vertical plug-flow reactor of a kind of anaerobism |
| CN108728336A (en) * | 2018-07-10 | 2018-11-02 | 中国农业大学 | A kind of superhigh temperature biological hydrolysis synchronizes the anaerobic fermentation processing system and method for deamination |
| TWI882326B (en) * | 2023-04-28 | 2025-05-01 | 財團法人紡織產業綜合研究所 | Artificial leather and manufacture method thereof |
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