CN201245652Y - Water pressure type slag liquid automatic circulation methane tank - Google Patents
Water pressure type slag liquid automatic circulation methane tank Download PDFInfo
- Publication number
- CN201245652Y CN201245652Y CNU2008201313249U CN200820131324U CN201245652Y CN 201245652 Y CN201245652 Y CN 201245652Y CN U2008201313249 U CNU2008201313249 U CN U2008201313249U CN 200820131324 U CN200820131324 U CN 200820131324U CN 201245652 Y CN201245652 Y CN 201245652Y
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- tank
- fermentation
- hydraulic
- pipe
- fermentation tank
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 15
- 239000007788 liquid Substances 0.000 title claims abstract description 14
- 239000002893 slag Substances 0.000 title claims abstract description 11
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title abstract description 6
- 238000000855 fermentation Methods 0.000 claims abstract description 49
- 230000004151 fermentation Effects 0.000 claims abstract description 47
- 239000002002 slurry Substances 0.000 abstract description 11
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 239000000463 material Substances 0.000 abstract description 5
- 238000000354 decomposition reaction Methods 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 4
- 239000002994 raw material Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
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Classifications
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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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- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
本实用新型涉及一种水压式渣液自动循环沼气池。该沼气池包括进料口、进料管、发酵池、活动盖、导气管、水压池,在所述发酵池的底部连接有一个出料管,该出料管的上端与水压池相连,出料管上设有一个单向阀,在所述发酵池与水压池之间连接有一根回流管,该回流管上端位于发酵池内的上部气室,下端位于水压池的底部。本实用新型优点是:水压池的沼液与沼渣液通过回流管从发酵池上部气室流入发酵池,沼液如此进行多次的反复循环发酵,并参与浮水发酵料的再次发酵分解,使浮水发酵料发酵分解充分,而且又不结壳,既增加产气效果,又通过环流达到破壳的目的。
The utility model relates to a water pressure type slag liquid automatic circulation methane pool. The biogas digester includes a feed inlet, a feed pipe, a fermentation tank, a movable cover, an air guide pipe, and a hydraulic tank. A discharge pipe is connected to the bottom of the fermentation tank, and the upper end of the discharge pipe is connected to the hydraulic tank. , A one-way valve is provided on the discharge pipe, and a return pipe is connected between the fermentation tank and the hydraulic tank, the upper end of the return pipe is located in the upper air chamber in the fermentation tank, and the lower end is located at the bottom of the hydraulic tank. The utility model has the advantages that the biogas slurry and biogas residue liquid in the hydraulic tank flow into the fermentation tank from the upper air chamber of the fermentation tank through the return pipe, and the biogas slurry undergoes repeated cycle fermentation for many times in this way, and participates in the re-fermentation and decomposition of the floating water fermentation material. The fermentation and decomposition of the floating water fermentation material can be fully carried out without crusting, which not only increases the effect of gas production, but also achieves the purpose of breaking the shell through circulation.
Description
技术领域 technical field
本实用新型涉及一种可生产气体燃料的装置,更具体地说是一种水压式渣液自动循环沼气池。The utility model relates to a device capable of producing gas fuel, in particular to a water pressure type slag liquid automatic circulation methane pool.
技术背景technical background
目前,家用水压式沼气池主要是由进料口、进料管、发酵池、出料管、活动盖、导气管、水压池构成,进料管、出料管与发酵池相连通,分别位于发酵池两侧,出料管一端还连接位于发酵池一侧的水压池,导气管位于发酵池活动盖上。这种传统沼气池有如下缺点:一是沼液不流动,菌种分布不均,产气量低;二是原料在池内分布不均,发酵效果差,三是发酵池液面易结壳,影响正常产气;四是发酵池池底易沉集渣料,其长期堆集影响有效池容。At present, the household hydraulic biogas digester is mainly composed of a feed inlet, a feed pipe, a fermentation tank, a discharge pipe, a movable cover, an air guide pipe, and a hydraulic tank. The feed pipe and the discharge pipe are connected with the fermentation tank. They are respectively located on both sides of the fermentation tank, one end of the discharge pipe is also connected to the hydraulic tank on one side of the fermentation tank, and the air guide tube is located on the movable cover of the fermentation tank. This traditional biogas digester has the following disadvantages: first, the biogas slurry does not flow, the strains are unevenly distributed, and the gas production is low; second, the raw materials are unevenly distributed in the pond, and the fermentation effect is poor; Normal gas production; Fourth, slag is easy to settle at the bottom of the fermentation tank, and its long-term accumulation will affect the effective tank capacity.
实用新型内容Utility model content
本实用新型的目的在于克服上述现有技术的不足之处,而提供一种发酵效果好、出渣方便、产气率高而且可自动破除液面结壳的一种水压式渣液自动循环沼气池。The purpose of this utility model is to overcome the shortcomings of the above-mentioned prior art, and provide a kind of hydraulic type slag liquid automatic circulation with good fermentation effect, convenient slag discharge, high gas production rate and can automatically break the liquid surface encrustation Digester.
为完成上述目的,本实用新型所提供的技术解决方案是.一种水压式渣液自动循环沼气池,包括进料口、进料管、发酵池、活动盖、导气管、水压池,在所述发酵池的底部连接有一个出料管,该出料管的上端与水压池相连,出料管上设有一个单向阀,在所述发酵池与水压池之间连接有一根回流管,该回流管上端位于发酵池内的上部气室,下端位于水压池的底部。In order to accomplish the above-mentioned purpose, the technical solution provided by the utility model is. A hydraulic slag liquid automatic circulation biogas digester, including a feed inlet, a feed pipe, a fermentation tank, a movable cover, an air guide pipe, and a hydraulic tank, A discharge pipe is connected to the bottom of the fermentation tank, the upper end of the discharge pipe is connected to the hydraulic pool, a one-way valve is arranged on the discharge pipe, and a discharge pipe is connected between the fermentation tank and the hydraulic tank. A return pipe, the upper end of the return pipe is located in the upper air chamber in the fermentation tank, and the lower end is located in the bottom of the hydraulic tank.
还可以在所述水压池底部连接有一个水封池,在所述发酵池与水封池之间连接有一根回流管,该回流管上端位于发酵池内的上部气室,上端管口为斜面,下端位于水封池的底部。It is also possible to connect a water-sealed pool at the bottom of the hydraulic pool, and a return pipe is connected between the fermentation tank and the water-sealed pool. The upper end of the return pipe is located in the upper air chamber in the fermentation tank. The lower end is located at the bottom of the water-sealed pool.
为了确保气室的沼气不至于从回流管溢出,回流管在水压池或水封池一端端部所受到的水的压力要略大于气压室压力,因此水压池、出料口的上平面要高于活动盖的上平面。In order to ensure that the biogas in the air chamber does not overflow from the return pipe, the pressure of the water on the return pipe at one end of the hydraulic pool or water-sealed pool should be slightly greater than the pressure of the air chamber, so the upper plane of the hydraulic pool and the outlet should be higher than the upper plane of the movable cover.
本实用新型优点是:产气时,气室压力将池体中的的沼液与沼渣通过出料管压入水压池及水封池;用气时,气室压力降低,出料管上的单向阀自动封闭,水压池的沼液与沼渣液通过回流管从发酵池上部气室流入发酵池,发酵池内的沼液能多次反复的内、外,上、下地环流利用,沼液如此进行多次的反复循环发酵,并参与浮水发酵料的再次发酵分解,使浮水发酵料发酵分解充分,而且又不结壳,既增加产气效果,又通过环流达到破壳的目的。The utility model has the advantages that: when gas is produced, the pressure of the air chamber will press the biogas slurry and biogas residue in the pool body into the hydraulic pool and the water seal pool through the discharge pipe; The one-way valve on the top is automatically closed, and the biogas slurry and biogas residue in the hydraulic tank flow into the fermentation tank from the upper air chamber of the fermentation tank through the return pipe. The biogas slurry in the fermentation tank can be circulated repeatedly inside, outside, up and down for use , the biogas slurry is fermented repeatedly in this way, and participates in the re-fermentation and decomposition of the floating water fermentation material, so that the fermentation and decomposition of the floating water fermentation material is sufficient, and it does not crust, which not only increases the effect of gas production, but also achieves the purpose of breaking the shell through circulation .
附图说明 Description of drawings
附图为本实用新型一种实施例结构原理示意图。The accompanying drawing is a schematic diagram of the structural principle of an embodiment of the utility model.
具体实施方式 Detailed ways
如图1所示,本实用新型一种实施例,包括进料口1、进料管2、发酵池3、气室4、活动盖板11、导气管5。所述进料管2与发酵池3相连通,位于发酵池左侧。所述水压池6设于所述发酵池3的右侧,水压池6的下底连接有一水封池7,水封池7的下底面有一定的坡度。所述水压池6通过出料管8与发酵池3相连通。产气时,气室4的压力将池体中的的沼液与沼渣通过出料管8压入水压池6,从发酵池3底部进来的渣料大部分落入水封池7;出料管8的上部设有单向阀9,单向阀9阻止了水压池的料液从出料管8回流到发酵池3。在所述发酵间3与水封池7之间连接有一根回流管10,该回流管10上端位于发酵池3内的上部气室4,上端管口为斜面,下端位于水封池7的底部。用气时,沼气从导气管5排出,气室4压力降低,水压池6和水封池7的沼液与沼渣液通过回流管10从发酵池3上部气室4流入发酵池,如此循环,中层清淡沼液和底层浓稠含渣沼液可自动混合搅拌,原料和菌种分布均匀,由于有料液流入,液面的结壳被自动发酵瓦解。为了确保气室4的沼气不至于从回流管10溢出,回流管10在水封池7端部所受到的水的压力要略大于气室4的压力,因此水压池6、出料口1的上平面要高于活动盖11的上平面。As shown in FIG. 1 , an embodiment of the utility model includes a
Claims (3)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201313249U CN201245652Y (en) | 2008-07-28 | 2008-07-28 | Water pressure type slag liquid automatic circulation methane tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201313249U CN201245652Y (en) | 2008-07-28 | 2008-07-28 | Water pressure type slag liquid automatic circulation methane tank |
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| Publication Number | Publication Date |
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| CN201245652Y true CN201245652Y (en) | 2009-05-27 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008201313249U Expired - Fee Related CN201245652Y (en) | 2008-07-28 | 2008-07-28 | Water pressure type slag liquid automatic circulation methane tank |
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Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101985596A (en) * | 2010-10-28 | 2011-03-16 | 赖泽民 | Moving bed methane tank |
| CN103540527A (en) * | 2013-10-22 | 2014-01-29 | 蒋正贵 | Automatic deslagging and stirring methane tank |
| CN104498341A (en) * | 2015-01-22 | 2015-04-08 | 陆永柱 | Biogas production method for dragon type super-effective biogas fermentation system |
| CN104560661A (en) * | 2015-01-22 | 2015-04-29 | 张伟伟 | Method for producing methane by virtue of novel methane generating device with detachable feeding and discharging pipes |
| CN104560665A (en) * | 2015-01-22 | 2015-04-29 | 张伟伟 | Method for producing methane by employing binocular bundled methane generation system capable of realizing multi-area mixed flowing bacteria distribution |
| CN104560671A (en) * | 2015-01-22 | 2015-04-29 | 张伟伟 | Method of producing methane by virtue of straight tube type hydraulic type super-effective methane fermentation device |
| CN105255709A (en) * | 2015-10-30 | 2016-01-20 | 李宗明 | Marsh gas tank capable of automatically stirring fermented material residue and material liquid |
| CN106010943A (en) * | 2016-05-10 | 2016-10-12 | 罗显平 | Closed loop adit biogas digester |
| CN106929395A (en) * | 2015-12-29 | 2017-07-07 | 益阳市金灿农业科技开发有限公司 | A kind of water pressure type slag liquid automatic circulation methane tank |
| CN106995237A (en) * | 2017-06-01 | 2017-08-01 | 段国昌 | A kind of unpowered automatic stirring and the methane production device for being recycled feed liquid |
| CN107574114A (en) * | 2017-08-01 | 2018-01-12 | 河南科技大学 | A hydraulic type biogas digester with automatic feeding and discharging and its automatic feeding and discharging method |
-
2008
- 2008-07-28 CN CNU2008201313249U patent/CN201245652Y/en not_active Expired - Fee Related
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101985596A (en) * | 2010-10-28 | 2011-03-16 | 赖泽民 | Moving bed methane tank |
| CN103540527A (en) * | 2013-10-22 | 2014-01-29 | 蒋正贵 | Automatic deslagging and stirring methane tank |
| CN104498341A (en) * | 2015-01-22 | 2015-04-08 | 陆永柱 | Biogas production method for dragon type super-effective biogas fermentation system |
| CN104560661A (en) * | 2015-01-22 | 2015-04-29 | 张伟伟 | Method for producing methane by virtue of novel methane generating device with detachable feeding and discharging pipes |
| CN104560665A (en) * | 2015-01-22 | 2015-04-29 | 张伟伟 | Method for producing methane by employing binocular bundled methane generation system capable of realizing multi-area mixed flowing bacteria distribution |
| CN104560671A (en) * | 2015-01-22 | 2015-04-29 | 张伟伟 | Method of producing methane by virtue of straight tube type hydraulic type super-effective methane fermentation device |
| CN105255709A (en) * | 2015-10-30 | 2016-01-20 | 李宗明 | Marsh gas tank capable of automatically stirring fermented material residue and material liquid |
| CN106929395A (en) * | 2015-12-29 | 2017-07-07 | 益阳市金灿农业科技开发有限公司 | A kind of water pressure type slag liquid automatic circulation methane tank |
| CN106010943A (en) * | 2016-05-10 | 2016-10-12 | 罗显平 | Closed loop adit biogas digester |
| CN106995237A (en) * | 2017-06-01 | 2017-08-01 | 段国昌 | A kind of unpowered automatic stirring and the methane production device for being recycled feed liquid |
| CN107574114A (en) * | 2017-08-01 | 2018-01-12 | 河南科技大学 | A hydraulic type biogas digester with automatic feeding and discharging and its automatic feeding and discharging method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: YIYANG JINCAN AGRICULTURAL TECHNOLOGY DEVELOPMENT Free format text: FORMER OWNER: LONG WUHUA Effective date: 20120314 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 413043 YIYANG, HUNAN PROVINCE TO: 413001 YIYANG, HUNAN PROVINCE |
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| TR01 | Transfer of patent right |
Effective date of registration: 20120314 Address after: 413001 No. 219, Liang Liang Bei Road, Yiyang supply and marketing cooperative, Ziyang, Hunan Patentee after: Yiyang can agricultural science and Technology Development Co., Ltd. Address before: 413043 Yiyang City, Hunan province Ziyang District Zi Hu Kou Zhen Zou Jia Cun Patentee before: Long Wuhua |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20090527 Termination date: 20150728 |
|
| EXPY | Termination of patent right or utility model |
