CN201634676U - A trough fermentation digester - Google Patents
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- CN201634676U CN201634676U CN2010201652705U CN201020165270U CN201634676U CN 201634676 U CN201634676 U CN 201634676U CN 2010201652705 U CN2010201652705 U CN 2010201652705U CN 201020165270 U CN201020165270 U CN 201020165270U CN 201634676 U CN201634676 U CN 201634676U
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- 238000000855 fermentation Methods 0.000 title claims abstract description 69
- 230000004151 fermentation Effects 0.000 title claims abstract description 68
- 239000002893 slag Substances 0.000 claims abstract description 24
- 238000003756 stirring Methods 0.000 claims abstract description 17
- 239000013049 sediment Substances 0.000 claims abstract description 12
- 239000010865 sewage Substances 0.000 claims abstract description 11
- 230000020477 pH reduction Effects 0.000 claims abstract description 9
- 238000002347 injection Methods 0.000 claims abstract description 6
- 239000007924 injection Substances 0.000 claims abstract description 6
- 239000002002 slurry Substances 0.000 claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims 1
- 239000002994 raw material Substances 0.000 abstract description 13
- 239000007788 liquid Substances 0.000 abstract description 9
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 239000010902 straw Substances 0.000 description 12
- 230000000694 effects Effects 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 239000010871 livestock manure Substances 0.000 description 4
- 238000007599 discharging Methods 0.000 description 3
- 238000011081 inoculation Methods 0.000 description 3
- 210000003608 fece Anatomy 0.000 description 2
- 244000144972 livestock Species 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 241000283690 Bos taurus Species 0.000 description 1
- 241000282887 Suidae Species 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 244000144977 poultry Species 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
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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
- 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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- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
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- C12M23/00—Constructional details, e.g. recesses, hinges
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- C12M27/00—Means for mixing, agitating or circulating fluids in the vessel
- C12M27/02—Stirrer or mobile mixing elements
- C12M27/06—Stirrer or mobile mixing elements with horizontal or inclined stirrer shaft or axis
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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
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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
本实用新型公开了一种槽式发酵沼气池,该沼气池包括污水入口(1)、酸化沉渣池(2)、污水通道(3)、进料池(5)、沼气池主体(7)、发酵池(8)、池罩(11)及出气口(12),进料池(5)与发酵池(8)之间安装有进料管(6),发酵池(8)内安装有搅拌管(14),搅拌管(14)上开有数个喷射孔,沼气池主体(7)的上部安装有活动栅网(10),沼气池主体(7)的外侧设有水压池(18)和排渣池(15),水压池(18)的上部设有溢流口(19),下部设有与发酵池(8)相连通的溢水管(17),排渣池(15)与发酵池(8)之间设有自动排渣管(16)。本实用新型能有效防止浮渣结壳,并可限压和限制最低液面,产气率比普通槽式池提高15%-25%,适应多种原料发酵,出渣方便。
The utility model discloses a trough-type fermentation biogas pond, which comprises a sewage inlet (1), an acidification sediment pond (2), a sewage channel (3), a feed pond (5), a biogas pond main body (7), The fermentation tank (8), the tank cover (11) and the air outlet (12), the feed pipe (6) is installed between the feed tank (5) and the fermentation tank (8), and the stirring tank (8) is installed Pipe (14), agitating pipe (14) has several injection holes, the upper part of the biogas tank main body (7) is equipped with a movable grid (10), and the outside of the biogas tank main body (7) is provided with a hydraulic pool (18) And slag discharge tank (15), the top of hydraulic tank (18) is provided with overflow port (19), and the bottom is provided with the overflow pipe (17) that links to each other with fermenting tank (8), and slag discharge tank (15) and An automatic slag discharge pipe (16) is arranged between the fermentation tanks (8). The utility model can effectively prevent scum from encrusting, and can limit the pressure and the minimum liquid level, and the gas production rate is 15%-25% higher than that of the common trough tank, and is suitable for the fermentation of various raw materials, and the slag is convenient to discharge.
Description
技术领域technical field
本实用新型涉及一种沼气池,特别是一种槽式发酵沼气池。The utility model relates to a biogas pool, in particular to a trough-type fermentation biogas pool.
背景技术Background technique
目前我国由过去一家一户家庭养殖逐步向集约化、规模化方向转变,不少农户不再养猪养牛,造成一些沼气农户的沼气原料不足,原料多样化,混合原料发酵的特点,要求沼气池能够适应多种发酵工艺和多种发酵原料的需要,提高混合发酵连续或批次发酵工艺的产气率。而传统的沼气池都存在畜禽废弃物与秸秆混合发酵后大秸秆原料上浮、传质接种效果差的缺陷。At present, our country has gradually changed from the past one family breeding to intensive and large-scale direction. Many farmers no longer raise pigs and cattle, resulting in the shortage of biogas raw materials for some biogas farmers. The raw materials are diversified and the characteristics of mixed raw material fermentation require biogas. The pool can adapt to the needs of various fermentation processes and various fermentation raw materials, and improve the gas production rate of mixed fermentation continuous or batch fermentation processes. However, traditional biogas digesters have the defects of large straw raw materials floating up after mixed fermentation of livestock waste and straw, and poor mass transfer inoculation effect.
实用新型内容Utility model content
本实用新型所要解决的技术问题是提供一种能有效防止浮渣结壳、提高混合发酵传质接种效果的槽式发酵沼气池。The technical problem to be solved by the utility model is to provide a trough-type fermentation biogas digester which can effectively prevent scum from encrusting and improve the effect of mixed fermentation mass transfer and inoculation.
本实用新型以如下技术方案解决上述技术问题:本实用新型槽式发酵沼气池包括污水入口1、酸化沉渣池2、污水通道3、进料池5、沼气池主体7、发酵池8、池罩11及出气口12,进料池5与发酵池8之间安装有进料管6,发酵池8内安装有搅拌管14,搅拌管14上开有数个喷射孔,沼气池主体7的上部安装有活动栅网10,沼气池主体7的外侧设有水压池18和排渣池15,水压池18的上部设有溢流口19,下部设有与发酵池8相连通的溢水管17,排渣池15与发酵池8之间设有自动排渣管16。The utility model solves the above-mentioned technical problems with the following technical solutions: the utility model trough-type fermentation biogas digester includes a sewage inlet 1, an acidification sediment pond 2, a sewage channel 3, a
所述进料管6在发酵池8内的出口位置低于活动栅网10。The outlet position of the feed pipe 6 in the
所述自动排渣管16与进料管6呈相对排布。The automatic
所述活动栅网10和池罩11与沼气池主体7之间均为活动连接。The
所述搅拌管14至少设有两排并连接加压泵,搅拌管14上的喷射孔呈品字形排布,加压泵的进口接水压池18的沼液或外接沼气。The
所述发酵池8的池底设有斜坡9,自动排渣管16的入口设在池内最低位置。The bottom of the
本实用新型槽式沼气池能够达到连续进料发酵工艺和批次进料发酵工艺要求,并具有进出料方便、发酵效果好及有效预防浮渣结壳的优点,解决了农村沼气池出料难问题、结壳问题,解决畜禽废弃物与秸秆混合发酵传质接种效果差的问题。The utility model trough-type biogas digester can meet the requirements of continuous feed fermentation process and batch feed fermentation process, and has the advantages of convenient feeding and discharging, good fermentation effect and effective prevention of scum encrustation, and solves the difficulty of discharging materials in rural methane digesters. problems, crusting problems, and solve the problem of poor mass transfer inoculation effect of mixed fermentation of livestock and poultry waste and straw.
本实用新型槽式沼气池与现有长方开固定式沼气池相比具备以下优点:Compared with the existing rectangular open fixed biogas digester, the utility model has the following advantages:
(1)方便实现连续或批次厌氧发酵,出渣方便;(1) It is convenient to realize continuous or batch anaerobic fermentation, and it is convenient to discharge slag;
(2)具有强制搅拌功能,能有效防止浮渣结壳;(2) It has the function of forced stirring, which can effectively prevent scum and crust;
(3)混合发酵时,可将秸秆全部浸在沼液内,提高传质效果,产气率比现有的普通槽式沼气池提高15%-25%。(3) During mixed fermentation, all the straw can be immersed in the biogas slurry to improve the mass transfer effect, and the gas production rate is 15%-25% higher than that of the existing common trough biogas digester.
附图说明Description of drawings
图1是本实用新型槽式发酵沼气池的结构示意图。图中没有示出池罩及活动栅网。Fig. 1 is a structural schematic diagram of a trough-type fermentation biogas digester of the present invention. The pool cover and movable grid are not shown in the figure.
图2是图1的A-A剖视示意图。图中示出了池罩及活动栅网。FIG. 2 is a schematic cross-sectional view along line A-A of FIG. 1 . The figure shows the pool cover and movable grid.
图3是图1的B-B剖视示意图。Fig. 3 is a schematic cross-sectional view along B-B of Fig. 1 .
图中:污水入口1,酸化沉渣池2,污水通道3,格栅4,进料池5,进料管6,沼气池主体7,发酵池8,斜坡9,活动栅网10,池罩11,出气口12,固定柱13,搅拌管14,排渣池15,自动排渣管16,溢水管17,水压池18,溢流口19。In the figure: sewage inlet 1, acidification sediment tank 2, sewage channel 3, grid 4,
具体实施方式Detailed ways
下面结合附图对本实用新型槽式沼气池作进一步描述:Below in conjunction with accompanying drawing, the utility model trough type biogas digester is further described:
在长方形的沼气池主体7的一侧设有相连通的酸化沉渣池2和进料池5,酸化沉渣池2一侧设有污水入口1,另一侧与进料池5相连的污水通道3上设有格栅4,进料池5的底部连接进料管6,进料管6伸入位于沼气池主体7内部的发酵池8下部,发酵池8内有三排固定柱13,每排固定柱上安装有相连通的搅拌管14,搅拌管14上开有数个呈品字形排布的喷射孔,沼气池主体7的上部安装有可拆装的活动栅网10和池罩11,池罩11上开有与用户炉具进气管相接的出气口12;沼气池主体7的另一侧设有排渣池15和两个相通的水压池18,水压池18的上部设有溢流口19,下部设有与发酵池8相连通的溢水管17,排渣池15与发酵池8之间设有自动排渣管16,自动排渣管16与进料管6呈相对排布;进料管6在发酵池8内的出口位置低于活动栅网10;发酵池8的池底设有斜坡9,自动排渣管16的入口设在池内最低位置;酸化沉渣池2的污水入口1高于水压池18上部的溢流口19。On one side of the rectangular biogas digester
所述沼气池主体7的高度以发酵池内产生的最大压力值为限,一般取40厘米-60厘米。The height of the biogas digester
所述池底的斜坡9从进料管6向自动排渣管16方向放坡,以沼渣能自由流动为宜。The
所述溢水管17伸入发酵池内后沿池壁向下伸,其深度超过活动栅网10深度的20-50厘米。Described
本实用新型槽式沼气池的工作过程如下:The working process of the utility model trough type biogas tank is as follows:
连续进料工艺的工作过程是:畜粪水流经酸化沉渣池2沉渣处理后,经过格栅4进入进料池5,再从进料管6流入发酵池8。秸秆等其它原料则经切碎堆沤处理后,从进料池5直接加入,经进料管6进入发酵池8。粪液与其它秸秆原料混合在密闭的发酵池8内发酵产生沼气,从出气口12排出。The working process of the continuous feeding process is: the livestock manure flows through the acidification sediment tank 2 and after the sediment is treated, it enters the
批次进料工艺的工作过程是:畜粪水流经酸化沉渣池2沉渣处理后,经过格栅4进入进料池5,再从进料管6流入发酵池8;秸秆等其它原料则经切碎堆沤处理后,打开活动栅网10和池罩11后,直接从池体上部进料,然后扣好活动栅网10和池罩11。粪液与其它秸秆原料混合在密闭的发酵池8内发酵产生沼气,从出气口12排出。The working process of the batch feeding process is: the livestock manure flows through the acidification sediment tank 2, after the sediment is treated, it enters the
由于原料在发酵池8内发酵产气,气压增加,发酵池8内的沼液通过溢水管17压入水压池18,发酵池8的液面下降,水压池18的液面上升,当超过溢流口19时,沼液便从溢流口19溢出;池外用气,发酵池8内的气压减小,在水压池18的作用下,发酵池8的液面回升,使发酵池8的沼液容量和气压始终保持在一定范围内。由于活动栅网10的隔离作用,浮渣和秸秆始终在液面以下,结壳层无法生成,同时提高了秸秆发酵效果。Because the raw material is fermented in the
新鲜原料边发酵边沿池底的斜坡9往自动排渣管16的管口方向运动,秸秆经过发酵溶解腐烂后沉降,最后堆积于发酵池的最低部位,在池内压力作用下,从自动排渣管16排出到排渣池15。当池内需要搅拌时,将搅拌管14连接加压泵,加压泵从水压池18抽沼液或外接沼气,并从搅拌管14上的喷射孔射出沼液或沼气,从而搅拌池内的沼液,使厌氧微生物与发酵原料充分接触,提高产气率,并且破坏和防止液面结壳。Fresh raw materials move towards the mouth of the automatic
当经过一段时间运行后,发酵池内沉淀物增多,秸秆发酵达一定周期,必须进行大出料时,或者批次进料发酵出料时,打开池罩11和活动栅网10后,操作人员便可很方便地进入池内进行出料操作。After a period of operation, the sediment in the fermentation tank increases, and the straw fermentation reaches a certain period. When it is necessary to carry out large-scale discharge, or when batch feeding and fermentation discharge, after opening the
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Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102174377A (en) * | 2010-12-16 | 2011-09-07 | 刘明江 | Stirring device for top floating crust breaking and bottom strong-current turning of anaerobic fermentation liquid |
CN102911857A (en) * | 2011-08-05 | 2013-02-06 | 李启仁 | Device for automatically skimming sewage to generate methane for increasing value |
CN102965279A (en) * | 2012-12-17 | 2013-03-13 | 湘潭市科达丽实业有限公司 | Four-module assembled methane tank |
CN104357318A (en) * | 2014-11-16 | 2015-02-18 | 农业部沼气科学研究所 | Integrated sedimentation/fermentation biogas device |
CN105273990A (en) * | 2015-12-01 | 2016-01-27 | 广西壮族自治区林业科学研究院 | Biogas tank for treating rural organic refuses |
CN105567561A (en) * | 2016-01-15 | 2016-05-11 | 曹秀保 | Underground-type two-stage anaerobic large-medium biogas digester achieving automatic high temperature fermentation |
CN106085826A (en) * | 2016-06-29 | 2016-11-09 | 东北师范大学 | A kind of methane-generating pit surges and stirs the Multifunctional treatment device combined with pump drainage |
CN106190790A (en) * | 2015-07-30 | 2016-12-07 | 毕仁贤 | Send out well methane-generating pit |
CN112574861A (en) * | 2020-12-28 | 2021-03-30 | 中国农业科学院农业环境与可持续发展研究所 | Anaerobic digestion system capable of automatically discharging slag and control method |
CN114015556A (en) * | 2021-11-24 | 2022-02-08 | 江苏新源能环科技有限公司 | Rural solid-state organic waste dry fermentation device of agricultural |
CN116731820A (en) * | 2023-06-08 | 2023-09-12 | 中国铁工投资建设集团有限公司 | Organic solid waste loop-ring two-phase anaerobic fermentation system and fermentation device |
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2010
- 2010-04-21 CN CN2010201652705U patent/CN201634676U/en not_active Expired - Fee Related
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102174377A (en) * | 2010-12-16 | 2011-09-07 | 刘明江 | Stirring device for top floating crust breaking and bottom strong-current turning of anaerobic fermentation liquid |
CN102911857A (en) * | 2011-08-05 | 2013-02-06 | 李启仁 | Device for automatically skimming sewage to generate methane for increasing value |
CN102965279A (en) * | 2012-12-17 | 2013-03-13 | 湘潭市科达丽实业有限公司 | Four-module assembled methane tank |
CN104357318A (en) * | 2014-11-16 | 2015-02-18 | 农业部沼气科学研究所 | Integrated sedimentation/fermentation biogas device |
CN106190790A (en) * | 2015-07-30 | 2016-12-07 | 毕仁贤 | Send out well methane-generating pit |
CN105273990A (en) * | 2015-12-01 | 2016-01-27 | 广西壮族自治区林业科学研究院 | Biogas tank for treating rural organic refuses |
CN105567561B (en) * | 2016-01-15 | 2018-05-22 | 曹秀保 | A kind of large and medium-sized methane-generating pit of automatic hot fermentation of underground type two-stage anaerobic |
CN105567561A (en) * | 2016-01-15 | 2016-05-11 | 曹秀保 | Underground-type two-stage anaerobic large-medium biogas digester achieving automatic high temperature fermentation |
CN106085826A (en) * | 2016-06-29 | 2016-11-09 | 东北师范大学 | A kind of methane-generating pit surges and stirs the Multifunctional treatment device combined with pump drainage |
CN106085826B (en) * | 2016-06-29 | 2018-03-16 | 东北师范大学 | A kind of methane-generating pit surges the Multifunctional treatment device that is combined with pump drainage of stirring |
CN112574861A (en) * | 2020-12-28 | 2021-03-30 | 中国农业科学院农业环境与可持续发展研究所 | Anaerobic digestion system capable of automatically discharging slag and control method |
CN114015556A (en) * | 2021-11-24 | 2022-02-08 | 江苏新源能环科技有限公司 | Rural solid-state organic waste dry fermentation device of agricultural |
CN114015556B (en) * | 2021-11-24 | 2024-04-30 | 江苏新源能环科技有限公司 | Agricultural rural solid organic waste dry fermentation device |
CN116731820A (en) * | 2023-06-08 | 2023-09-12 | 中国铁工投资建设集团有限公司 | Organic solid waste loop-ring two-phase anaerobic fermentation system and fermentation device |
CN116731820B (en) * | 2023-06-08 | 2024-02-09 | 中国铁工投资建设集团有限公司 | Organic solid waste loop-ring two-phase anaerobic fermentation system and fermentation device |
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