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CN201080460Y - Vertical operation dry-type anaerobic digestion device - Google Patents

Vertical operation dry-type anaerobic digestion device Download PDF

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Publication number
CN201080460Y
CN201080460Y CNU2007200265328U CN200720026532U CN201080460Y CN 201080460 Y CN201080460 Y CN 201080460Y CN U2007200265328 U CNU2007200265328 U CN U2007200265328U CN 200720026532 U CN200720026532 U CN 200720026532U CN 201080460 Y CN201080460 Y CN 201080460Y
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China
Prior art keywords
anaerobic digestion
communicated
tank
digestion tank
valve
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Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CNU2007200265328U
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Chinese (zh)
Inventor
曹曼
刘林
陈萍
郭冰瑜
王传水
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Qingdao Tianren Environment Co., Ltd.
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QINGDAO TIANREN ENVIRONMENT ENGINEERING Co Ltd
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Priority to CNU2007200265328U priority Critical patent/CN201080460Y/en
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Publication of CN201080460Y publication Critical patent/CN201080460Y/en
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/40Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse

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Abstract

Disclosed is a dry anaerobic digestion device which is vertically moved. The anaerobic digestion device comprises a tank body of a vertical anaerobic digestion tank; the top of the anaerobic digestion tank is provided with a biogas outlet, a relief valve connection and an inspection manhole and the bottom is a taper bucket. The anaerobic digestion device is characterized in that the lower opening of the taper bucket is communicated with the inlet of a control valve, while the outlet of the control valve is communicated with the upper opening of a feeding recycle pump through a pipeline; the upper opening of the feeding recycle pump is communicated with the lower opening of a feed hopper through a valve; the lower opening of the feeding recycle pump is communicated with the inlets of 2-10 vertical feeding pipes in the anaerobic digestion tank through the pipeline and the valve; the outlet of each feeding pipe is arranged close to the top of the tank body of the anaerobic digestion tank; the bottom of the tank body of the anaerobic digestion tank is provided with a steadier. When the utility model is used to treat materials, the solid content ratio can reach 15 to 40 percent. The utility model has the advantages of simple structure, free maintenance, and simple and convenient operation management; has no internal stirrer and moving parts; the volume biogas production can reach 5 to 20 square meters per cubic meter; and the utility model produces no liquid waste, no solid disposition and is sealed without releasing waste gas.

Description

一种垂直运行的干式厌氧消化装置 A dry anaerobic digestion unit running vertically

技术领域 technical field

本实用新型涉及一种有机废物厌氧消化的装置,特别是涉及一种垂直运行的有机废物干式厌氧消化的装置。The utility model relates to a device for anaerobic digestion of organic waste, in particular to a device for vertically running dry anaerobic digestion of organic waste.

背景技术 Background technique

有机物废物包括农产品加工废物、畜禽粪便、城市生活垃圾、城市污泥等,这些废物含有大量有机成分,是很好的厌氧发酵原料,可转化为沼气作为再生能源利用,并且产生的沼渣是很好的有机肥料。目前采用的厌氧消化装置大多是含固率在4-10%的湿式发酵,其特点是由于处理有机物废物时用水量高,通常需要容积较大的反应器,占地大,也需要消耗更多的能量,此外发酵后产生的大量沼液还需要处理。湿式发酵装置投资大、占地多、能耗高、单位容积产气率低。Organic waste includes agricultural product processing waste, livestock and poultry manure, municipal solid waste, urban sludge, etc. These wastes contain a large amount of organic components and are good raw materials for anaerobic fermentation, which can be converted into biogas for use as renewable energy, and the produced biogas residue It is a good organic fertilizer. Most of the anaerobic digestion devices currently used are wet fermentation with a solid content of 4-10%, which is characterized by high water consumption when treating organic waste, usually requiring a larger reactor, occupying a large area, and requiring more consumption In addition, a large amount of biogas slurry produced after fermentation needs to be treated. The wet fermentation device has large investment, large land occupation, high energy consumption, and low gas production rate per unit volume.

发明内容 Contents of the invention

本实用新型的目的是提供一种垂直运行的干式厌氧消化装置,它能直接处理有机废物,具有运行简便,投资省的特点,可解决现有技术的上述不足之处。The purpose of this utility model is to provide a vertically running dry anaerobic digestion device, which can directly process organic waste, has the characteristics of simple operation and low investment, and can solve the above-mentioned shortcomings of the prior art.

一种垂直运行的干式厌氧消化装置,有立式厌氧消化罐罐体,它的顶部有沼气外排口、安全阀接口和检修人孔,底部为锥形斗,其特征是锥形斗的下口与控制阀门的入口连通,控制阀门的出口通过管道与进料循环泵的上口连通,进料循环泵的上口还通过阀门与进料斗的下口连通,进料循环泵的下口通过管道、阀门与厌氧消化罐罐体内垂直竖立的2-10根进料管道的入口连通,各进料管道的出口均靠近厌氧消化罐罐体的顶部,厌氧消化罐罐体的底部有支架。A vertically running dry anaerobic digestion device with a vertical anaerobic digestion tank body, the top of which has a biogas outlet, a safety valve interface and a maintenance manhole, and a conical bucket at the bottom, which is characterized by a conical The lower port of the bucket is connected with the inlet of the control valve, the outlet of the control valve is connected with the upper port of the feeding circulation pump through the pipeline, and the upper port of the feeding circulating pump is also connected with the lower port of the feeding hopper through the valve, and the feeding circulating pump The lower opening of the anaerobic digestion tank communicates with the inlets of 2-10 vertically erected feed pipes in the anaerobic digestion tank through pipes and valves. The outlets of each feed pipe are close to the top of the anaerobic digestion tank. There are brackets at the bottom of the body.

本实用新型处理物料时,含固率可以达到15-40%;结构简单,无内部搅拌机械和活动部件,免维护,操作管理简便;厌氧消化罐容积产气率可达5-20m3/m3;无废水产生,无固体沉积,密闭不释放废气。When the utility model handles materials, the solid content rate can reach 15-40%; the structure is simple, without internal stirring machinery and moving parts, maintenance-free, easy to operate and manage; the gas production rate of the volume of the anaerobic digestion tank can reach 5-20m 3 / m 3 ; No waste water, no solid deposits, no waste gas release in airtight.

附图说明 Description of drawings

附图为本实用新型的结构示意图。Accompanying drawing is the structural representation of the utility model.

具体实施方式 Detailed ways

本实用新型有立式厌氧消化罐罐体1,它的顶部有沼气外排口(图中未画出),安全阀接口(图中未画出)和检修人孔(图中未画出),底部为锥形斗4,其特征是锥形斗4的下口与控制阀门5的入口连通,控制阀门5的出口通过管道8与进料循环泵2的上口连通,进料循环泵2的上口还通过阀门7与进料斗6的下口连通,进料循环泵2的下口通过管道、阀门与厌氧消化罐罐体1内垂直竖立的2-10根进料管道3的入口连通,进料管道3的出口靠近厌氧消化罐罐体1的顶部,厌氧消化罐罐体1的底部有支架9。The utility model has a vertical anaerobic digestion tank body 1, and its top has a biogas outlet (not shown in the figure), a safety valve interface (not shown in the figure) and a maintenance manhole (not shown in the figure). ), the bottom is a conical bucket 4, which is characterized in that the lower mouth of the conical bucket 4 communicates with the inlet of the control valve 5, and the outlet of the control valve 5 communicates with the upper mouth of the feed circulation pump 2 through a pipeline 8, and the feed circulation pump The upper port of 2 is also communicated with the lower port of the feed hopper 6 through the valve 7, and the lower port of the feed circulation pump 2 is connected with 2-10 feed pipes 3 vertically erected in the anaerobic digestion tank body 1 through pipelines and valves. The inlet of the feed pipe 3 is close to the top of the anaerobic digestion tank body 1, and the bottom of the anaerobic digestion tank body 1 has a bracket 9.

使用本垂直运行的干式厌氧消化装置时,使有机废物(干物质的重量百分含量15-40%)通过进料斗6进入进料循环泵2内,该物料通过管道、阀门被送入进料管道3内,垂直向上运行到进料管道3的出口被推出,并垂直跌落在厌氧消化罐罐体1内,落在厌氧消化罐罐体1底部的物料在锥形斗4的引导下,通过控制阀门5和管道8被送入进料循环泵2内。采用序批式进料,可使生物料与循环的熟物料以一定配比进行混合。向进料斗6进物料时打开阀门7,不进物料时关闭阀门7。在厌氧消化罐罐体1内没有任何机械搅拌装置,物料经进料循环泵2在厌氧消化罐罐体1内从上至下不断循环、成层运动。厌氧消化罐罐体1可以是圆柱形钢罐、拼装罐或钢混罐体。所述的进料循环泵2可为输送高浓度物料的往复泵、转子泵或螺杆泵。When using this vertically running dry anaerobic digestion device, organic waste (15-40% by weight of dry matter) enters the feed circulation pump 2 through the feed hopper 6, and the material is sent to the feed circulation pump 2 through pipelines and valves. into the feed pipe 3, run vertically upwards until the outlet of the feed pipe 3 is pushed out, and fall vertically into the anaerobic digestion tank body 1, and the material falling on the bottom of the anaerobic digestion tank body 1 is in the conical bucket 4 Under the guidance of the control valve 5 and pipeline 8, it is sent into the feed circulation pump 2. By adopting sequential batch feeding, the biological material and the recycled clinker can be mixed in a certain ratio. Open the valve 7 when feeding materials into the feed hopper 6, and close the valve 7 when not feeding materials. There is no mechanical stirring device in the tank body 1 of the anaerobic digestion tank, and the material circulates continuously and moves in layers through the feed circulation pump 2 in the tank body 1 of the anaerobic digestion tank from top to bottom. The tank body 1 of the anaerobic digestion tank can be a cylindrical steel tank, an assembled tank or a steel-mixed tank body. The feed circulation pump 2 can be a reciprocating pump, a rotor pump or a screw pump for conveying high-concentration materials.

Claims (2)

1. the dry anaerobic digestion device of a vertical operation has vertical type anaerobic digester tank body (1), and its top has biogas to efflux mouth; Relief valve connection and inspection manhole, the bottom is taper bucket (4), the end opening that it is characterized in that taper bucket (4) is communicated with the inlet of by-pass valve control (5), the outlet of by-pass valve control (5) is by suitable for reading being communicated with of pipeline (8) with feed cycle pump (2), the suitable for reading of feed cycle pump (2) also is communicated with the end opening of hopper (6) by valve (7), the end opening of feed cycle pump (2) passes through pipeline, the inlet of the 2-10 root feed pipe (3) that stands vertically in valve and the anaerobic digestion tank (1) is communicated with, all near the top of anaerobic digestion tank (1), support (9) is arranged at the bottom of anaerobic digestion tank (1) in the outlet of each feed pipe (3).
2. the dry anaerobic digestion device of vertical operation as claimed in claim 1 is characterized in that described feed cycle pump (2) is reciprocation pump, rotor pump or spiral pump.
CNU2007200265328U 2007-08-11 2007-08-11 Vertical operation dry-type anaerobic digestion device Expired - Fee Related CN201080460Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2007200265328U CN201080460Y (en) 2007-08-11 2007-08-11 Vertical operation dry-type anaerobic digestion device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2007200265328U CN201080460Y (en) 2007-08-11 2007-08-11 Vertical operation dry-type anaerobic digestion device

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101812400A (en) * 2009-12-22 2010-08-25 上海济兴能源环保技术有限公司 Vertical dry-process anaerobic fermentation device
CN102344232A (en) * 2011-07-21 2012-02-08 农业部沼气科学研究所 Method for producing biogas and organic fertilizer by dry fermentation of livestock and poultry feces
CN102453731A (en) * 2010-10-27 2012-05-16 青岛天人环境股份有限公司 Process and equipment for preparing methane by continuous dry fermentation
CN103667018A (en) * 2012-09-07 2014-03-26 天津市北方园林生态科学技术研究所 Small-sized marsh gas generator with conical bottom
CN104843202A (en) * 2014-10-13 2015-08-19 瑞安市恺鸿包装机械有限公司 Full-automatic charging mechanism
WO2019166694A1 (en) * 2018-02-27 2019-09-06 Biogts Oy Reactor for producing biogas from biomass using anaerobic digestion

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101812400A (en) * 2009-12-22 2010-08-25 上海济兴能源环保技术有限公司 Vertical dry-process anaerobic fermentation device
CN102453731A (en) * 2010-10-27 2012-05-16 青岛天人环境股份有限公司 Process and equipment for preparing methane by continuous dry fermentation
CN102344232A (en) * 2011-07-21 2012-02-08 农业部沼气科学研究所 Method for producing biogas and organic fertilizer by dry fermentation of livestock and poultry feces
CN103667018A (en) * 2012-09-07 2014-03-26 天津市北方园林生态科学技术研究所 Small-sized marsh gas generator with conical bottom
CN104843202A (en) * 2014-10-13 2015-08-19 瑞安市恺鸿包装机械有限公司 Full-automatic charging mechanism
WO2019166694A1 (en) * 2018-02-27 2019-09-06 Biogts Oy Reactor for producing biogas from biomass using anaerobic digestion
CN111868225A (en) * 2018-02-27 2020-10-30 碧奥新能源有限公司 Reactor for biogas production from biomass using anaerobic digestion

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C14 Grant of patent or utility model
GR01 Patent grant
C56 Change in the name or address of the patentee

Owner name: QINGDAO TIANREN ENVIRONMENT CO., LTD.

Free format text: FORMER NAME: QINGDAO TIANREN ENVIRONMENT ENGINEERING CO., LTD.

CP01 Change in the name or title of a patent holder

Address after: 266101 Shandong city of Qingdao province high tech Zone Keyuan Road by the two Heaven Qingdao Environmental Engineering Co.

Patentee after: Qingdao Tianren Environment Co., Ltd.

Address before: 266101 Shandong city of Qingdao province high tech Zone Keyuan Road by the two Heaven Qingdao Environmental Engineering Co.

Patentee before: Qingdao Tianren Environment Engineering Co., Ltd.

DD01 Delivery of document by public notice

Addressee: Chen Ping

Document name: Notification of Passing Examination on Formalities

C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20080702

Termination date: 20120811