CN115448450A - Two-phase anaerobic fermentation device - Google Patents
Two-phase anaerobic fermentation device Download PDFInfo
- Publication number
- CN115448450A CN115448450A CN202211146480.3A CN202211146480A CN115448450A CN 115448450 A CN115448450 A CN 115448450A CN 202211146480 A CN202211146480 A CN 202211146480A CN 115448450 A CN115448450 A CN 115448450A
- Authority
- CN
- China
- Prior art keywords
- aeration
- rod
- stirring
- stirring rod
- stirring blade
- Prior art date
- 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.)
- Pending
Links
- 238000000855 fermentation Methods 0.000 title claims abstract description 26
- 238000003756 stirring Methods 0.000 claims abstract description 127
- 238000005273 aeration Methods 0.000 claims abstract description 108
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 19
- 238000005192 partition Methods 0.000 claims description 26
- 238000010992 reflux Methods 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 abstract description 7
- 238000006243 chemical reaction Methods 0.000 abstract description 6
- 230000000694 effects Effects 0.000 abstract description 6
- 238000012544 monitoring process Methods 0.000 abstract description 3
- 239000010802 sludge Substances 0.000 abstract description 3
- 239000002245 particle Substances 0.000 abstract 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 230000000903 blocking effect Effects 0.000 description 4
- 238000013019 agitation Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 230000002708 enhancing effect Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 241001135750 Geobacter Species 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 230000027756 respiratory electron transport chain Effects 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/28—Anaerobic digestion processes
- C02F3/286—Anaerobic digestion processes including two or more steps
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/40—Mixers using gas or liquid agitation, e.g. with air supply tubes
- B01F33/402—Mixers using gas or liquid agitation, e.g. with air supply tubes comprising supplementary stirring elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/40—Mixers using gas or liquid agitation, e.g. with air supply tubes
- B01F33/402—Mixers using gas or liquid agitation, e.g. with air supply tubes comprising supplementary stirring elements
- B01F33/4021—Mixers using gas or liquid agitation, e.g. with air supply tubes comprising supplementary stirring elements the gas being introduced through the shaft of the stirring element
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/40—Mixers using gas or liquid agitation, e.g. with air supply tubes
- B01F33/407—Mixers using gas or liquid agitation, e.g. with air supply tubes by blowing gas on the material from above
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/40—Mixers using gas or liquid agitation, e.g. with air supply tubes
- B01F33/409—Parts, e.g. diffusion elements; Accessories
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/40—Mixers using gas or liquid agitation, e.g. with air supply tubes
- B01F33/4094—Plants
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/28—Anaerobic digestion processes
- C02F3/2866—Particular arrangements for anaerobic reactors
- C02F3/2873—Particular arrangements for anaerobic reactors with internal draft tube circulation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2203/00—Apparatus and plants for the biological treatment of water, waste water or sewage
- C02F2203/006—Apparatus and plants for the biological treatment of water, waste water or sewage details of construction, e.g. specially adapted seals, modules, connections
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/08—Chemical Oxygen Demand [COD]; Biological Oxygen Demand [BOD]
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Microbiology (AREA)
- Biodiversity & Conservation Biology (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
Description
技术领域technical field
本发明涉及微生物厌氧发酵技术领域,特别涉及到一种两相厌氧发酵装置。The invention relates to the technical field of microbial anaerobic fermentation, in particular to a two-phase anaerobic fermentation device.
背景技术Background technique
厌氧生物处理具有投资省、可回收利用能源的特点,是处理高浓度有机废水的主要方法。目前常见的反应器各有其优缺点,如内循环反应器能通过自身厌氧发酵反应完成相应循环,不需要额外动力驱动,但当仅依靠气体内循环,当进水水质不太稳定时,易导致其出水水量不稳定,出水水质也相对不稳定,同时,在进行高固体浓度厌氧发酵时,需进行搅拌,而仅靠曝气回流不能充分搅拌。Anaerobic biological treatment has the characteristics of low investment and recyclable energy, and is the main method for treating high-concentration organic wastewater. At present, the common reactors have their own advantages and disadvantages. For example, the internal circulation reactor can complete the corresponding cycle through its own anaerobic fermentation reaction without additional power drive. It is easy to cause unstable effluent water volume and relatively unstable effluent water quality. At the same time, when performing anaerobic fermentation with high solid concentration, stirring is required, but aeration and reflux alone cannot fully stir.
如公告号为CN202111251697的中国发明专利申请中公开了一种厌氧发酵循环装置,包括:壁板,壁板环绕形成一个内部的空腔,空腔内设置有循环室一与循环室二;进料口,进料口连接壁板形成的空腔与空腔外部;循环室一包括:气提缝一,三相分离器一,三相分离器一的一端连接气提缝一,下降室一,下降室一上侧连通进料口,厌氧区一,厌氧区一连通下降室一下侧;隔板一,隔板一设置于循环室一的下方;循环室二与循环室一呈水平布置,循环室二包括:三相分离器二,下降室二,厌氧区二,厌氧区二连通下降室二下侧;出料口,出料口连接壁板形成的空腔与空腔外部;盖板,盖板盖住壁板形成的空腔,盖板上设置有气孔,其不能监测出水水质,无法直观判断反应情况,不能及时进行后续工艺处理。For example, the Chinese invention patent application with the notification number CN202111251697 discloses an anaerobic fermentation circulation device, including: a wall plate surrounded by a wall plate to form an internal cavity, and a
发明内容Contents of the invention
本发明目的为提供一种两相厌氧发酵装置,旨在解决现有技术中两相厌氧发酵装置由于仅依靠气体内循环,当进水水质不太稳定时,易导致其出水水量不稳定,出水水质也相对不稳定,不能及时进行后续工艺处理的问题;The purpose of the present invention is to provide a two-phase anaerobic fermentation device, which aims to solve the problem that the two-phase anaerobic fermentation device in the prior art only relies on the internal circulation of gas, and when the water quality of the influent is not stable, it is easy to cause unstable water output. , the water quality of the effluent is relatively unstable, and the follow-up process treatment cannot be carried out in time;
为到达上述目的,本发明采用以下技术方案:一种两相厌氧发酵装置,包括:壁板,壁板环绕形成一个内部的空腔,空腔内设置有循环室一与循环室二,循环室一与循环室二分别设置有曝气搅拌棒一,曝气搅拌棒二;进料口,进料口连接壁板形成的空腔与空腔外部;出料口,出料口连接BOD传感器,BOD传感器用于检测出料口水质;盖板,盖板盖住壁板形成的空腔,盖板上设置有气孔,气孔通过管道连接流量计传感器;储气罐,储气罐通过管道连接流量计传感器;曝气泵,曝气泵一端连接储气罐,另一端连接曝气搅拌棒一与曝气搅拌棒二;控制器,控制器连接流量计传感器、曝气泵与BOD传感器;In order to achieve the above object, the present invention adopts the following technical solutions: a two-phase anaerobic fermentation device, comprising: a wall plate, surrounded by a wall plate to form an internal cavity, and a
上述技术方案中,本发明通过气孔连接气体流量计传感器,实现产气量的监测,当产气量较低时,控制器控制曝气泵进行沼气回流曝气,进而增强内循环效果,实现强化传质;BOD传感器与反应器出料口相连,BOD传感器实时监测出水水质情况,根据污水综合排放标准,当水体BOD含量小于20mg/L时,通过控制器控制出料口出料,然后在进料口进料继续进行反应,并通过曝气搅拌棒一、曝气搅拌棒二增强曝气回流效果,加快反应。In the above technical solution, the present invention connects the gas flow meter sensor through the stomata to realize the monitoring of gas production. When the gas production is low, the controller controls the aeration pump to perform biogas backflow aeration, thereby enhancing the internal circulation effect and realizing enhanced mass transfer. ;The BOD sensor is connected to the discharge port of the reactor, and the BOD sensor monitors the water quality of the effluent in real time. According to the comprehensive sewage discharge standard, when the BOD content of the water body is less than 20mg/L, the discharge port is controlled by the controller, and then at the feed port The feed continues to react, and the aeration and reflux effect is enhanced through the
进一步地,根据本发明实施例,循环室一包括:气提缝一,三相分离器一,三相分离器一一端连接气提缝一,下降室一,下降室一上侧连通进料口,厌氧区一,厌氧区一连通下降室一下侧;隔板一,隔板一设置于循环室一的下方;循环室二与循环室一呈水平布置,循环室二包括:三相分离器二,下降室二,厌氧区二,厌氧区二连通下降室二下侧,循环室二设置有气提缝二,气提缝二连接三相分离器二的一端,循环室二还设置有隔板二,隔板二与隔板一上下分布设置;隔板二设置在下降室二上侧;三相分离器一与隔板一之间形成回流缝一,回流缝一处设置有阻气板一,阻气板一设置于隔板一上;三相分离器二与壁板之间形成回流缝二,回流缝二处设置有阻气板二,阻气板二设置于壁板上。Further, according to the embodiment of the present invention, the
进一步地,根据本发明实施例,曝气搅拌棒一包括:搅拌杆一、曝气棒一、搅拌叶片一、曝气棒二、搅拌叶片二,搅拌杆一底部设置有旋转连接件一,曝气搅拌棒一通过旋转连接件一旋转连接于循环室一的底部。Further, according to an embodiment of the present invention, the
进一步地,根据本发明实施例,曝气搅拌棒二包括:搅拌杆二、曝气棒三、搅拌叶片三、曝气棒四、搅拌叶片四,搅拌杆二底部设置有旋转连接件二,曝气搅拌棒二通过旋转连接件一旋转连接于循环室二的底部。Further, according to the embodiment of the present invention, the
更进一步地,根据本发明实施例,搅拌叶片一设置于曝气棒一上方,搅拌叶片二(196)设置于曝气棒二上方。Furthermore, according to the embodiment of the present invention, the first stirring blade is arranged above the first aeration rod, and the second stirring blade (196) is arranged above the second aeration rod.
更进一步地,根据本发明实施例,搅拌叶片三设置于曝气棒三上方,搅拌叶片四设置于曝气棒四上方。Furthermore, according to the embodiment of the present invention, the third stirring blade is arranged above the third aeration rod, and the fourth stirring blade is arranged above the fourth aeration rod.
更进一步地,根据本发明实施例,曝气棒一上设置至少3个开气孔,搅拌叶片一设置为相对于水平位置倾斜15°-75°,曝气棒二上设置至少3个开气孔,搅拌叶片二设置为相对于水平位置倾斜15°-75°。Furthermore, according to an embodiment of the present invention, at least 3 air holes are set on the first aeration rod, the first stirring blade is set to be inclined by 15°-75° relative to the horizontal position, and at least 3 air holes are set on the second aeration rod, The second stirring blade is set to be inclined at 15°-75° relative to the horizontal position.
更进一步地,根据本发明实施例,曝气棒三上设置至少3个开气孔,搅拌叶片三设置为相对于水平位置倾斜15°-75°,曝气棒四上设置至少3个开气孔,搅拌叶片四设置为相对于水平位置倾斜15°-75°。Furthermore, according to an embodiment of the present invention, at least 3 air holes are set on the third aeration rod, the third stirring blade is set to be inclined at 15°-75° relative to the horizontal position, and at least 3 air holes are set on the fourth aeration rod, The four stirring blades are set to incline 15°-75° relative to the horizontal position.
进一步地,根据本发明实施例,出料口还连接有出料水箱。Further, according to an embodiment of the present invention, the discharge port is also connected with a discharge water tank.
本发明通过气体流量计传感器,实现产气量的监测,当产气量较低时,控制器控制曝气泵进行沼气回流曝气,进而增强内循环效果,实现强化传质;BOD传感器实时监测出水水质情况,当水体BOD含量小于20mg/L时,通过控制器控制出料口出料,然后在进料口进料继续进行反应;并通过曝气棒一、曝气棒二、曝气棒三、曝气棒四上的气孔曝气,当气体向上分别经过搅拌叶片一、搅拌叶片二、搅拌叶片三、搅拌叶片四时,带动搅拌叶片一、搅拌叶片二、搅拌叶片三、搅拌叶片四旋转,通过气流驱动机械搅拌,结合曝气回流,在进行高固体浓度厌氧发酵时也能实现充分搅拌,加快反应速率。The invention realizes the monitoring of the gas production through the gas flow meter sensor. When the gas production is low, the controller controls the aeration pump to perform biogas backflow aeration, thereby enhancing the internal circulation effect and realizing enhanced mass transfer; the BOD sensor monitors the effluent water quality in real time When the BOD content of the water body is less than 20mg/L, the controller controls the discharge of the material at the discharge port, and then feeds the material at the feed port to continue the reaction; and through the
附图说明Description of drawings
下面结合附图和实施例对本发明进一步说明。The present invention will be further described below in conjunction with the accompanying drawings and embodiments.
图1是本发明一种两相厌氧发酵装置的结构示意图。Fig. 1 is a structural schematic diagram of a two-phase anaerobic fermentation device of the present invention.
图2是本发明一种两相厌氧发酵装置的曝气搅拌棒一的结构示意图。Fig. 2 is a schematic structural view of the
图3是本发明一种两相厌氧发酵装置的曝气搅拌棒二的结构示意图。Fig. 3 is a schematic structural view of the
附图中In the attached picture
1、进料口 2、气体缝一 3、三相分离器一1.
4、下降室一 5、厌氧区一 6、阻气板一4.
7、隔板一 8、隔板二 9、气体缝二7. Partition one 8. Partition two 9. Gas joint two
10、三相分离器二 11、下降室二 12、厌氧区二10. Three-phase separator two 11. Falling chamber two 12. Anaerobic zone two
13、阻气板二 14、出料口 15、气孔13.
16、流量计传感器 17、储气罐 18、曝气泵16.
19、曝气搅拌棒一 20、曝气搅拌棒二 21、BOD传感器19.
22、出料水箱 23、控制器 191、搅拌杆一22. Discharging
192、旋转连接件一 193、曝气棒一 194、搅拌叶片一192.
195、曝气棒二 196、搅拌叶片二 201、搅拌杆二195.
202、旋转连接件二 203、曝气棒三 204、搅拌叶片三202.
205、曝气棒四 206、搅拌叶片四205.
具体实施方式detailed description
为了使本发明的目的、技术方案进行清楚、完整地描述,及优点更加清楚明白,以下结合附图对本发明实施例进行进一步详细说明。应当理解,此处所描述的具体实施例是本发明一部分实施例,而不是全部的实施例,仅仅用以解释本发明实施例,并不用于限定本发明实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。In order to clearly and completely describe the purpose, technical solution, and advantages of the present invention, the embodiments of the present invention will be further described in detail below in conjunction with the accompanying drawings. It should be understood that the specific embodiments described here are part of the embodiments of the present invention, rather than all embodiments, and are only used to explain the embodiments of the present invention, and are not intended to limit the embodiments of the present invention. All other embodiments obtained under the premise of creative work all belong to the protection scope of the present invention.
在本发明的描述中,需要说明的是,术语“中心”、“中”“上”、“下”、“左”、“右”、“内”、“外”、“顶”、“底”、“侧”、“竖直”、“水平”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本发明和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本发明的限制。In the description of the present invention, it should be noted that the terms "center", "middle", "upper", "lower", "left", "right", "inner", "outer", "top", "bottom" ", "side", "vertical", "horizontal" and other indicated orientations or positional relationships are based on the orientations or positional relationships shown in the drawings, and are only for the convenience of describing the present invention and simplifying the description, rather than indicating or implying the It should not be construed as limiting the invention that a device or element must have a particular orientation, be constructed, and operate in a particular orientation.
出于简明和说明的目的,实施例的原理主要通过参考例子来描述。在以下描述中,很多具体细节被提出用以提供对实施例的彻底理解。然而明显的是。对于本领域普通技术人员,这些实施例在实践中可以不限于这些具体细节。在一些实例中,没有详细地描述公知方法和结构,以避免无必要地使这些实施例变得难以理解。另外,所有实施例可以互相结合使用。For purposes of simplicity and illustration, the principles of the embodiments are mainly described with reference to examples. In the following description, numerous specific details are set forth in order to provide a thorough understanding of the embodiments. However obvious it is. To those of ordinary skill in the art, the embodiments may in practice not be limited to these specific details. In some instances, well-known methods and structures have not been described in detail to avoid unnecessarily obscuring the embodiments. In addition, all the embodiments can be used in combination with each other.
如图1所示,本实施例公开了一种两相厌氧发酵装置,包括:壁板,所述壁板环绕形成一个内部的空腔,所述空腔内设置有循环室一与循环室二,所述循环室一与所述循环室二分别设置有曝气搅拌棒一19,曝气搅拌棒二20;进料口1,所述进料口1连接所述壁板形成的空腔与空腔外部;出料口14,所述出料口14连接BOD传感器21,所述BOD传感器21用于检测所述出料口14水质;盖板,所述盖板盖住所述壁板形成的空腔,所述盖板上设置有气孔15,所述气孔15通过管道连接流量计传感器16;储气罐17,所述储气罐17通过管道连接流量计传感器16;曝气泵18,所述曝气泵18一端连接所述储气罐17,另一端连接所述曝气搅拌棒一19与所述曝气搅拌棒二20;控制器23,所述控制器23连接所述流量计传感器16、所述曝气泵18与所述BOD传感器21。As shown in Figure 1, the present embodiment discloses a two-phase anaerobic fermentation device, comprising: a wall plate, the wall plate surrounds and forms an internal cavity, and a circulation chamber 1 and a circulation chamber are arranged in the cavity Two, the circulation chamber one and the circulation chamber two are respectively provided with an aeration stirring rod one 19 and an aeration stirring rod two 20; a feed port 1, the feed port 1 is connected to the cavity formed by the wall plate With the outside of the cavity; the discharge port 14, the discharge port 14 is connected to the BOD sensor 21, and the BOD sensor 21 is used to detect the water quality of the discharge port 14; the cover plate, the cover plate covers the wall plate Formed cavity, the cover plate is provided with an air hole 15, the air hole 15 is connected to the flow meter sensor 16 through a pipeline; an air storage tank 17, and the air storage tank 17 is connected to the flow meter sensor 16 through a pipeline; an aeration pump 18 , one end of the aeration pump 18 is connected to the air storage tank 17, and the other end is connected to the aeration stirring rod one 19 and the aeration stirring rod two 20; the controller 23, the controller 23 is connected to the flow rate meter sensor 16, the aeration pump 18 and the BOD sensor 21.
具体地,所述循环室一包括:气提缝一2,三相分离器一3,所述三相分离器一3一端连接所述气提缝一2,下降室一4,所述下降室一4上侧连通所述进料口1,厌氧区一5,所述厌氧区一5连通所述下降室一4下侧;隔板一7,所述隔板一7设置于循环室一的下方;所述循环室二与所述循环室一呈水平布置,所述循环室二包括:三相分离器二10,下降室二11,厌氧区二12,所述厌氧区二12连通所述下降室二11下侧,所述循环室二设置有气提缝二9,所述气提缝二9连接所述三相分离器二10的一端,所述循环室二还设置有隔板二8,所述隔板二8与所述隔板一7上下分布设置;所述隔板二8设置在所述下降室二11上侧;所述三相分离器一3与所述隔板一7之间形成回流缝一,所述回流缝一处设置有阻气板一6,所述阻气板一6设置于所述隔板一7上;所述三相分离器二10与所述壁板之间形成回流缝二,所述回流缝二处设置有阻气板二13,所述阻气板二13设置于所述壁板上。Specifically, the circulation chamber one includes: air lift slot one 2, a three-phase separator one 3, one end of the three phase separator one 3 is connected to the air lift slot one 2, a descending chamber one 4, and the descending chamber The upper side of -4 communicates with the feed port 1, the anaerobic zone -5, and the anaerobic zone -5 communicates with the lower side of the descending chamber -4; the separator -7, the separator -7 is arranged in the circulation chamber Below one; said circulation chamber two and said circulation chamber one are arranged horizontally, said circulation chamber two comprises: three-phase separator two 10, descending chamber two 11, anaerobic zone two 12, said anaerobic zone two 12 communicates with the lower side of the second descending chamber 11, the second circulation chamber is provided with an air lift slot two 9, and the second air lift slot 9 is connected to one end of the three-phase separator two 10, and the second circulation chamber is also provided with There is a partition two 8, and the partition two 8 and the partition one 7 are distributed up and down; the partition two 8 is arranged on the upper side of the descending chamber two 11; the three-phase separator one 3 is connected to the A reflow slot 1 is formed between the partitions 7, and a gas baffle 6 is arranged at one of the reflux slots, and the gas baffle 6 is arranged on the partition 7; the three-phase separator 2 A second reflow slot is formed between 10 and the wall plate, and a second gas blocking plate 13 is arranged at the second reflow slot, and the second gas blocking plate 13 is arranged on the wall plate.
如图2所示,所述曝气搅拌棒一19包括:搅拌杆一191、曝气棒一193、搅拌叶片一194、曝气棒二195、搅拌叶片二196,所述搅拌杆一191底部设置有旋转连接件一192,所述曝气搅拌棒一19通过所述旋转连接件一191旋转连接于所述循环室一的底部。As shown in Figure 2, the aeration stirring rod one 19 includes: stirring rod one 191, aeration rod one 193, stirring blade one 194, aeration rod two 195, stirring blade two 196, the bottom of the stirring rod one 191 A
具体地,所述搅拌叶片一194设置于所述曝气棒一193上方,所述搅拌叶片二196设置于所述曝气棒二195上方。Specifically, the
更具体地,所述曝气棒一193上设置至少3个开气孔,所述搅拌叶片一194设置为相对于水平位置倾斜15°-75°,如具体设置为45°,所述曝气棒二195上设置至少3个开气孔,所述搅拌叶片二196设置为相对于水平位置倾斜15°-75°,如具体设置为45°;所述曝气棒一193上的开气孔设置为越远离搅拌杆一191的气孔间的间隔越小,越远离搅拌杆一191的气孔越大,曝气泵工作时,越远离搅拌杆一191的气泡越大越密集,当气泡上升至搅拌叶片一194时,搅拌叶片一194越远离搅拌杆一191处受力越大;所述曝气棒二195上的卡气孔设置为越远离搅拌杆一191的气孔间间隔越小,越远离搅拌杆一191的气孔越大,曝气泵工作时,越远离搅拌杆一191的气泡越大越密集,当气泡上升至搅拌叶片二196时,搅拌叶片二196越远离搅拌杆一191处受力越大,这样可更高效地带动搅拌叶片一194、搅拌叶片二196旋转搅拌,配合气泡曝气回流,达到充分搅拌循环室一的效果。More specifically, at least 3 air holes are set on the aeration rod one 193, and the agitation blade one 194 is set to be inclined at 15°-75° relative to the horizontal position, such as specifically set at 45°, the aeration rod one At least 3 air holes are set on the second 195, and the
如图3所示,所述曝气搅拌棒二20包括:搅拌杆二201、曝气棒三203、搅拌叶片三204、曝气棒四205、搅拌叶片四206,所述搅拌杆二201底部设置有旋转连接件二202,所述曝气搅拌棒二20通过所述旋转连接件一201旋转连接于所述循环室二的底部。As shown in Figure 3, the aeration stirring rod two 20 includes: stirring rod two 201, aeration rod three 203, stirring blade three 204, aeration rod four 205, stirring blade four 206, the bottom of the stirring rod two 201 A
具体地,所述搅拌叶片三204设置于所述曝气棒三203上方,所述搅拌叶片四206设置于所述曝气棒四205上方。Specifically, the
更具体地,所述曝气棒三203上设置至少3个开气孔,所述搅拌叶片三204设置为相对于水平位置倾斜15°-75°,如具体设置为45°,所述曝气棒四205上设置至少3个开气孔,所述搅拌叶片四206设置为相对于水平位置倾斜15°-75°如具体设置为45°;所述曝气棒三203上的开气孔设置为越远离搅拌杆二201的气孔间的间隔越小,越远离搅拌杆二201的气孔越大,曝气泵工作时,越远离搅拌杆二201的气泡越大越密集,当气泡上升至搅拌叶片三204时,搅拌叶片三204越远离搅拌杆二201处受力越大;所述曝气棒四205上的卡气孔设置为越远离搅拌杆二201的气孔间间隔越小,越远离搅拌杆二201的气孔越大,曝气泵工作时,越远离搅拌杆二201的气泡越大越密集,当气泡上升至搅拌叶片四206时,搅拌叶片四206越远离搅拌杆二201处受力越大,这样可更高效地带动搅拌叶片三204、搅拌叶片四206旋转搅拌,配合气泡曝气回流,达到充分搅拌循环室二的效果。More specifically, at least 3 air holes are provided on the
发酵过程中,也可通过在搅拌叶片一194、搅拌叶片二196、搅拌叶片三204、搅拌叶片四206上设置碳层,用碳层作为导体材料,介入厌氧氧化菌和甲烷菌之间的电子传递,使地杆菌分解有机物产生的电子直接被产甲烷菌利用,还原二氧化碳为甲烷,提高产甲烷量和污泥分解速度,提高污泥处理效率,节省投资。In the fermentation process, carbon layers can also be set on stirring blades one 194, stirring blades two 196, stirring blades three 204, and stirring blades four 206, and use the carbon layer as a conductor material to intervene between the anaerobic oxidizing bacteria and the methane bacteria. Electron transfer enables the electrons produced by Geobacter to decompose organic matter to be directly used by methanogens to reduce carbon dioxide to methane, increase methane production and sludge decomposition speed, improve sludge treatment efficiency, and save investment.
尽管上面对本发明说明性的具体实施方式进行了描述,以便于本技术领域的技术人员能够理解本发明,但是本发明不仅限于具体实施方式的范围,对本技术领域的普通技术人员而言,只要各种变化只要在所附的权利要求限定和确定的本发明精神和范围内,一切利用本发明构思的发明创造均在保护之列。Although the illustrative specific embodiments of the present invention have been described above, so that those skilled in the art can understand the present invention, the present invention is not limited to the scope of the specific embodiments. For those of ordinary skill in the art, as long as each As long as the changes are within the spirit and scope of the present invention defined and determined by the appended claims, all inventions and creations utilizing the concept of the present invention are included in the protection list.
Claims (9)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202211146480.3A CN115448450A (en) | 2022-09-20 | 2022-09-20 | Two-phase anaerobic fermentation device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202211146480.3A CN115448450A (en) | 2022-09-20 | 2022-09-20 | Two-phase anaerobic fermentation device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN115448450A true CN115448450A (en) | 2022-12-09 |
Family
ID=84304202
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202211146480.3A Pending CN115448450A (en) | 2022-09-20 | 2022-09-20 | Two-phase anaerobic fermentation device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN115448450A (en) |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2010167328A (en) * | 2009-01-20 | 2010-08-05 | Hitachi Plant Technologies Ltd | Aeration agitator |
CN105884021A (en) * | 2016-06-12 | 2016-08-24 | 武汉东川自来水科技开发有限公司 | Intermittent anaerobic wastewater treatment system and method |
CN112678946A (en) * | 2020-12-24 | 2021-04-20 | 华北水利水电大学 | Self-driven rotary aeration device |
CN112678945A (en) * | 2020-12-24 | 2021-04-20 | 华北水利水电大学 | Moving bed biofilm reactor based on blade self-driven rotary aeration |
CN113845998A (en) * | 2021-10-25 | 2021-12-28 | 西北农林科技大学 | Anaerobic fermentation circulating device |
-
2022
- 2022-09-20 CN CN202211146480.3A patent/CN115448450A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2010167328A (en) * | 2009-01-20 | 2010-08-05 | Hitachi Plant Technologies Ltd | Aeration agitator |
CN105884021A (en) * | 2016-06-12 | 2016-08-24 | 武汉东川自来水科技开发有限公司 | Intermittent anaerobic wastewater treatment system and method |
CN112678946A (en) * | 2020-12-24 | 2021-04-20 | 华北水利水电大学 | Self-driven rotary aeration device |
CN112678945A (en) * | 2020-12-24 | 2021-04-20 | 华北水利水电大学 | Moving bed biofilm reactor based on blade self-driven rotary aeration |
CN113845998A (en) * | 2021-10-25 | 2021-12-28 | 西北农林科技大学 | Anaerobic fermentation circulating device |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN206127003U (en) | Improved generation ozone catalytic oxidation device | |
CN103436435B (en) | Crop straw co-fermentation device | |
JP2015525667A (en) | Biological sewage treatment apparatus and method | |
CN218786554U (en) | An anaerobic reactor with biogas internal circulation | |
CN115784435A (en) | Micro-aerobic anaerobic reaction system with enhanced circulation | |
CN115448450A (en) | Two-phase anaerobic fermentation device | |
CN208218632U (en) | A kind of material filling type change air pressure reinforcing excess sludge ozone minimizing device | |
CN221740027U (en) | Fenton fluidized bed reactor | |
CN217732760U (en) | Green energy-saving environment-friendly water treatment device | |
CN114804343B (en) | A continuous flow reaction device for rapid cultivation of aerobic granular sludge | |
CN207016545U (en) | A kind of flow deflector for being used to fluidize cyclic aeration device | |
CN216039550U (en) | Anaerobic fermentation circulating device | |
CN105819542B (en) | Plasma sewage treatment device and treatment method thereof | |
CN105695309A (en) | Integrated device for conveying gas and stirring materials, and bioreactor comprising same | |
CN207121459U (en) | A kind of efficient ozone couples electroxidation device | |
CN215799554U (en) | Dry-type anaerobic system for stirring by utilizing gas pressure | |
CN211445199U (en) | COD oxidation unit of organic waste water | |
CN213885864U (en) | A medicament jar for sewage treatment | |
CN212655549U (en) | Pure oxygen aeration tank for sewage treatment | |
CN110255698B (en) | Water treatment device and method for strengthening mass transfer and oxidation process of ozone | |
CN110643492B (en) | Material stirring device and method for producing biogas through anaerobic fermentation | |
CN113845998A (en) | Anaerobic fermentation circulating device | |
CN2204803Y (en) | Dual circulating aerating lifting fertilizing tank with mixing components | |
CN206645885U (en) | Aerobic particle mud microorganism fungus kind cultivation reactor | |
CN220643075U (en) | Dry anaerobic fermentation tank does not have from producing gas agitated vessel |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20221209 |