CN208586106U - Sewage treatment device of integrated membrane bioreactor - Google Patents
Sewage treatment device of integrated membrane bioreactor Download PDFInfo
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- CN208586106U CN208586106U CN201820636754.XU CN201820636754U CN208586106U CN 208586106 U CN208586106 U CN 208586106U CN 201820636754 U CN201820636754 U CN 201820636754U CN 208586106 U CN208586106 U CN 208586106U
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- peristaltic pump
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- 239000012528 membrane Substances 0.000 title claims abstract description 35
- 239000010865 sewage Substances 0.000 title claims abstract description 28
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 181
- 230000002572 peristaltic effect Effects 0.000 claims abstract description 31
- 238000005276 aerator Methods 0.000 claims abstract description 24
- 239000010802 sludge Substances 0.000 claims abstract description 7
- 238000005192 partition Methods 0.000 claims abstract description 5
- 230000008676 import Effects 0.000 claims abstract 2
- 238000005273 aeration Methods 0.000 claims description 3
- 230000037431 insertion Effects 0.000 claims 1
- 238000003780 insertion Methods 0.000 claims 1
- 239000002033 PVDF binder Substances 0.000 description 3
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 3
- 239000007788 liquid Substances 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000009285 membrane fouling Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000006213 oxygenation reaction Methods 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
技术领域technical field
本实用新型涉及一种污水处理,具体涉及一体化膜生物反应器的污水处理装置。The utility model relates to sewage treatment, in particular to a sewage treatment device of an integrated membrane biological reactor.
背景技术Background technique
伴随生活质量的提高,人们对环境要求越来越高,对于大量排放的生活污水,早就引起社会的广泛关注。目前,公知的膜处理污水装置是由多个不同处理功能的设备顺序串联而成,并非一体化,在处理污水的时候,预处理需要单独进行,并且处理过后还需要放置到平板膜的装置中,效率低,浪费资源。With the improvement of the quality of life, people have higher and higher requirements for the environment, and a large amount of domestic sewage has long been aroused widespread concern in the society. At present, the known membrane sewage treatment device is composed of multiple devices with different treatment functions in series, which is not integrated. When treating sewage, pretreatment needs to be carried out separately, and after treatment, it needs to be placed in a flat membrane device. , low efficiency and waste of resources.
实用新型内容Utility model content
为解决现有技术的不足,本实用新型的目的在于提供一体化膜生物反应器的污水处理装置,该装置可通过对活性污泥进行曝气来对污水进行初步的处理从而降低污水有机物的浓度,将混合液回流和充氧功能融为一体,降低能耗,提高膜的寿命。In order to solve the deficiencies of the prior art, the purpose of this utility model is to provide a sewage treatment device of an integrated membrane bioreactor, which can perform preliminary treatment on sewage by aerating activated sludge to reduce the concentration of organic matter in sewage , which integrates the mixed liquid reflux and oxygenation functions to reduce energy consumption and improve the life of the membrane.
为了实现上述目标,本实用新型采用如下的技术方案:In order to achieve the above-mentioned goals, the utility model adopts the following technical scheme:
一体化膜生物反应器的污水处理装置,包括水箱、曝气器、第一蠕动泵、第二蠕动泵、平板膜、流量计;所述水箱通过隔板分为第一水箱和第二水箱,所述第二水箱上方设有第三水箱;The sewage treatment device of the integrated membrane bioreactor includes a water tank, an aerator, a first peristaltic pump, a second peristaltic pump, a flat membrane, and a flow meter; the water tank is divided into a first water tank and a second water tank by a partition plate, A third water tank is arranged above the second water tank;
所述第一水箱顶部设有支架,支架靠近第三水箱左侧边,所述支架上方设有曝气器和第一蠕动泵,所述曝气器一接口与第一水管一端相连接,所述第一水管另一端插入第三水箱,所述曝气器另一接口连接的第一水管与第一蠕动泵连接的第一水管通过三通汇集于第一水箱;The top of the first water tank is provided with a bracket, the bracket is close to the left side of the third water tank, an aerator and a first peristaltic pump are arranged above the bracket, and an interface of the aerator is connected with one end of the first water pipe, so The other end of the first water pipe is inserted into the third water tank, and the first water pipe connected to the other interface of the aerator and the first water pipe connected to the first peristaltic pump are collected in the first water tank through a tee;
所述第一水箱内设有活性污泥和平板膜,所述第二水箱底部设有第二蠕动泵,侧壁固定有流量计,所述平板膜通过第二水管依次与第二蠕动泵、流量计的输入端口串联连接,所述流量计的输出端口通过第三水管导入第三水箱。Activated sludge and a flat membrane are arranged in the first water tank, a second peristaltic pump is arranged at the bottom of the second water tank, a flow meter is fixed on the side wall, and the flat membrane is sequentially connected with the second peristaltic pump, The input ports of the flowmeter are connected in series, and the output port of the flowmeter is led into the third water tank through the third water pipe.
优选的,所述第三水箱左壁一端设有若干处于同一水平的溢流孔,所述第一水管通过溢流孔插入第三水箱。Preferably, one end of the left wall of the third water tank is provided with a plurality of overflow holes at the same level, and the first water pipe is inserted into the third water tank through the overflow holes.
优选的,所述隔板上端设有第一开孔,所述第二水管穿过第一开孔与平板膜和第二蠕动泵相连接。Preferably, the upper end of the separator is provided with a first opening, and the second water pipe is connected to the flat membrane and the second peristaltic pump through the first opening.
优选的,所述第二水箱右壁设有流量计和第二开孔,所述第三水管穿过第二开孔连接流量计的输出端口与第三水箱顶部。Preferably, the right wall of the second water tank is provided with a flow meter and a second opening, and the third water pipe passes through the second opening to connect the output port of the flow meter and the top of the third water tank.
进一步优选的,所述第一水管、第二水管、第三水管均采用软管。Further preferably, the first water pipe, the second water pipe and the third water pipe are all hoses.
进一步优选的,所述第二水箱和第三水箱之间联通有一固定位置的坚硬导水管,所述导水管的一端连接第二开孔,所述导水管另一端伸入第三水箱,所述第三水管穿过导水管与第三水箱相连接。Further preferably, a rigid water conduit at a fixed position is communicated between the second water tank and the third water tank, one end of the water conduit is connected to the second opening, and the other end of the water conduit extends into the third water tank, and the The third water pipe is connected with the third water tank through the water conduit.
优选的,所述第三水箱的宽度等于第二水箱宽度,长度大于第二水箱的长度,小于水箱的长度。Preferably, the width of the third water tank is equal to the width of the second water tank, and the length is greater than the length of the second water tank and less than the length of the water tank.
优选的,所述平板膜设有若干个,且相互平行,所述平板膜与第一水箱的底部相互垂直。Preferably, several flat membranes are provided and are parallel to each other, and the flat membranes are perpendicular to the bottom of the first water tank.
优选的,所述曝气器采用的是射流曝气器。Preferably, the aerator is a jet aerator.
本实用新型的有益之处在于:本实用新型的一体化膜生物反应器的污水处理装置,处理污水时,活性污泥在曝气条件下,氧化污水使废水中的有机污染物分解;具有较高的表面错流速度,可有效控制由悬浮物、胶体物质形成凝胶层产生的膜污染问题;采用流量计控制流速,结构简单。The utility model has the advantages that: the sewage treatment device of the integrated membrane bioreactor of the present utility model, when treating sewage, the activated sludge oxidizes the sewage under aeration conditions to decompose the organic pollutants in the wastewater; The high surface cross-flow velocity can effectively control the membrane fouling problem caused by the formation of the gel layer by the suspended solids and colloidal substances; the flow meter is used to control the flow rate, and the structure is simple.
附图说明Description of drawings
图1为本实用新型的一体化膜生物反应器的污水处理装置的结构示意图。FIG. 1 is a schematic structural diagram of the sewage treatment device of the integrated membrane bioreactor of the present invention.
附图中标记的含义如下:1、水箱,101、第一水箱,102、第二水箱,2、第二蠕动泵,3、第二水管,4、第三水管,5、流量计,6、导水管,7、第三水箱,8、溢流孔,9、曝气器,10、第一蠕动泵,11、支架,12、第一水管,13、平板膜,14、第一开孔,15、第二开孔。The meanings of the symbols in the accompanying drawings are as follows: 1, water tank, 101, first water tank, 102, second water tank, 2, second peristaltic pump, 3, second water pipe, 4, third water pipe, 5, flow meter, 6, Water conduit, 7, third water tank, 8, overflow hole, 9, aerator, 10, first peristaltic pump, 11, bracket, 12, first water pipe, 13, flat membrane, 14, first opening, 15. The second opening.
具体实施方式Detailed ways
以下结合附图和具体实施例对本实用新型作具体的介绍。The present utility model is described in detail below with reference to the accompanying drawings and specific embodiments.
如图1所示,一体化膜生物反应器的污水处理装置,包括水箱1、曝气器9、第一蠕动泵10、第二蠕动泵2、平板膜13、流量计5;所述水箱1通过隔板分为第一水箱101和第二水箱102,所述第二水箱102上方设有第三水箱7;As shown in Figure 1, the sewage treatment device of the integrated membrane bioreactor includes a water tank 1, an aerator 9, a first peristaltic pump 10, a second peristaltic pump 2, a flat membrane 13, and a flow meter 5; the water tank 1 It is divided into a first water tank 101 and a second water tank 102 by a partition, and a third water tank 7 is arranged above the second water tank 102;
所述第一水箱101顶部设有支架11,所述支架11上方设有曝气器9和第一蠕动泵10,所述曝气器9一接口与第一水管12一端相连接,所述第一水管12另一端插入第三水箱7,所述曝气器9另一接口连接的第一水管12与第一蠕动泵10连接的第一水管12通过三通汇集于第一水箱101;The top of the first water tank 101 is provided with a bracket 11, an aerator 9 and a first peristaltic pump 10 are arranged above the bracket 11, an interface of the aerator 9 is connected to one end of the first water pipe 12, and the first water pipe 12 is connected to the first water pipe 12. The other end of a water pipe 12 is inserted into the third water tank 7, and the first water pipe 12 connected to the other interface of the aerator 9 and the first water pipe 12 connected to the first peristaltic pump 10 are collected in the first water tank 101 through a tee;
所述第一水箱101内设有活性污泥和PVDF平板膜13,所述第二水箱102底部设有第二蠕动泵2,侧壁固定有流量计5,通过流量计5控制灌入第三水箱7内水的速度,所述平板膜13通过第二水管3依次与第二蠕动泵2、流量计5的输入端口串联连接,所述流量计5的输出端口通过第三水管4导入第三水箱7,将处理过的污水送入第三水箱7。The first water tank 101 is provided with activated sludge and PVDF flat membrane 13, the second water tank 102 is provided with a second peristaltic pump 2 at the bottom, and a flow meter 5 is fixed on the side wall, through which the flow meter 5 controls the filling into the third water tank. The speed of the water in the water tank 7, the flat membrane 13 is sequentially connected in series with the input port of the second peristaltic pump 2 and the flowmeter 5 through the second water pipe 3, and the output port of the flowmeter 5 is introduced into the third through the third water pipe 4. The water tank 7 sends the treated sewage into the third water tank 7 .
所述第三水箱7左壁一端设有若干处于同一水平的溢流孔8,当第三水箱7内水位高度达到溢流孔8高度时,水直接通过溢流孔8流入第一水箱101,稀释第一水箱101污水浓度,保护PVDF平板膜13;所述第一水管12通过溢流孔8插入第三水箱7。One end of the left wall of the third water tank 7 is provided with a number of overflow holes 8 at the same level. When the water level in the third water tank 7 reaches the height of the overflow hole 8, the water directly flows into the first water tank 101 through the overflow hole 8, Dilute the concentration of sewage in the first water tank 101 to protect the PVDF flat membrane 13 ; the first water pipe 12 is inserted into the third water tank 7 through the overflow hole 8 .
所述隔板上端设有第一开孔14,所述第二水管3穿过第一开孔14与PVDF平板膜13和第二蠕动泵2相连接。The upper end of the separator is provided with a first opening 14 , and the second water pipe 3 is connected to the PVDF flat membrane 13 and the second peristaltic pump 2 through the first opening 14 .
所述第二水箱102右壁设有流量计5和第二开孔15,所述第三水管4穿过第二开孔15连接流量计5的输出端口与第三水箱7顶部。The right wall of the second water tank 102 is provided with a flow meter 5 and a second opening 15 , and the third water pipe 4 passes through the second opening 15 to connect the output port of the flow meter 5 and the top of the third water tank 7 .
所述第一水管12、第二水管3、第三水管4均采用软管,任意改变形状,方便安装。The first water pipe 12 , the second water pipe 3 and the third water pipe 4 are all made of hoses, and the shape can be changed arbitrarily, which is convenient for installation.
所述第二水箱102和第三水箱7之间联通有一固定位置的坚硬导水管6,为使导水管6有固定形状,所述导水管6的一端连接第二开孔15,所述导水管6另一端伸入第三水箱7,所述第三水管4穿过导水管6与第三水箱7相连接,因为第三水管4为软管,不方便固定,将第三水管4穿入有固定形状的导水管6,可将第三水管4固定住。A rigid water conduit 6 at a fixed position is communicated between the second water tank 102 and the third water tank 7. In order to make the water conduit 6 have a fixed shape, one end of the water conduit 6 is connected to the second opening 15. 6. The other end extends into the third water tank 7, and the third water pipe 4 is connected to the third water tank 7 through the water conduit 6. Because the third water pipe 4 is a hose, it is inconvenient to fix. The water conduit 6 with a fixed shape can fix the third water pipe 4 .
所述第三水箱7的宽度等于第二水箱102宽度,长度大于第二水箱102的长度,小于水箱1的总长度,以便于第三水箱7内的水通过溢流孔8正好落入第一水箱101。The width of the third water tank 7 is equal to the width of the second water tank 102, and the length is greater than the length of the second water tank 102, and less than the total length of the water tank 1, so that the water in the third water tank 7 just falls into the first water tank through the overflow hole 8. Water tank 101 .
所述平板膜13设有若干个,且相互平行,所述平板膜13与第一水箱101的底部相互垂直。若干平板膜13之间为并联,汇集于第二水管3。Several flat membranes 13 are provided and are parallel to each other, and the flat membranes 13 and the bottom of the first water tank 101 are perpendicular to each other. Several flat membranes 13 are connected in parallel, and are collected in the second water pipe 3 .
所述曝气器9采用的是射流曝气器9。The aerator 9 is a jet aerator 9 .
第一蠕动泵10吸入第三水箱7内的水,与射流曝气器9所吸入的气体在三通中混合,通过第一软管放出。由于曝气量3.5L/min远大于吸水量90mL/min,气液混合体以喷射状放出。第三水箱7内的水平板膜13和第二蠕动泵2的一接口通过穿过第一开孔14的第二水管3串联,再将蠕动泵的另一接口通过第二水管3连接到流量计5的输入端口;最终处理后的污水通过与流量计5串联的第三水管4导入第三水箱7。第一水箱101中置有平板膜13与活性污泥,使用支撑架上的射流曝气器9曝气。第三水箱7内的水达到溢流孔8的水位时可将处理过的水体溢流到第一水箱101,降低第一水箱101污染物浓度,再次处理,达到循环处理的目的。The first peristaltic pump 10 sucks the water in the third water tank 7, mixes it with the gas sucked in by the jet aerator 9 in the tee, and releases it through the first hose. Since the aeration rate of 3.5L/min is much larger than the water absorption rate of 90mL/min, the gas-liquid mixture is released in a jet. The horizontal plate membrane 13 in the third water tank 7 and one interface of the second peristaltic pump 2 are connected in series through the second water pipe 3 passing through the first opening 14 , and then the other interface of the peristaltic pump is connected to the flow rate through the second water pipe 3 The input port of the meter 5; the finally treated sewage is introduced into the third water tank 7 through the third water pipe 4 connected in series with the flow meter 5. The first water tank 101 is provided with a flat membrane 13 and activated sludge, which is aerated by the jet aerator 9 on the support frame. When the water in the third water tank 7 reaches the water level of the overflow hole 8, the treated water can be overflowed to the first water tank 101 to reduce the pollutant concentration of the first water tank 101, and then reprocessed to achieve the purpose of circulating treatment.
以上显示和描述了本实用新型的基本原理、主要特征和优点。本行业的技术人员应该了解,上述实施例不以任何形式限制本实用新型,凡采用等同替换或等效变换的方式所获得的技术方案,均落在本实用新型的保护范围内。The basic principles, main features and advantages of the present invention have been shown and described above. Those skilled in the art should understand that the above-mentioned embodiments do not limit the present invention in any form, and all technical solutions obtained by means of equivalent replacement or equivalent transformation all fall within the protection scope of the present invention.
Claims (9)
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