CN101402487A - Water treatment system in two-stage moving bed biomembrane reactor - Google Patents
Water treatment system in two-stage moving bed biomembrane reactor Download PDFInfo
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- CN101402487A CN101402487A CNA2008102268531A CN200810226853A CN101402487A CN 101402487 A CN101402487 A CN 101402487A CN A2008102268531 A CNA2008102268531 A CN A2008102268531A CN 200810226853 A CN200810226853 A CN 200810226853A CN 101402487 A CN101402487 A CN 101402487A
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Abstract
本发明属于水处理领域,涉及一种两级移动床生物膜反应器中水处理系统。其特征是工艺全程采用可编程PLC自动控制系统,主要处理构筑物为两级串联的移动床生物膜反应器,具体工艺流程为:生活污水或类似水质的污水经格栅进入调节池,后经泵提升顺序进入一、二级MBBR反应器,然后出水在沉淀池进入清水池,再通过循环的紫外线杀菌消毒回用于冲厕、景观用水等。本发明的优点是1.中水处理效果好、有较强的抗冲击负荷能力、出水水质稳定。2.运行管理简便,占地面积小,维护方便,剩余污泥量少;采用PLC自动控制系统,自动化程度高。3.采用机械曝气方式,能耗小,充氧性能好,无需单独设置鼓风机设备。4.采用循环紫外线杀菌消毒方式,工艺全程无需添加药剂,可避免二次污染的发生。5.应用范围广。
The invention belongs to the field of water treatment and relates to a water treatment system in a two-stage moving bed biofilm reactor. It is characterized in that the whole process adopts programmable PLC automatic control system, and the main processing structure is a two-stage series moving bed biofilm reactor. The lifting sequence enters the first and second MBBR reactors, and then the effluent enters the clear water tank in the sedimentation tank, and then is sterilized by circulating ultraviolet light and reused for toilet flushing and landscape water. The advantages of the invention are: 1. Good reclaimed water treatment effect, strong impact load resistance and stable effluent quality. 2. Simple operation and management, small footprint, convenient maintenance, and less residual sludge; PLC automatic control system is adopted, with a high degree of automation. 3. The mechanical aeration method is adopted, with low energy consumption and good oxygenation performance, and there is no need to set up blower equipment separately. 4. The cycle ultraviolet ray sterilization method is adopted, and there is no need to add chemicals in the whole process, which can avoid the occurrence of secondary pollution. 5. Wide range of applications.
Description
技术领域 technical field
本发明属于水处理领域,涉及一种生物工艺的中水处理系统,具体的说为两级移动床生物膜反应器(MBBR)中水处理系统。The invention belongs to the field of water treatment, and relates to a reclaimed water treatment system of a biological process, specifically a two-stage moving bed biofilm reactor (MBBR) reclaimed water treatment system.
背景技术 Background technique
中水主要是指城市污水或生活污水经处理后达到一定的水质标准、可在一定范围内重复使用的非饮用的杂用水,其水质介于上水与下水水质之间。目前中国已经是世界第13个贫水国,水资源十分匾乏,有400多个城市处于缺水状态,其中一些地区已经实行了以限制供水的方式来提倡节水,这样也给人民群众带来了诸多不便。同时,大量的污水排放不仅造成了严重的环境污染,也极度浪费了宝贵的水资源。在水资源日益紧缺的今天,将处理后的水回用于绿化、冲洗车辆和冲洗厕所,是将污水资源化的一种有效形式,其应用前景非常广泛。Reclaimed water mainly refers to non-potable miscellaneous water that can be reused within a certain range after urban sewage or domestic sewage has been treated to meet certain water quality standards, and its water quality is between that of upper water and sewage. At present, China is already the 13th water-poor country in the world. Water resources are very scarce. More than 400 cities are in a state of water shortage. A lot of inconvenience came. At the same time, a large amount of sewage discharge not only causes serious environmental pollution, but also wastes precious water resources. In today's increasingly scarce water resources, returning the treated water to greening, flushing vehicles and flushing toilets is an effective form of recycling sewage, and its application prospects are very broad.
现有的一些中水处理工艺,其主要处理单元大多为混凝沉淀、气浮或接触氧化、膜生物反应器等,根据文献(工业安全与环保,2006,32[6],17)和文献(南京工程学院学报,2005,3[4],65)报道,其分别存在着抗冲击负荷能力差、易堵赛、出水水质不稳定等缺点,影响了中水处理的质量,同时运行维护费用高,设备能耗大等因素也制约了中水处理设备的应用。另一方面,其消毒方式主要为氯消毒法、臭氧消毒法、氯胺消毒法和二氧化氯消毒法,在加药消毒的同时存在着二次污染的风险。In some existing reclaimed water treatment processes, the main treatment units are mostly coagulation sedimentation, air flotation or contact oxidation, membrane bioreactor, etc., according to literature (Industrial Safety and Environmental Protection, 2006, 32[6], 17) and literature (Journal of Nanjing Institute of Engineering, 2005, 3[4], 65) reported that they have disadvantages such as poor resistance to impact load, easy to block, unstable effluent quality, etc., which affect the quality of reclaimed water treatment. At the same time, the operation and maintenance costs High energy consumption and other factors also restrict the application of reclaimed water treatment equipment. On the other hand, its disinfection methods are mainly chlorine disinfection, ozone disinfection, chloramine disinfection and chlorine dioxide disinfection, and there is a risk of secondary pollution while adding drugs for disinfection.
发明内容 Contents of the invention
本发明的目的是为了提供一种自动化程度高、占地面积小、维护方便、剩余污泥量少、出水水质稳定的中水处理工艺;工艺全程无需添加药剂,可避免二次污染的发生。The purpose of the present invention is to provide a reclaimed water treatment process with high degree of automation, small floor space, convenient maintenance, less residual sludge, and stable effluent quality; the whole process does not need to add chemicals, which can avoid the occurrence of secondary pollution.
一种两级移动床生物膜反应器中水处理系统,其特征是工艺流程为:生活污水经格栅1进入调节池2,经潜水泵8提升进入一级MBBR反应器3,在一级MBBR反应器3中,采用机械表面曝气10方式,使反应器处于好氧状态,投加多面空心球填料12,悬浮的活性污泥和填料上附着的生物膜共存,除了可以去除有机物和氨氮外,生物膜内部形成兼氧和厌氧层可同时脱氮除磷。出水为重力流进入二级MBBR反应器4,池内投加圆筒外螺旋13,采用转笼式曝气装置11,进一步去除有机物、氮、磷,并使本发明工艺具有较强的抗冲击负荷能力。二级MBBR反应器出水仍为重力流进入沉淀池5后溢流进入清水池6,再通过循环的紫外线消毒装置8去除病原微生物后进行回用,用于冲厕、景观用水等。工艺全程采用可编程PLC自动控制系统。A two-stage moving bed biofilm reactor water treatment system, characterized in that the process flow is as follows: domestic sewage enters the regulating
上述的二级MBBR反应器池体上部分是长方体,下部分是半圆柱体,底部设有排泥口,采用转笼式曝气装置,池内设有悬浮填料,填料上附有生物膜;一级和二级MBBR反应器的出水口均设有一个孔径尺寸稍小的网筛18,可截留载体和悬浮污泥;根据处理水质和水量的不同,二级MBBR反应器既可以单个使用,又可以采用2-5个并联的方式使用。The upper part of the above-mentioned secondary MBBR reactor pool body is a cuboid, the lower part is a semi-cylindrical body, the bottom is provided with a mud discharge port, and a rotating cage aeration device is used. The tank is provided with suspended fillers, and biofilms are attached to the fillers; The water outlets of the primary and secondary MBBR reactors are equipped with a
上述的清水池中设有潜水泵9,将处理后的中水循环的打入紫外线消毒装置中;紫外线消毒装置为几个并联的紫外线灯管。The above-mentioned clean water pool is provided with a submersible pump 9, which circulates treated reclaimed water into the ultraviolet disinfection device; the ultraviolet disinfection device is several parallel ultraviolet lamp tubes.
上述的可编程PLC自动控制系统可对液位的高低、潜水泵的运转、曝气时间、消毒装置进行自动控制。The above-mentioned programmable PLC automatic control system can automatically control the height of the liquid level, the operation of the submersible pump, the aeration time, and the disinfection device.
综上所述,与以往的中水处理工艺相比,本发明的优点在于:In summary, compared with the previous reclaimed water treatment process, the present invention has the following advantages:
1)中水处理效果好。本发明采用的移动床生物膜反应器(MBBR)内,悬浮的活性污泥和附着的生物膜共存,除了可以去除有机物和氨氮外,生物膜内部形成兼氧和厌氧层可同时脱氮除磷。另外,采用两级MBBR,使得本工艺具有较强的抗冲击负荷能力,出水水质稳定。1) The reclaimed water treatment effect is good. In the moving bed biofilm reactor (MBBR) adopted in the present invention, the suspended activated sludge and the attached biofilm coexist. In addition to removing organic matter and ammonia nitrogen, the formation of facultative and anaerobic layers inside the biofilm can simultaneously remove nitrogen and denitrification. phosphorus. In addition, the use of two-stage MBBR makes this process have a strong ability to resist impact loads, and the effluent water quality is stable.
2)运行管理简便。采用MBBR工艺,占地面积小,维护方便,剩余污泥量少;采用PLC自动控制系统,自动化程度高。2) Easy operation and management. The MBBR process is adopted, which occupies a small area, is easy to maintain, and has a small amount of residual sludge; it adopts a PLC automatic control system with a high degree of automation.
3)本发明采用机械曝气方式,能耗小,并能使载体呈现良好的流化状态,充氧性能好,无需单独设置鼓风机设备。3) The present invention adopts a mechanical aeration method, which has low energy consumption, can make the carrier present a good fluidization state, has good oxygenation performance, and does not need a separate blower device.
4)采用循环紫外线杀菌消毒方式,可以保证出水水质稳定。工艺全程无需添加药剂,可避免二次污染的发生。4) The cyclic ultraviolet sterilization and disinfection method can ensure the stability of the effluent water quality. There is no need to add chemicals in the whole process, which can avoid the occurrence of secondary pollution.
5)应用范围广,可根据处理要求和处理水量水质的不同,灵活改变MBBR反应器的串并联方式和规格大小。5) It has a wide range of applications, and can flexibly change the series-parallel connection mode and size of MBBR reactors according to the treatment requirements and the treatment water quality.
附图说明 Description of drawings
图1为本发明的工艺流程图Fig. 1 is a process flow diagram of the present invention
图2为本发明的工艺装置示意图Fig. 2 is a schematic diagram of a process device of the present invention
图3为本发明的一级MBBR反应器装置示意图Fig. 3 is a schematic diagram of a primary MBBR reactor device of the present invention
图4为本发明的二级MBBR反应器装置主视图Fig. 4 is the front view of the secondary MBBR reactor device of the present invention
图5为本发明的二级MBBR反应器装置侧视图Fig. 5 is the side view of secondary MBBR reactor device of the present invention
具体实施方式 Detailed ways
如图1、2所示,生活污水经格栅1进入调节池2,后经泵8提升顺序进入一级MBBR反应器3、二级MBBR反应器4,然后出水在沉淀池5溢流进入清水池6,再通过循环的紫外线消毒装置7后进行回用。根据处理水质和水量的不同,二级MBBR反应器4可采用多个并联的方式。As shown in Figures 1 and 2, the domestic sewage enters the
如图4、图5所示,二级MBBR反应器池体上部分是长方体,下部分是半圆柱体,底部设有排泥口,采用转笼式曝气装置14(转笼)、16(电机)、17(链条),池内设有悬浮填料15,填料上附有生物膜;反应器的出水口设有一个孔径尺寸稍小的网筛18可截留载体和悬浮污泥。As shown in Fig. 4 and Fig. 5, the upper part of the secondary MBBR reactor pool body is a cuboid, the lower part is a semi-cylindrical body, and the bottom is provided with a mud discharge port, and the rotating cage type aeration device 14 (rotating cage), 16 ( motor), 17 (chain), the pool is provided with suspended
实施举例Implementation example
如图2所示,生活污水经格栅1进入调节池2,经潜水泵8提升进入一级MBBR反应器3,在一级MBBR反应器3中,采用机械表面曝气10方式,使反应器处于好氧状态,投加多面空心球填料12,悬浮的活性污泥和填料上附着的生物膜共存,除了可以去除有机物和氨氮外,生物膜内部形成兼氧和厌氧层可同时脱氮除磷。出水为重力流进入二级MBBR反应器4,池内投加圆筒外螺旋13,采用转笼式曝气装置11,进一步去除有机物、氮、磷,并使本发明工艺具有较强的抗冲击负荷能力。出水仍为重力流进入沉淀池5后溢流进入清水池6,再通过循环的紫外线消毒装置8去除病原微生物后进行回用,用于冲厕、景观用水等。由于本发明工艺剩余污泥量小,所以无需进行污泥回流。经过以上工艺的处理,出水各项指标优于国家回用标准要求。As shown in Figure 2, the domestic sewage enters the
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Cited By (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101786770A (en) * | 2010-03-12 | 2010-07-28 | 浙江至美环境科技有限公司 | Oligodynamic moving bed sanitary sewage disposal system |
| CN101830607A (en) * | 2010-05-24 | 2010-09-15 | 哈尔滨工程大学 | Alternate two-stage aerobic membrane bioreactor |
| CN102329056A (en) * | 2011-09-08 | 2012-01-25 | 大连理工大学 | Marine sewage treatment integrated device on basis of biological moving beds |
| CN102358672A (en) * | 2011-09-22 | 2012-02-22 | 大连格兰清水环境工程有限公司 | Five-segment medical wastewater intelligent treatment machine and water feed control thereof |
| CN102583718A (en) * | 2012-03-09 | 2012-07-18 | 高晓华 | MBBR (Moving Bed Biofilm Reactor) packing material negative pressure and positive pressure conveying method and device |
| CN102020395B (en) * | 2009-09-11 | 2012-09-05 | 上海浩为环境工程有限公司 | Decentralized sewage treatment method |
| CN102976552A (en) * | 2012-11-19 | 2013-03-20 | 四川大学 | Method for deep treatment on difficultly-degraded organic nitrogen-containing industrial wastewater |
| CN102976553A (en) * | 2012-11-19 | 2013-03-20 | 四川大学 | Method for biological denitrogenation of nitrogen-containing organic industrial wastewater |
| CN103864211A (en) * | 2014-02-26 | 2014-06-18 | 上海大学 | Method for processing food processing wastewater by adopting facultative membrane bioreactor and facultative membrane bioreactor |
| CN104085988A (en) * | 2014-07-11 | 2014-10-08 | 北京科技大学 | Device and method for processing coking wastewater by adopting suspended filler-anaerobic membrane bioreactor |
| CN104496014A (en) * | 2014-12-23 | 2015-04-08 | 东北农业大学 | Biological treatment device of wastewater and cultivation method of aerobic granular sludge |
| CN105293835A (en) * | 2015-11-25 | 2016-02-03 | 中山市厚源电子科技有限公司 | A rural and township domestic sewage treatment system |
| CN107473379A (en) * | 2017-08-21 | 2017-12-15 | 武汉和尔环保科技有限公司 | A kind of movable container formula sewage-treatment plant |
| CN108862563A (en) * | 2018-06-25 | 2018-11-23 | 安徽恒宇环保设备制造股份有限公司 | A kind of MBBR technique for nanometer water process |
| CN109179657A (en) * | 2018-09-30 | 2019-01-11 | 诚通凯胜生态建设有限公司 | A kind of second level fluidized bed domestic sewage processing method and device |
| CN111170470A (en) * | 2020-01-15 | 2020-05-19 | 浙江永续环境工程有限公司 | Composite strain biological fluidized bed membrane reactor |
| CN112979100A (en) * | 2021-04-13 | 2021-06-18 | 天津市联合环保工程设计有限公司 | Traditional Chinese medicine wastewater treatment system difficult to biochemically treat and treatment method thereof |
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| CN102020395B (en) * | 2009-09-11 | 2012-09-05 | 上海浩为环境工程有限公司 | Decentralized sewage treatment method |
| CN101786770A (en) * | 2010-03-12 | 2010-07-28 | 浙江至美环境科技有限公司 | Oligodynamic moving bed sanitary sewage disposal system |
| CN101830607A (en) * | 2010-05-24 | 2010-09-15 | 哈尔滨工程大学 | Alternate two-stage aerobic membrane bioreactor |
| CN102329056A (en) * | 2011-09-08 | 2012-01-25 | 大连理工大学 | Marine sewage treatment integrated device on basis of biological moving beds |
| CN102358672A (en) * | 2011-09-22 | 2012-02-22 | 大连格兰清水环境工程有限公司 | Five-segment medical wastewater intelligent treatment machine and water feed control thereof |
| CN102358672B (en) * | 2011-09-22 | 2014-01-22 | 大连格兰清水环境工程有限公司 | Five-segment medical wastewater intelligent treatment machine and water feed control thereof |
| CN102583718A (en) * | 2012-03-09 | 2012-07-18 | 高晓华 | MBBR (Moving Bed Biofilm Reactor) packing material negative pressure and positive pressure conveying method and device |
| CN102976552A (en) * | 2012-11-19 | 2013-03-20 | 四川大学 | Method for deep treatment on difficultly-degraded organic nitrogen-containing industrial wastewater |
| CN102976553A (en) * | 2012-11-19 | 2013-03-20 | 四川大学 | Method for biological denitrogenation of nitrogen-containing organic industrial wastewater |
| CN103864211A (en) * | 2014-02-26 | 2014-06-18 | 上海大学 | Method for processing food processing wastewater by adopting facultative membrane bioreactor and facultative membrane bioreactor |
| CN104085988A (en) * | 2014-07-11 | 2014-10-08 | 北京科技大学 | Device and method for processing coking wastewater by adopting suspended filler-anaerobic membrane bioreactor |
| CN104496014A (en) * | 2014-12-23 | 2015-04-08 | 东北农业大学 | Biological treatment device of wastewater and cultivation method of aerobic granular sludge |
| CN105293835A (en) * | 2015-11-25 | 2016-02-03 | 中山市厚源电子科技有限公司 | A rural and township domestic sewage treatment system |
| CN107473379A (en) * | 2017-08-21 | 2017-12-15 | 武汉和尔环保科技有限公司 | A kind of movable container formula sewage-treatment plant |
| CN108862563A (en) * | 2018-06-25 | 2018-11-23 | 安徽恒宇环保设备制造股份有限公司 | A kind of MBBR technique for nanometer water process |
| CN109179657A (en) * | 2018-09-30 | 2019-01-11 | 诚通凯胜生态建设有限公司 | A kind of second level fluidized bed domestic sewage processing method and device |
| CN109179657B (en) * | 2018-09-30 | 2022-04-26 | 诚通凯胜生态建设有限公司 | Secondary fluidized bed domestic sewage treatment method and device |
| CN111170470A (en) * | 2020-01-15 | 2020-05-19 | 浙江永续环境工程有限公司 | Composite strain biological fluidized bed membrane reactor |
| CN111170470B (en) * | 2020-01-15 | 2021-09-28 | 浙江永续环境工程有限公司 | Composite strain biological fluidized bed membrane reactor |
| CN112979100A (en) * | 2021-04-13 | 2021-06-18 | 天津市联合环保工程设计有限公司 | Traditional Chinese medicine wastewater treatment system difficult to biochemically treat and treatment method thereof |
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