CN201990576U - A printing and dyeing wastewater treatment system - Google Patents
A printing and dyeing wastewater treatment system Download PDFInfo
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- CN201990576U CN201990576U CN2011200274249U CN201120027424U CN201990576U CN 201990576 U CN201990576 U CN 201990576U CN 2011200274249 U CN2011200274249 U CN 2011200274249U CN 201120027424 U CN201120027424 U CN 201120027424U CN 201990576 U CN201990576 U CN 201990576U
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Abstract
Description
技术领域technical field
本实用新型涉及工业废水多级处理技术领域,尤其涉及一种印染废水处理系统。The utility model relates to the technical field of multistage treatment of industrial waste water, in particular to a printing and dyeing waste water treatment system.
背景技术Background technique
印染行业是用水大户,也是排污大户,印染企业一般都建有污水处理系统,现有的污水处理系统主要采用物化预处理工艺,污水经处理达标后直接纳管排放,如图1所示,进入城市污水处理管网或直接排入地表水体。但由于现有系统未进行生化处理,氨氮超标,并考虑到水资源的日渐短缺和严重污染,因此无论从企业成本的角度还是从社会环保的发展角度来看,都有必要将印染废水进行深度处理后回用于生产。The printing and dyeing industry is a major user of water and sewage. Printing and dyeing enterprises generally have a sewage treatment system. The existing sewage treatment system mainly adopts physical and chemical pretreatment processes. After the sewage is treated up to the standard, it is directly discharged into the pipe, as shown in Figure 1. Urban sewage treatment pipe network or directly discharged into surface water bodies. However, since the existing system does not carry out biochemical treatment, ammonia nitrogen exceeds the standard, and considering the increasing shortage and serious pollution of water resources, it is necessary to carry out in-depth treatment of printing and dyeing wastewater no matter from the perspective of enterprise cost or social environmental protection. After processing, it is reused in production.
实用新型内容Utility model content
本实用新型就是为了解决上述现有技术存在的问题而提供一种印染废水处理系统,印染废水经深度处理后可大部分回用至生产车间,其余浓水则按照当地纳管排放标准可直接纳管排放。The utility model provides a printing and dyeing wastewater treatment system in order to solve the problems existing in the above-mentioned prior art. After advanced treatment, most of the printing and dyeing wastewater can be recycled to the production workshop, and the rest of the concentrated water can be directly collected according to the local pipe discharge standard. pipe discharge.
本实用新型的目的通过以下技术方案来实现:The purpose of this utility model is achieved through the following technical solutions:
一种印染废水处理系统,包括综合废水前处理系统、深度回用处理系统和污泥处理系统,所述污泥处理系统包括污泥池,所述综合废水前处理系统包括依次连接的调节池、混凝沉淀池、排水池、生物水解酸化池、好氧接触氧化池、辐流式二沉池和中间水池;所述深度回用处理系统包括依次连接的自动反洗式砂滤系统、加压式超滤膜系统、RO膜系统(RO反渗透集成膜处理系统)和RO回用水池;所述辐流式二沉池的污泥出口连通污泥池;所述中间水池的出水口连通自动反洗式砂滤系统。A printing and dyeing wastewater treatment system, including a comprehensive wastewater pre-treatment system, a deep reuse treatment system and a sludge treatment system, the sludge treatment system includes a sludge pool, and the comprehensive wastewater pre-treatment system includes sequentially connected adjustment pools, Coagulation sedimentation tank, drainage tank, biological hydrolysis acidification tank, aerobic contact oxidation tank, radial flow secondary sedimentation tank and intermediate water tank; the deep reuse treatment system includes automatic backwashing sand filter system connected in sequence, pressurized Ultrafiltration membrane system, RO membrane system (RO reverse osmosis integrated membrane treatment system) and RO reuse water tank; the sludge outlet of the radial flow secondary sedimentation tank is connected to the sludge tank; the outlet of the intermediate tank is connected to the automatic Backwash sand filter system.
所述调节池内前端设置格栅井。A grid well is arranged at the front end of the adjustment pool.
所述生物水解酸化池内设有防止污泥沉积的潜水混合搅拌系统。The biological hydrolysis and acidification tank is equipped with a submersible mixing system to prevent sludge deposition.
所述生物水解酸化池、好氧接触氧化池上设置废气收集处理系统。The biological hydrolysis acidification tank and the aerobic contact oxidation tank are equipped with a waste gas collection and treatment system.
与现有技术相比,本实用新型具有以下有益效果:Compared with the prior art, the utility model has the following beneficial effects:
1、采用更有针对性的(水解酸化)A/(好氧接触氧化)O工艺进行处理,解决氨氮超标问题;1. Adopt a more targeted (hydrolytic acidification) A/(aerobic contact oxidation) O process to solve the problem of excessive ammonia nitrogen;
2、深度回用水质要求特别是色度、总硬度等指标达到出水水质标准;2. The water quality requirements for deep reuse, especially the indicators such as chroma and total hardness, meet the water quality standards for effluent;
3、响应国家节能减排号召,具有较大的环保效益,深度回用处理系统回用水量大,可节省排污费和自来水费;通过深水回用可节省水资源,同时每年减排COD,而且氨氮能够达标排放;3. In response to the national call for energy conservation and emission reduction, it has great environmental benefits. The deep reuse treatment system reuses a large amount of water, which can save sewage discharge fees and tap water fees; through deep water reuse, water resources can be saved, and COD emissions can be reduced every year, and Ammonia nitrogen can discharge up to standard;
4、处理效率高,工程投资低,运行费用低,占地面积低,废水处理系统运行稳定,安全可靠,操作灵活;4. High treatment efficiency, low engineering investment, low operating cost, low floor space, stable operation of the wastewater treatment system, safety and reliability, and flexible operation;
5、妥善处理废水处理过程中产生的污泥,避免产生二次污染;5. Properly handle the sludge generated during the wastewater treatment process to avoid secondary pollution;
6、对废水处理过程中产生的废气、噪声污染等,采取有效的防治措施,减少其对周边环境的影响。6. Take effective prevention and control measures for waste gas and noise pollution generated during wastewater treatment to reduce their impact on the surrounding environment.
附图说明Description of drawings
图1为现有废水处理系统的流程示意图;Fig. 1 is the schematic flow sheet of existing wastewater treatment system;
图2为本实用新型一实施例的流程示意图。Fig. 2 is a schematic flow chart of an embodiment of the present invention.
具体实施方式Detailed ways
下面结合附图详细描述本实用新型。Describe the utility model in detail below in conjunction with accompanying drawing.
如图2所示,一种印染废水处理系统,分为三部分,包括综合废水前处理系统、深度回用处理系统和污泥处理系统。As shown in Figure 2, a printing and dyeing wastewater treatment system is divided into three parts, including a comprehensive wastewater pretreatment system, an advanced reuse treatment system and a sludge treatment system.
1、综合废水前处理系统1. Comprehensive wastewater pre-treatment system
综合废水前处理系统首先通过pH调节和混凝沉淀进行预处理,然后采用“水解酸化和生物接触氧化法”二级生化组合处理工艺,将废水处理到一级标准(COD≦100mg/L),最后二沉池出水进入深度处理系统。The comprehensive wastewater pre-treatment system first pre-treats through pH adjustment and coagulation sedimentation, and then adopts the secondary biochemical combined treatment process of "hydrolytic acidification and biological contact oxidation" to treat the wastewater to the primary standard (COD≦100mg/L), Finally, the effluent from the secondary sedimentation tank enters the advanced treatment system.
综合废水前处理系统包括依次连接的调节池1、混凝沉淀池2、排水池3、生物水解酸化池4、好氧接触氧化池5、辐流式二沉池6和中间水池7。The comprehensive wastewater pretreatment system includes a regulating tank 1, a coagulation sedimentation tank 2, a
综合废水经收集后首先进入调节池,池内前端设置格栅井8,去除纤维、垃圾等物质。调节池有利于均匀水质水量,保证后续处理稳定性。均匀水质水量后的废水进行pH调节,通过投加混凝剂、絮凝剂等进行混凝反应,去除部分有机物,降低后续生化处理负荷和难度,设置平流式初沉池,进行沉淀作用。After the comprehensive wastewater is collected, it first enters the regulating pool, and the front end of the pool is provided with a grid well 8 to remove fibers, garbage and other substances. The regulating pool is conducive to uniform water quality and quantity, and ensures the stability of subsequent treatment. After uniform water quality and quantity, the pH of the wastewater is adjusted, and the coagulation reaction is carried out by adding coagulants, flocculants, etc. to remove some organic matter, reduce the load and difficulty of subsequent biochemical treatment, and set up an advection primary sedimentation tank for sedimentation.
预处理后的废水由排水池打入生物水解酸化池,生物水解酸化池中设接触填料,以附着异养性兼性微生物为主,达到水解酸化阶段,并设有潜水混合搅拌系统,防止污泥沉积,也有利于废水与污泥的充分接触反应。在兼氧菌作用下,使废水中的高分子和复杂的有机物降解为小分子、简单的有机物,提高废水的可生化性,改善后续好氧生化处理条件,并对染料也具有较好的脱色作用。同时,将后续好氧混合液及二沉池污泥回流,在兼氧状态下(溶解氧小于0.5mg/L)进行反硝化生物脱氮作用,降低废水中的氨氮含量。The pretreated wastewater is poured into the biological hydrolysis and acidification tank from the drainage tank. The biological hydrolysis and acidification tank is equipped with contact fillers, which are mainly attached to heterotrophic facultative microorganisms to reach the stage of hydrolysis and acidification. A submersible mixing system is also installed to prevent sludge Sedimentation is also conducive to the full contact reaction of wastewater and sludge. Under the action of facultative bacteria, the macromolecule and complex organic matter in the wastewater are degraded into small molecules and simple organic matter, which improves the biodegradability of the wastewater, improves the subsequent aerobic biochemical treatment conditions, and has good decolorization of dyes effect. At the same time, the subsequent aerobic mixed liquid and the sludge of the secondary sedimentation tank are returned to carry out denitrification biological denitrification in a facultative state (dissolved oxygen is less than 0.5mg/L) to reduce the ammonia nitrogen content in the wastewater.
水解酸化出水接入好氧接触氧化池,通过鼓风机进行曝气(溶解氧在1-2mg/L左右),利用池内处于悬浮状态下的微生物(好氧菌)对废水中的有机污染物进行吸附、分解,从而达到去除有机污染物、净化水质的目的。好氧池设置涡街流量计,可根据变频控制风量大小,可节省运行费用。好氧接触氧化池出水流入辐流式二沉池进行泥水分离,其出水自流至中间水池待深度回用处理。The effluent from hydrolysis and acidification is connected to the aerobic contact oxidation tank, aerated by a blower (dissolved oxygen is about 1-2 mg/L), and the microorganisms (aerobic bacteria) in a suspended state in the tank are used to adsorb organic pollutants in the wastewater , Decomposition, so as to achieve the purpose of removing organic pollutants and purifying water quality. The aerobic pool is equipped with a vortex flowmeter, which can control the air volume according to the frequency conversion, which can save operating costs. The effluent from the aerobic contact oxidation tank flows into the radial flow secondary settling tank for mud-water separation, and the effluent flows to the intermediate pool by itself for deep reuse treatment.
在综合废水前处理过程中,会产生废气、噪声等污染,对周边环境有较大的影响,因此增加污水处理系统废气防治和污水处理系统噪声污染的防治。In the process of comprehensive wastewater pre-treatment, pollution such as waste gas and noise will be generated, which will have a great impact on the surrounding environment. Therefore, the prevention and control of waste gas in the sewage treatment system and the prevention and control of noise pollution in the sewage treatment system will be added.
在污水处理系统运行过程中,由于微生物的新陈代谢作用会产生一定量的异味废气,污染周边大气环境,因此,对生化反应池(生物水解酸化池、好氧接触氧化池)加盖板,增设废气收集处理系统9,对生化系统中产生的异味气体采取集中收集后排放,以减少对周边大气环境的污染。During the operation of the sewage treatment system, due to the metabolism of microorganisms, a certain amount of odorous waste gas will be generated, which will pollute the surrounding atmospheric environment. The collection and
生化处理系统运行过程中,需要鼓风机不断提供空气,产生较大的噪声污染,影响周边居住的生活环境,因此,对鼓风机加隔音罩,对风机房采用隔音墙、隔音窗等措施,降低噪音影响。During the operation of the biochemical treatment system, the air blower is required to continuously provide air, which generates large noise pollution and affects the living environment of the surrounding residents. Therefore, soundproof covers are added to the blower, and measures such as soundproof walls and soundproof windows are used for the fan room to reduce the impact of noise .
2、深度回用处理系统2. Deep reuse processing system
中间水池的废水继续进行深度回用处理,深度回用处理系统采用自动清洗砂滤及“加压式UF超滤膜和反渗透RO集成膜”的双膜处理工艺技术进行深度回用处理,使回用水达到高级回用水水质要求。深度处理回用水回用至生产车间,其余深度膜分离浓水按照三级标准纳管排放。若排放标准提高,则膜分离浓水可另增处理设施处理。The wastewater in the middle pool continues to be treated in depth. The deep reuse treatment system adopts the double-membrane treatment technology of automatic cleaning sand filter and "pressurized UF ultrafiltration membrane and reverse osmosis RO integrated membrane" for deep reuse treatment. Recycled water meets the water quality requirements for high-grade reused water. The advanced treatment water is reused to the production workshop, and the rest of the deep membrane separation concentrated water is discharged according to the three-level standard. If the discharge standard is raised, the concentrated water from membrane separation can be treated by additional treatment facilities.
深度回用处理系统包括依次连接的自动反洗式砂滤系统10、加压式超滤膜系统11、RO膜系统(RO反渗透集成膜处理系统)12和RO回用水池13;The deep reuse treatment system includes an automatic backwash
深度回用处理系统是以生化二沉池出水为原水,由中间水池经过泵提升进入深度处理系统,中间水池的出水口连通自动反洗式砂滤系统。为保证后续双膜系统的稳定运行,在前段增加自动反洗式砂滤系统,进一步去除废水中的悬浮物、胶体等物质,其出水再通过精密过滤进入加压式超滤膜系统去除废水中的细菌、病毒、有机物及色度等,提高后续RO反渗透集成膜处理系统进水水质,延长其使用寿命,保证整体深度回用工艺运行稳定性。超滤膜系统出水进入RO反渗透集成膜系统,通过RO膜的浓缩、截留能力脱盐、纯化出水水质,供染色、印花用水水质要求较高的工段回用。膜系统浓液达到三级纳管排放标准可直接纳管排放。若排放标准提高,则膜分离浓水可另增处理设施处理。The advanced reuse treatment system uses the effluent of the biochemical secondary settling tank as raw water, which is lifted by the intermediate pool into the advanced treatment system through a pump, and the outlet of the intermediate pool is connected to the automatic backwashing sand filter system. In order to ensure the stable operation of the subsequent double-membrane system, an automatic backwash sand filter system is added in the front section to further remove suspended solids, colloids and other substances in the wastewater, and the effluent is then filtered into the pressurized ultrafiltration membrane system to remove the wastewater. bacteria, viruses, organic matter and chroma, etc., improve the water quality of the subsequent RO reverse osmosis integrated membrane treatment system, prolong its service life, and ensure the stability of the overall deep recycling process. The effluent from the ultrafiltration membrane system enters the RO reverse osmosis integrated membrane system. Through the concentration and interception capacity of the RO membrane, the desalination and purification of the effluent water quality can be reused for dyeing and printing water quality requirements. Membrane system dope can be discharged directly through nanotubes if it reaches the third-level nanotube discharge standard. If the discharge standard is raised, the concentrated water from membrane separation can be treated by additional treatment facilities.
3、污泥处理系统3. Sludge treatment system
污泥处理系统包括污泥池14,辐流式二沉池的污泥出口连通污泥池,辐流式二沉池产生污泥均接入污泥池,减量后的污泥通过砂浆泵作用送入带式浓缩一体压滤机进行脱水处理,处理后的污泥外运处理,滤液接入水解酸化池,避免产生二次污染。The sludge treatment system includes a
以上公开的仅为本申请的几个具体实施例,但本申请并非局限于此,任何本领域的技术人员能思之的变化,都应落在本申请的保护范围内。The above disclosures are only a few specific embodiments of the present application, but the present application is not limited thereto, and any changes conceivable by those skilled in the art shall fall within the protection scope of the present application.
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102633404A (en) * | 2012-03-16 | 2012-08-15 | 山东天畅环保工程有限公司 | Treatment process for comprehensive wastewater |
| CN103011529A (en) * | 2012-12-07 | 2013-04-03 | 常州大学 | Industrial wastewater treatment technology |
| CN103523988A (en) * | 2013-09-27 | 2014-01-22 | 昆山培新服装有限公司 | Printing and dyeing wastewater treatment process |
| CN104591478A (en) * | 2014-12-22 | 2015-05-06 | 福建宇邦纺织科技有限公司 | Method for recycling full chemical fiber dyeing wastewater after treatment |
| CN105110560A (en) * | 2015-08-27 | 2015-12-02 | 常州大学 | Zero-discharge dyeing wastewater treatment system |
| CN106245259A (en) * | 2016-08-27 | 2016-12-21 | 杭州大地印染有限公司 | Knitting fabric environment-friendly production process and cleaning system thereof |
| CN108911420A (en) * | 2018-08-17 | 2018-11-30 | 广东溢达纺织有限公司 | The system and technique of a kind of processing of laundrywastes and zero-emission |
| WO2019196057A1 (en) * | 2018-04-12 | 2019-10-17 | 苏州荣能环保科技有限公司 | Environmentally friendly mixed wastewater treatment system |
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2011
- 2011-01-27 CN CN2011200274249U patent/CN201990576U/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102633404A (en) * | 2012-03-16 | 2012-08-15 | 山东天畅环保工程有限公司 | Treatment process for comprehensive wastewater |
| CN103011529A (en) * | 2012-12-07 | 2013-04-03 | 常州大学 | Industrial wastewater treatment technology |
| CN103523988A (en) * | 2013-09-27 | 2014-01-22 | 昆山培新服装有限公司 | Printing and dyeing wastewater treatment process |
| CN104591478A (en) * | 2014-12-22 | 2015-05-06 | 福建宇邦纺织科技有限公司 | Method for recycling full chemical fiber dyeing wastewater after treatment |
| CN105110560A (en) * | 2015-08-27 | 2015-12-02 | 常州大学 | Zero-discharge dyeing wastewater treatment system |
| CN106245259A (en) * | 2016-08-27 | 2016-12-21 | 杭州大地印染有限公司 | Knitting fabric environment-friendly production process and cleaning system thereof |
| WO2019196057A1 (en) * | 2018-04-12 | 2019-10-17 | 苏州荣能环保科技有限公司 | Environmentally friendly mixed wastewater treatment system |
| CN108911420A (en) * | 2018-08-17 | 2018-11-30 | 广东溢达纺织有限公司 | The system and technique of a kind of processing of laundrywastes and zero-emission |
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