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CN101525202A - Advanced dyeing wastewater treatment and reclaimed water reuse system and method thereof - Google Patents

Advanced dyeing wastewater treatment and reclaimed water reuse system and method thereof Download PDF

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Publication number
CN101525202A
CN101525202A CN200910049268A CN200910049268A CN101525202A CN 101525202 A CN101525202 A CN 101525202A CN 200910049268 A CN200910049268 A CN 200910049268A CN 200910049268 A CN200910049268 A CN 200910049268A CN 101525202 A CN101525202 A CN 101525202A
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sludge
wastewater
water
printing
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黄兴泉
张明友
蔡再生
俞建勇
赵亚萍
徐丽慧
陈玉梅
孙洁
眭均平
陈小红
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Donghua University
Shanghai Academy of Environmental Sciences
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CHANGZHOU DONGXIA PRINTING AND DYEING Co Ltd
Donghua University
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Abstract

本发明涉及一种印染废水深度处理与中水回用系统及方法,系统由调节池(2),混凝池(3),预沉池(4),酸化水解池(5),深井(6),脱气池(7),二沉池(8),生物活性炭池(9),污泥浓缩池(10),污泥脱水池(11),过滤池(12),臭氧氧化池(13)组成;方法:废水经调节池,混凝池,预沉池后,污泥回入混凝池,多余污泥排入污泥浓缩池,澄清水流入酸化水解池,再进入深井曝气池,入二沉池;达标排放,否则流入生物活性炭池,经处理用于生产。本发明工艺简单,运行费用低且稳定可靠,操作方便,可实现自动化控制;废水处理达标后排放大部分回用于生产,不仅减少污染物的排放量,还能消除废水对环境的污染,保护环境。

Figure 200910049268

The invention relates to a system and method for advanced treatment of printing and dyeing wastewater and reuse of reclaimed water. The system consists of a regulating tank (2), a coagulation tank (3), a pre-sedimentation tank (4), an acidification hydrolysis tank (5), and a deep well (6 ), degassing tank (7), secondary settling tank (8), biological activated carbon tank (9), sludge thickening tank (10), sludge dewatering tank (11), filter tank (12), ozone oxidation tank (13 ) composition; method: after the wastewater passes through the regulating tank, the coagulation tank and the pre-sedimentation tank, the sludge returns to the coagulation tank, the excess sludge is discharged into the sludge concentration tank, the clarified water flows into the acidification hydrolysis tank, and then enters the deep well aeration tank , enter the secondary sedimentation tank; discharge up to the standard, otherwise flow into the biological activated carbon pool, and be used for production after treatment. The invention has the advantages of simple process, low operating cost, stable reliability, convenient operation, and automatic control; most of the discharged waste water is reused in production after the waste water treatment reaches the standard, which not only reduces the discharge of pollutants, but also eliminates the pollution of waste water to the environment and protects the environment. environment.

Figure 200910049268

Description

一种印染废水深度处理与中水回用系统及方法 A system and method for advanced treatment of printing and dyeing wastewater and reuse of reclaimed water

技术领域 technical field

本发明属纺织染整中水处理领域,特别是涉及一种印染废水深度处理与中水回用系统及方法。The invention belongs to the field of reclaimed water treatment in textile dyeing and finishing, in particular to a system and method for advanced treatment of printing and dyeing wastewater and reuse of reclaimed water.

背景技术 Background technique

印染行业是纺织工业的重要组成部分,既是提升产品质量、提高产品附加值的关键行业,又是耗水、耗能、排污较大的行业。近年来,在纺织工业稳步快速增长的拉动下,印染行业得到了快速发展,与此同时也越来越受到资源、环境的制约。印染废水主要来源于前处理、染色印花两个工序,具有水量大、有机污染物含量高(COD值高)、色度深、碱性大、水质变化大等特点,属难处理的工业废水。此外,纺织品的染整加工还要使用大量的酸、碱、盐、表面活性剂及各种功能性整理剂等,这些化学品势必要造成一定的环境污染,因此,染整业被称为“能耗大户(用水大户)、污染大户”,据不完全统计,我国印染废水排放量约为每天3×106m3~4×106m3,约占整个工业废水的35%,且回用率不到10%,90%以上作废水排放。由此而造成的生态及经济损失是不可估量的。此外,在印染行业分布地区,特别是在水资源比较短缺的地方,由于供应的新鲜用水总量受到限制,使印染企业产量的增加或生产规模的扩大受到制约,企业发展受到限制,因此印染行业的节能减排工作迫在眉睫,必须实现开源节流来满足生产过程中增加的用水量。The printing and dyeing industry is an important part of the textile industry. It is not only a key industry to improve product quality and increase product added value, but also an industry that consumes a lot of water, energy, and pollutants. In recent years, driven by the steady and rapid growth of the textile industry, the printing and dyeing industry has developed rapidly, but at the same time it is increasingly constrained by resources and the environment. Printing and dyeing wastewater mainly comes from the two processes of pretreatment and dyeing and printing. It has the characteristics of large water volume, high content of organic pollutants (high COD value), deep color, high alkalinity, and large changes in water quality. It is a difficult-to-treat industrial wastewater. In addition, the dyeing and finishing of textiles also uses a large amount of acids, alkalis, salts, surfactants and various functional finishing agents. These chemicals are bound to cause certain environmental pollution. Therefore, the dyeing and finishing industry is called " According to incomplete statistics, the discharge of printing and dyeing wastewater in China is about 3×10 6 m 3 to 4×10 6 m 3 per day, accounting for about 35% of the entire industrial wastewater. The utilization rate is less than 10%, and more than 90% is discharged as waste water. The resulting ecological and economic losses are immeasurable. In addition, in the areas where the printing and dyeing industry is distributed, especially in places where water resources are relatively scarce, due to the limitation of the total amount of fresh water supplied, the increase in output or the expansion of production scale of printing and dyeing enterprises is restricted, and the development of enterprises is restricted. Therefore, the printing and dyeing industry The work of energy saving and emission reduction is imminent, and it is necessary to increase revenue and reduce expenditure to meet the increased water consumption in the production process.

目前,印染废水深度处理及回用技术主要有以下几种:At present, the advanced treatment and reuse technologies of printing and dyeing wastewater mainly include the following types:

(1)吸附法。活性炭吸附法对去除水中溶解性有机物非常有效,但它不能去除水中的胶体和疏水性染料,并且它只对阳离子染料、直接染料、酸性染料、活性染料等水溶性染料具有较好的吸附性能。高岭土吸附剂能有效地吸附废水中的黄色直接染料。此外,国内也应用活性硅藻土和煤渣处理传统印染工艺废水,费用较低,脱色效果较好,其缺点是泥渣产生量大,且进一步处理难度大。(1) Adsorption method. Activated carbon adsorption is very effective for removing dissolved organic matter in water, but it cannot remove colloids and hydrophobic dyes in water, and it only has good adsorption properties for water-soluble dyes such as cationic dyes, direct dyes, acid dyes, and reactive dyes. Kaolin adsorbent can effectively adsorb yellow direct dye in wastewater. In addition, activated diatomaceous earth and coal cinders are also used in China to treat traditional printing and dyeing process wastewater. The cost is low and the decolorization effect is good. The disadvantage is that the amount of sludge generated is large and the further treatment is difficult.

(2)氧化法。臭氧氧化法在国外应用较多,对多数染料能获得良好的脱色效果,但对硫化、还原、涂料等不溶于水的染料脱色效果较差,该法脱色效果好,但耗电多,大规模推广应用有一定困难。光氧化法处理印染废水脱色效率较高,但设备投资和电耗还有待进一步降低。采用光敏化半导体为催化剂处理有机废水是近年来国内外研究的热点。光敏化氧化大多采用光敏化半导体TiO2催化氧化降解废水,是废水处理的新技术。(2) Oxidation method. The ozone oxidation method is widely used in foreign countries. It can obtain good decolorization effect on most dyes, but it has poor decolorization effect on water-insoluble dyes such as vulcanization, reduction and paint. It is difficult to promote the application. Photooxidation treatment of printing and dyeing wastewater has a high decolorization efficiency, but equipment investment and power consumption need to be further reduced. The use of photosensitized semiconductors as catalysts to treat organic wastewater has become a hot research topic at home and abroad in recent years. Photo-sensitized oxidation mostly uses photo-sensitized semiconductor TiO 2 to catalyze oxidation to degrade wastewater, which is a new technology for wastewater treatment.

(3)生物法。生物技术不仅应用于印染废水的二级处理中,还可以作为印染废水的深度处理技术。针对二级出水中的污染物生化性不高,大都难生物降解的特点,开发出了许多采用生物强化处理技术的新型反应器,以进一步降低二级出水中的COD和色度。主要有生物活性炭法、曝气生物滤池等。(3) Biological method. Biotechnology is not only used in the secondary treatment of printing and dyeing wastewater, but also can be used as an advanced treatment technology for printing and dyeing wastewater. In view of the low biochemical properties of the pollutants in the secondary effluent and most of them are difficult to biodegrade, many new reactors using bio-enhanced treatment technology have been developed to further reduce the COD and chroma in the secondary effluent. There are mainly biological activated carbon method, biological aerated filter and so on.

(4)膜法。将不同的膜分离技术(如微滤、超滤、纳滤、反渗透等)相结合,或膜分离技术与其他技术(如膜生物反应器)相结合,是目前印染废水深度处理的一个方向。膜法的废水再利用主要包括“超滤膜+反渗透膜”的工艺流程,超滤是以压力为驱动的膜分离过程,它能够将颗粒物质从流体及溶解组分中分离出来。应用在印染废水的再处理流程中,超滤膜除对有机物及色度有一定的去除作用外,最主要的作用是去除可能污堵反渗透膜的胶体、细菌、病毒等杂质,延长反渗透膜的清洗周期和寿命,降低总体运行成本;反渗透膜可去除98%的盐离子,完全去除硬度,同时对COD、色度也具有极高的去除作用,从而确保回用水水质。(4) Membrane method. Combining different membrane separation technologies (such as microfiltration, ultrafiltration, nanofiltration, reverse osmosis, etc.), or combining membrane separation technologies with other technologies (such as membrane bioreactors), is currently a direction for the advanced treatment of printing and dyeing wastewater . Membrane wastewater reuse mainly includes the process of "ultrafiltration membrane + reverse osmosis membrane". Ultrafiltration is a membrane separation process driven by pressure, which can separate particulate matter from fluid and dissolved components. Applied in the retreatment process of printing and dyeing wastewater, the ultrafiltration membrane not only has a certain removal effect on organic matter and chroma, but also removes impurities such as colloids, bacteria, and viruses that may foul the reverse osmosis membrane, and prolongs the life of reverse osmosis. The cleaning cycle and life of the membrane reduce the overall operating cost; the reverse osmosis membrane can remove 98% of salt ions, completely remove hardness, and also have a very high removal effect on COD and chroma, thereby ensuring the quality of reused water.

由于不同织物、不同印染加工工艺排放的废水水质有很大差异,应对废水组分、水质特征进行分析,通过技术经济比较,选择最优化的处理技术。单一的处理工艺很难将废水处理达标排放,需采多工艺联合。印染废水回用还存在一些问题,如:废水大量回用对生产及污水处理系统会带来一系列问题,主要包括有机污染物和无机盐的积累,使污水处理系统无法运行,回用率过高,且不进行脱盐处理,也会使得生产和污水处理无法进行。一般地,深度处理费用比常规处理高,对于用水量较小的工厂不太合适,对于用水量大的工厂就显示出其优势,并能为企业带来经济效益和环境效益。随着新型化学纤维、仿真丝、印染整理技术的发展,聚乙烯醇、染料、新型助剂等难生物降解有机物大量进人印染废水,使废水的可生化性进一步降低,这些因素也影响到废水的回用。Due to the great difference in the quality of wastewater discharged from different fabrics and different printing and dyeing processes, the components and water quality characteristics of wastewater should be analyzed, and the optimal treatment technology should be selected through technical and economic comparison. It is difficult for a single treatment process to treat wastewater up to standard discharge, and a combination of multiple processes is required. There are still some problems in the reuse of printing and dyeing wastewater, such as: a large amount of wastewater reuse will bring a series of problems to the production and sewage treatment system, mainly including the accumulation of organic pollutants and inorganic salts, making the sewage treatment system unable to operate, and the reuse rate is too high High, and without desalination treatment, it will also make production and sewage treatment impossible. Generally, the cost of advanced treatment is higher than that of conventional treatment. It is not suitable for factories with small water consumption, but it shows its advantages for factories with large water consumption, and can bring economic and environmental benefits to enterprises. With the development of new chemical fiber, imitation silk, printing and dyeing finishing technology, polyvinyl alcohol, dyes, new additives and other refractory organic substances enter printing and dyeing wastewater in large quantities, which further reduces the biodegradability of wastewater. These factors also affect wastewater reuse.

发明内容 Contents of the invention

本发明所要解决的技术问题是提供一种印染废水深度处理与中水回用系统及方法,该方法工艺简单,运行费用低且稳定可靠,操作方便,可实现自动化控制;废水处理达标后排放大部分回用于生产,这样不仅减少污染物的排放量,还能消除废水对环境的污染,保护环境。The technical problem to be solved by the present invention is to provide a system and method for advanced treatment of printing and dyeing wastewater and reclaimed water reuse. Part of it is reused for production, which not only reduces the discharge of pollutants, but also eliminates the pollution of waste water to the environment and protects the environment.

本发明的一种印染废水深度处理与中水回用方法,包括:A method for advanced treatment of printing and dyeing wastewater and reuse of reclaimed water according to the present invention, comprising:

印染废水先经格栅除渣机除去废水中直径大于1.5mm的悬浮物后流入调节池,进行废水水质水量调节,然后用污水泵将废水提升入混凝池,并在泵前投加无机混凝剂硫酸亚铁,通过水泵叶轮搅拌进行混凝反应,经预沉池沉淀分离,沉淀污泥大部分回入混凝池,多余污泥排入污泥浓缩池,浓缩脱水后外运,澄清水流入酸化水解池,与回流的活性污泥混合,在缺氧条件下,活性污泥中的兼氧微生物对大分子有机物进行酸化水解作用,将大分子难以生化物质降解为小分子可生化物质,提高废水的可生化性,酸化水解后混合液自流入深井曝气池,对废水进行好氧生物处理;由于深井的深度大,静水压力高,溶解氧浓度大,可快速、高效地将废水中的有机物氧化降解为CO2、H2O,化有害为无害,深井处理液自流入脱气池脱除粘附在活性污泥上的微气泡后,入二沉池进行固液分离,沉淀污泥大部分回入深井、酸化水解池,多余污泥排入污泥浓缩池,浓缩脱水后泥并外运;二沉池的澄清水达标就直接排放,否则与需回用水一道自流入生物活性碳池,在好氧条件下,利用活性炭与微生物的降解作用,去除废水中的有机物,处理水再经过滤、臭氧氧化、消毒灭菌,进一步氧化去除残剩的有害物质后,入回用水池,用加压泵送车间回用于生产。Printing and dyeing wastewater first passes through the grid deslagging machine to remove suspended solids with a diameter greater than 1.5mm in the wastewater, and then flows into the regulating tank to adjust the quality and quantity of the wastewater. Then the wastewater is lifted into the coagulation tank with a sewage pump, and inorganic mixing The coagulant ferrous sulfate is stirred by the impeller of the water pump to carry out the coagulation reaction, and is precipitated and separated by the pre-sedimentation tank. Most of the settled sludge is returned to the coagulation tank, and the excess sludge is discharged into the sludge thickening tank. After concentration and dehydration, it is transported outside and clarified The water flows into the acidification hydrolysis tank and mixes with the returning activated sludge. Under anoxic conditions, the facultative microorganisms in the activated sludge acidify and hydrolyze the macromolecular organic matter, and degrade the macromolecular difficult-to-biochemical substances into small molecular biochemical substances. , to improve the biodegradability of wastewater, after acidification and hydrolysis, the mixed liquid flows into the deep well aeration tank, and aerobic biological treatment is carried out on the wastewater; due to the deep well depth, high hydrostatic pressure, and high dissolved oxygen concentration, the wastewater can be quickly and efficiently The organic matter in the sludge is oxidized and degraded into CO 2 and H 2 O, turning harmful into harmless. After the deep well treatment fluid flows into the degassing tank to remove the microbubbles adhering to the activated sludge, it enters the secondary sedimentation tank for solid-liquid separation. Most of the settled sludge is returned to the deep well and the acidification hydrolysis tank, and the excess sludge is discharged into the sludge concentration tank, and the sludge is concentrated and dehydrated and transported outside; the clarified water in the secondary settling tank is discharged directly if it meets the standard, otherwise it will flow in with the reused water The bioactive carbon pool, under aerobic conditions, utilizes the degradation effect of activated carbon and microorganisms to remove organic matter in wastewater, and the treated water is filtered, ozone oxidized, sterilized, and further oxidized to remove residual harmful substances before entering the recycling Use the pool, and use the pressurized pump to send the workshop back to production.

所述的无机混凝剂为硫酸亚铁液(来源于常州钢铁厂),每升废水用量为8-10mL。The inorganic coagulant is liquid ferrous sulfate (from Changzhou Iron and Steel Works), and the dosage per liter of waste water is 8-10mL.

本发明的废水处理工艺流程如下:Wastewater treatment technological process of the present invention is as follows:

Figure A20091004926800061
Figure A20091004926800061

各工艺设备作用如下:The functions of each process equipment are as follows:

1.格栅除渣机;1. Grid slag remover;

2.调节池:废水水质水量调节;2. Regulating pool: wastewater water quality and water regulation;

3.混凝池:池内安装混凝搅拌机,用于废水加药混凝,在快速搅拌下,加入混凝剂,使之与废水进行混凝反应;3. Coagulation pool: a coagulation mixer is installed in the pool for the coagulation of waste water, and the coagulant is added under rapid stirring to make it coagulate with the waste water;

4.预沉池:用于混凝后废水的固液分离;4. Pre-sedimentation tank: used for solid-liquid separation of wastewater after coagulation;

5.酸化水解池:用于对预处理后的废水及进行微生物酸化水解处理,池内安装曝气管,用少量曝气法使废水和活性污泥的混合,并维持池内溶解氧0.2mg/L以下,使兼氧微生物在缺氧条件下将大分子有机物降解为小分子有机物,提供废水的可生化性;5. Acidification and hydrolysis pool: used for pretreated wastewater and microbial acidification and hydrolysis treatment. Aeration pipes are installed in the pool, and a small amount of aeration is used to mix wastewater and activated sludge, and maintain dissolved oxygen in the pool at 0.2mg/L Below, make facultative microorganisms degrade macromolecular organic matter into small molecular organic matter under anoxic conditions, and provide biodegradability of wastewater;

6.深井顶槽:用于脱除深井循环液中含氧极低的废气;6. Deep well top tank: used to remove waste gas with extremely low oxygen content in deep well circulating fluid;

附属设备为深井:为同心圆钢结构,采用气体循环运行方式,供给的压缩空气既作为深井的运行动力,又为生物作用提供充足的高浓度的溶解氧。深井是占地少、处理效果好、运行费用低、快速、高效的最佳活性污泥法。The auxiliary equipment is a deep well: it is a concentric circular steel structure and adopts the gas circulation operation mode. The compressed air supplied is not only used as the operating power of the deep well, but also provides sufficient high-concentration dissolved oxygen for biological functions. Deep well is the best activated sludge method with less land occupation, good treatment effect, low operating cost, fast and efficient.

7.脱气池:由于深井深达百米,静水压力为1MPa,通入深井的压缩空气全部溶入水中,循环到达深井顶槽后,循环液中含大量的过饱和空气,会释放出大量微气泡,粘附到活性污泥上,使活性污泥上浮。采用曝气法脱除粘附在污泥上的微气泡,便于污泥在二沉池进行重力法固液分离;7. Degassing tank: Since the deep well is as deep as 100 meters and the hydrostatic pressure is 1MPa, all the compressed air that passes into the deep well is dissolved in the water, and after the circulation reaches the top groove of the deep well, the circulating fluid contains a large amount of supersaturated air, which will release a large amount of air. Micro-bubbles adhere to the activated sludge and make the activated sludge float up. The aeration method is used to remove the micro-bubbles adhering to the sludge, which facilitates the solid-liquid separation of the sludge in the secondary sedimentation tank by gravity method;

8.二沉池:为辐射式结构的沉淀池,用于深井处理液的固液分离8. Secondary sedimentation tank: a sedimentation tank with radial structure, used for solid-liquid separation of deep well treatment fluid

附属结构:A.池内安装中心传动刮泥,用于收集沉淀污泥;B.污泥回流泵,用于将二沉池的沉淀污泥回入深井、酸化水解池和污泥浓缩池;Auxiliary structure: A. A central drive scraper is installed in the pool to collect sedimentation sludge; B. Sludge return pump is used to return the sedimentation sludge from the secondary sedimentation tank to the deep well, acidification hydrolysis tank and sludge concentration tank;

9.生物活性碳池:废水在池内停留3-5小时,池底部有微孔曝气器,池中部布置厚2米的活性碳滤层,处理水中残剩有机物通过活性碳滤层时被活性碳吸附,富集在活性碳上,活性碳上同时长满微生物,在有溶解氧的情况下,在微生物与活性碳的协同作用下,废水中的有机物能被高效地去除,提高去除效果;9. Biologically activated carbon pool: The wastewater stays in the pool for 3-5 hours. There is a microporous aerator at the bottom of the pool, and an activated carbon filter layer with a thickness of 2 meters is arranged in the middle of the pool. The residual organic matter in the treated water is activated when it passes through the activated carbon filter layer. Carbon adsorption, enriched on the activated carbon, and the activated carbon is covered with microorganisms at the same time. In the presence of dissolved oxygen, under the synergistic effect of microorganisms and activated carbon, the organic matter in the wastewater can be efficiently removed, improving the removal effect;

10.污泥浓缩池:用于生化剩余污泥和预处理污泥的浓缩、脱水;10. Sludge concentration tank: used for concentration and dehydration of biochemical excess sludge and pretreatment sludge;

螺杆空气压缩机:对深井进行曝气供氧;Screw air compressor: aeration and oxygen supply to deep wells;

低压离心风机:用于调节池、酸化水解池、脱气池、生物活性碳池的曝气;Low-pressure centrifugal fan: used for aeration of regulating tanks, acidification hydrolysis tanks, degassing tanks, and biologically activated carbon tanks;

污泥脱水机,废水处理产生的污泥主要包括生化污泥和混凝气浮处理产生的污泥;Sludge dewatering machine, the sludge produced by wastewater treatment mainly includes biochemical sludge and sludge produced by coagulation and air flotation treatment;

11.污泥脱水池;11. Sludge dewatering tank;

12.过滤池:内装石英砂滤料,处理水由上向下通过滤层,滤速为5-10米/秒,过滤除去处理水的悬浮物,将处理水中的SS降低到10mg/L以下;12. Filter pool: built-in quartz sand filter material, the treated water passes through the filter layer from top to bottom, the filtration speed is 5-10 m/s, the suspended solids in the treated water are filtered out, and the SS in the treated water is reduced to below 10mg/L ;

13.臭氧氧化池:池底布置钛质微孔曝气器,臭氧由臭氧发生器供给,从钛质微孔曝气器释放出微小气泡与待处理水接触,含臭氧的空气溶入水中,臭氧是最强的氧化剂,它可将微生物灭活、将有机物氧化分解,脱除废水中残剩的色度,使水洁净,处理后可回用于生产;13. Ozone oxidation tank: a titanium microporous aerator is arranged at the bottom of the pool, and the ozone is supplied by the ozone generator. Tiny bubbles are released from the titanium microporous aerator to contact the water to be treated, and the ozone-containing air dissolves into the water. Ozone is the strongest oxidant, it can inactivate microorganisms, oxidize and decompose organic matter, remove residual color in wastewater, make water clean, and can be reused for production after treatment;

臭氧发生器:设备主要包括空压机、空气干燥器、变压器、臭氧发生器等。Ozone generator: The equipment mainly includes air compressors, air dryers, transformers, ozone generators, etc.

有益效果Beneficial effect

(1)本发明方法工艺简单,运行费用低且稳定可靠,操作方便,可实现自动化控制;(1) The method of the present invention has the advantages of simple process, low operating cost, stable and reliable operation, convenient operation and automatic control;

(2)本发明方法的废水处理达标后排放大部分回用于生产,这样不仅减少污染物的排放量,还能消除废水对环境的污染,保护环境。(2) After the waste water treatment of the method of the present invention reaches the standard, most of the discharge is reused in production, so that not only reduces the discharge of pollutants, but also eliminates the pollution of waste water to the environment and protects the environment.

附图说明 Description of drawings

图1废水处理工艺流程图;1为格栅除渣机,2为调节池,3为混凝池,4为预沉池,5为酸化水解池,6为深井,7为脱气池,8为二沉池,9为生物活性碳池,10为污泥浓缩池,11为污泥脱水池,12为过滤池,13为臭氧氧化池。Fig. 1 is the process flow chart of wastewater treatment; 1 is the grid deslagging machine, 2 is the adjustment tank, 3 is the coagulation tank, 4 is the pre-sedimentation tank, 5 is the acidification hydrolysis tank, 6 is the deep well, 7 is the degassing tank, 8 10 is a sludge concentration tank, 11 is a sludge dewatering tank, 12 is a filter tank, and 13 is an ozone oxidation tank.

具体实施方式 Detailed ways

下面结合具体实施例,进一步阐述本发明。应理解,这些实施例仅用于说明本发明而不用于限制本发明的范围。此外应理解,在阅读了本发明讲授的内容之后,本领域技术人员可以对本发明作各种改动或修改,这些等价形式同样落于本申请所附权利要求书所限定的范围。Below in conjunction with specific embodiment, further illustrate the present invention. It should be understood that these examples are only used to illustrate the present invention and are not intended to limit the scope of the present invention. In addition, it should be understood that after reading the teachings of the present invention, those skilled in the art can make various changes or modifications to the present invention, and these equivalent forms also fall within the scope defined by the appended claims of the present application.

实施例1Example 1

印染废水深度处理与中水回用系统,其特征在于:由调节池(2),混凝池(3),预沉池(4),酸化水解池(5),深井(6),脱气池(7),二沉池(8),生物活性碳池(9),污泥浓缩池(10),污泥脱水池(11),过滤池(12),臭氧氧化池(13)组成。The printing and dyeing wastewater advanced treatment and reclaimed water reuse system is characterized in that it consists of a regulating tank (2), a coagulation tank (3), a pre-sedimentation tank (4), an acidification hydrolysis tank (5), a deep well (6), a degassing tank Pool (7), secondary settling tank (8), biologically activated carbon pool (9), sludge thickening tank (10), sludge dehydration tank (11), filter tank (12), and ozone oxidation tank (13).

调节池:废水水质水量调节;Regulating pool: wastewater quality and quantity regulation;

混凝池:用于废水加药混凝,快速搅拌下,加入混凝剂,使之与废水进行混凝反应;Coagulation tank: used for coagulation of waste water, under rapid stirring, add coagulant to make coagulation reaction with waste water;

预沉池:用于混凝后废水的固液分离;Pre-sedimentation tank: used for solid-liquid separation of wastewater after coagulation;

酸化水解池:用于对预处理后的废水及进行微生物酸化水解处理,池内安装曝气管,用少量曝气法使废水和活性污泥的混合,并维持池内溶解氧0.2mg/L以下,使兼氧微生物在缺氧条件下将大分子有机物降解为小分子有机物,提供废水的可生化性;Acidification and hydrolysis tank: used for pretreated wastewater and microbial acidification and hydrolysis treatment. Aeration pipes are installed in the tank, and a small amount of aeration is used to mix the wastewater and activated sludge, and maintain the dissolved oxygen in the tank below 0.2mg/L. Make facultative microorganisms degrade macromolecular organic matter into small molecular organic matter under anoxic conditions, and provide biodegradability of wastewater;

深井顶槽:用于脱除深井循环液中含氧极低的废气;Deep well top tank: used to remove waste gas with extremely low oxygen content in deep well circulating fluid;

附属设备为深井:为同心圆钢结构,采用气体循环运行方式,供给的压缩空气既作为深井的运行动力,又为生物作用提供充足的高浓度溶解氧。深井是占地少、处理效果好、运行费用低、快速、高效的最佳活性污泥法。The auxiliary equipment is a deep well: it is a concentric circular steel structure and adopts the gas circulation operation mode. The compressed air supplied is not only used as the operating power of the deep well, but also provides sufficient high-concentration dissolved oxygen for biological functions. Deep well is the best activated sludge method with less land occupation, good treatment effect, low operating cost, fast and efficient.

脱气池:由于深井深达百米,静水压力为1MPa,通入深井的压缩空气全部溶入水中,循环到达深井顶槽后,循环液中含大量的过饱和空气,会释放出大量微气泡,粘附到活性污泥上,使活性污泥上浮。采用曝气法脱除粘附在污泥上的微气泡,便于污泥在二沉池进行重力法固液分离;Degassing tank: Since the deep well is as deep as 100 meters and the hydrostatic pressure is 1MPa, all the compressed air that enters the deep well is dissolved in the water, and after the circulation reaches the top groove of the deep well, the circulating fluid contains a large amount of supersaturated air, which will release a large number of microbubbles , adhere to the activated sludge and make the activated sludge float. The aeration method is used to remove the micro-bubbles adhering to the sludge, which facilitates the solid-liquid separation of the sludge in the secondary sedimentation tank by gravity method;

二沉池:为辐射式结构的沉淀池,用于深井处理液的固液分离,附属结构:A.池内安装中心传动刮泥,用于收集沉淀污泥;B.污泥回流泵,用于将二沉池的沉淀污泥回入深井、酸化水解池和污泥浓缩池;Secondary settling tank: a settling tank with radial structure, used for solid-liquid separation of deep well treatment fluid, subsidiary structure: A. Central transmission scraper is installed in the tank to collect sedimentation sludge; B. Sludge return pump is used for Return the settled sludge from the secondary settling tank to the deep well, acidification hydrolysis tank and sludge thickening tank;

污泥浓缩池:用于生化剩余污泥和预处理污泥的浓缩、脱水;Sludge concentration tank: used for concentration and dehydration of biochemical excess sludge and pretreatment sludge;

螺杆空气压缩机:对深井进行曝气供氧;Screw air compressor: aeration and oxygen supply to deep wells;

低压离心风机:用于调节池、酸化水解池、脱气池、生物活性碳池的曝气;Low-pressure centrifugal fan: used for aeration of regulating tanks, acidification hydrolysis tanks, degassing tanks, and biologically activated carbon tanks;

污泥脱水机:废水处理产生的污泥主要包括生化污泥和混凝气浮处理产生的污泥;Sludge dewatering machine: The sludge produced by wastewater treatment mainly includes biochemical sludge and sludge produced by coagulation and air flotation treatment;

生物活性碳池:废水在池内停留3小时,池底部有微孔曝气器,池中部布置厚2米的活性碳滤层,处理水中残剩有机物通过活性碳滤层时被活性碳吸附,富集在活性碳上,活性碳上同时长满微生物,在有溶解氧的情况下,在微生物与活性碳的协同作用下,废水中的有机物能被高效地去除,提高去除效果。Biological activated carbon pool: The wastewater stays in the pool for 3 hours. There is a microporous aerator at the bottom of the pool, and an activated carbon filter layer with a thickness of 2 meters is arranged in the middle of the pool. Collected on the activated carbon, the activated carbon is covered with microorganisms at the same time. In the presence of dissolved oxygen, under the synergistic effect of microorganisms and activated carbon, the organic matter in the wastewater can be efficiently removed, improving the removal effect.

过滤池:内装石英砂滤料,处理水由上向下通过滤层,滤速为8米/秒,过滤除去处理水的悬浮物(SS),将处理水中的SS降低到8mg/L;Filter tank: Built-in quartz sand filter material, the treated water passes through the filter layer from top to bottom, the filtration speed is 8 m/s, the suspended solids (SS) in the treated water are filtered out, and the SS in the treated water is reduced to 8mg/L;

臭氧氧化池:池底布置钛质微孔曝气器,臭氧由臭氧发生器供给,从钛质微孔曝气器释放出微小气泡与待处理水接触,含臭氧的空气溶入水中,臭氧是最强的氧化剂,它可将微生物灭活、将有机物氧化分解,脱除废水中残剩的色度,使水洁净,处理后可回用于生产;Ozone oxidation tank: Titanium microporous aerators are arranged at the bottom of the pool. Ozone is supplied by the ozone generator. Tiny bubbles released from the titanium microporous aerators contact the water to be treated, and the ozone-containing air dissolves into the water. Ozone is The strongest oxidant, it can inactivate microorganisms, oxidize and decompose organic matter, remove residual chroma in wastewater, make water clean, and can be reused for production after treatment;

臭氧发生器:设备主要包括空压机、空气干燥器、变压器、臭氧发生器等。Ozone generator: The equipment mainly includes air compressors, air dryers, transformers, ozone generators, etc.

将98m3/hr印染废水先经格栅除渣机除去废水中直径大于1.5mm的悬浮物后流入调节池,进行废水水质水量调节,使废水pH由12.5降低至11.1,水量降至80m3/hr,然后用污水泵将废水提升入混凝池,并在泵前投加硫酸亚铁液(来源于常州钢铁厂),每升废水用量为10mL,通过水泵叶轮搅拌进行混凝反应;经预沉池沉淀分离,沉淀污泥大部分回入混凝池,多余污泥排入污泥浓缩池,浓缩脱水后外运,澄清水流入酸化水解池,与回流的活性污泥混合,当池内溶解氧低于0.2mg/L时,活性污泥中的兼氧微生物对大分子有机物进行酸化水解作用,将大分子难以生化物质降解为小分子可生化物质,提高废水的可生化性,酸化水解后混合液自流入深井曝气池,对废水进行好氧生物处理;由于深井的深度大,静水压力高,溶解氧浓度大,可快速、高效地将废水中的有机物氧化降解为CO2、H2O,化有害为无害,深井处理液自流入脱气池脱除粘附在活性污泥上的微气泡后,入二沉池进行固液分离、沉淀污泥大部分回入深井、酸化水解池,多余污泥排入污泥浓缩池,浓缩脱水后泥并外运;二沉池的澄清水达标就直接排放,否则与需回用水一道自流入生物活性碳池,停留3h,在好氧条件下,利用活性炭与微生物的降解作用,去除废水中的有机物,处理水再经过滤、臭氧氧化、消毒灭菌,进一步氧化去除残剩的有害物质后,入回用水池,用加压泵送车间回用于生产。The 98m 3 /hr printing and dyeing wastewater is first removed by the grid slag remover to remove the suspended solids with a diameter greater than 1.5mm in the wastewater, and then flows into the adjustment tank to adjust the quality and quantity of the wastewater, so that the pH of the wastewater is reduced from 12.5 to 11.1, and the water volume is reduced to 80m 3 / hr, and then use the sewage pump to lift the wastewater into the coagulation tank, and add ferrous sulfate solution (from Changzhou Iron and Steel Works) before the pump. Sedimentation and separation in the settling tank, most of the settled sludge is returned to the coagulation tank, and the excess sludge is discharged into the sludge thickening tank, concentrated and dehydrated, then transported outside, and the clarified water flows into the acidification hydrolysis tank, mixed with the returning activated sludge, and dissolved in the tank When the oxygen is lower than 0.2mg/L, the facultative microorganisms in the activated sludge will acidify and hydrolyze the macromolecular organic matter, degrade the macromolecular difficult-to-biochemical substances into small molecular biochemical substances, improve the biodegradability of wastewater, and after acidification and hydrolysis The mixed liquid flows into the deep well aeration tank for aerobic biological treatment of wastewater; due to the deep well depth, high hydrostatic pressure, and high dissolved oxygen concentration, the organic matter in the wastewater can be oxidized and degraded into CO 2 and H 2 quickly and efficiently O, turning harmful into harmless, the deep well treatment fluid flows into the degassing tank to remove the microbubbles attached to the activated sludge, and then enters the secondary settling tank for solid-liquid separation, most of the settled sludge is returned to the deep well, acidified and hydrolyzed The excess sludge is discharged into the sludge concentration tank, and the sludge is concentrated and dehydrated and transported outside; the clarified water in the secondary settling tank is discharged directly if it meets the standard, otherwise it will flow into the biological activated carbon pool together with the reused water, and stay for 3 hours. Under certain conditions, the degradation of activated carbon and microorganisms is used to remove the organic matter in the wastewater, and the treated water is filtered, ozone oxidized, disinfected and sterilized, and after further oxidation to remove the remaining harmful substances, it is put into the reuse pool and pumped by pressurized water. The workshop is reused for production.

采用本项发明后,印染废水进出水各项水质指标如表1所示:After adopting this invention, the various water quality indicators of printing and dyeing wastewater inflow and outflow are as shown in Table 1:

表1废水处理效果表Table 1 Wastewater treatment effect table

项目 project   进水指标 Water intake index   出水指标 Water output index CODcr(mg/L) CODcr (mg/L)   2000 2000   38 38 BOD5(mg/L) BOD5(mg/L)   750 750   4 4 悬浮物SS(mg/L) Suspended solid SS(mg/L)   500 500   8 8 总磷 Total Phosphorus   5.1 5.1   0.39 0.39 氨氮 Ammonia nitrogen   5.35 5.35   0.25 0.25 色度(倍) Chroma (times)   600 600   4 4 pH pH   12.5 12.5   8.5 8.5

实施例2Example 2

印染废水深度处理与中水回用系统,其特征在于:由调节池(2),混凝池(3),预沉池(4),酸化水解池(5),深井(6),脱气池(7),二沉池(8),生物活性碳池(9),污泥浓缩池(10),污泥脱水池(11),过滤池(12),臭氧氧化池(13)组成。The printing and dyeing wastewater advanced treatment and reclaimed water reuse system is characterized in that it consists of a regulating tank (2), a coagulation tank (3), a pre-sedimentation tank (4), an acidification hydrolysis tank (5), a deep well (6), a degassing tank Pool (7), secondary settling tank (8), biologically activated carbon pool (9), sludge thickening tank (10), sludge dehydration tank (11), filter tank (12), and ozone oxidation tank (13).

调节池:废水水质水量调节;Regulating pool: wastewater quality and quantity regulation;

混凝池:用于废水加药混凝;Coagulation tank: used for coagulation of wastewater dosing;

预沉池:用于混凝后废水的固液分离;Pre-sedimentation tank: used for solid-liquid separation of wastewater after coagulation;

酸化水解池:用于对预处理后的废水及进行微生物酸化水解处理,池内安装曝气管,用少量曝气法使废水和活性污泥混合,并维持池内溶解氧0.2mg/L以下,使兼氧微生物在缺氧条件下将大分子有机物降解为小分子有机物,提供废水的可生化性;Acidification and hydrolysis tank: used for pretreated wastewater and microbial acidification and hydrolysis treatment. Aeration pipes are installed in the tank, and a small amount of aeration is used to mix wastewater and activated sludge, and maintain dissolved oxygen in the tank below 0.2mg/L, so that Facultative microorganisms degrade macromolecular organic matter into small molecular organic matter under anoxic conditions, providing biodegradability of wastewater;

深井顶槽:用于脱除深井循环液中含氧极低的废气;Deep well top tank: used to remove waste gas with extremely low oxygen content in deep well circulating fluid;

脱气池:采用曝气法脱除粘附在污泥上的微气泡,便于污泥在二沉池进行重力法固液分离;Degassing tank: The aeration method is used to remove the micro-bubbles adhering to the sludge, which facilitates the solid-liquid separation of the sludge in the secondary sedimentation tank by gravity method;

二沉池:为辐射式结构的沉淀池,用于深井处理液的固液分离,附属设备:A.池内安装中心传动刮泥,用于收集沉淀污泥,B.污泥回流泵,用于将二沉池的沉淀污泥回入深井、酸化水解池和污泥浓缩池;Secondary settling tank: a settling tank with radial structure, used for solid-liquid separation of deep well treatment fluid, auxiliary equipment: A. Central drive mud scraper is installed in the tank to collect sedimentation sludge, B. Sludge return pump is used for Return the settled sludge from the secondary settling tank to the deep well, acidification hydrolysis tank and sludge thickening tank;

污泥浓缩池:用于生化剩余污泥和预处理污泥的浓缩、脱水;Sludge concentration tank: used for concentration and dehydration of biochemical excess sludge and pretreatment sludge;

螺杆空气压缩机:对深井进行曝气供氧;Screw air compressor: aeration and oxygen supply to deep wells;

低压离心风机:用于调节池、酸化水解池、脱气池、生物活性碳池的曝气;Low-pressure centrifugal fan: used for aeration of regulating tanks, acidification hydrolysis tanks, degassing tanks, and biologically activated carbon tanks;

污泥脱水机:污泥脱水,废水处理产生的污泥主要包括生化污泥和混凝气浮处理产生的污泥;Sludge dewatering machine: sludge dehydration, the sludge produced by wastewater treatment mainly includes biochemical sludge and sludge produced by coagulation and air flotation treatment;

生物活性碳池:废水在池内停留4小时,池底部有微孔曝气器,池中部布置厚2米的活性碳滤层,处理水中残剩有机物,通过活性碳滤层时被活性碳吸附,富集在活性碳上,活性碳上同时长满微生物,在有溶解氧的情况下,在微生物与活性碳的协同作用下,废水中的有机物能被高效地去除,提高去除效果;Biological activated carbon pool: Wastewater stays in the pool for 4 hours. There is a microporous aerator at the bottom of the pool, and an activated carbon filter layer with a thickness of 2 meters is arranged in the middle of the pool to treat residual organic matter in the water. When it passes through the activated carbon filter layer, it is adsorbed by activated carbon. Enriched on the activated carbon, the activated carbon is covered with microorganisms at the same time, in the presence of dissolved oxygen, under the synergistic effect of microorganisms and activated carbon, the organic matter in the wastewater can be efficiently removed, improving the removal effect;

过滤池:内装石英砂滤料,处理水由上向下通过滤层,滤速为6米/秒,过滤除去处理水的悬浮物(SS),将处理水中的SS降低到7mg/L;Filter tank: Built-in quartz sand filter material, the treated water passes through the filter layer from top to bottom, the filtration speed is 6 m/s, the suspended solids (SS) in the treated water are filtered out, and the SS in the treated water is reduced to 7mg/L;

臭氧氧化池:池底布置钛质微孔曝气器,臭氧由臭氧发生器供给,从钛质微孔曝气器释放出微小气泡与待处理水接触,含臭氧的空气溶入水中,将微生物灭活,将有机物氧化分解,脱除废水中残剩的色度,使水洁净,处理后可回用于生产;Ozone oxidation tank: Titanium microporous aerators are arranged at the bottom of the pool. Ozone is supplied by the ozone generator. Tiny bubbles are released from the titanium microporous aerators to contact with the water to be treated. The ozone-containing air dissolves into the water, and microorganisms Inactivation, oxidative decomposition of organic matter, removal of residual chroma in wastewater, making water clean, and can be reused for production after treatment;

臭氧发生器:设备主要包括空压机、空气干燥器、变压器、臭氧发生器等。Ozone generator: The equipment mainly includes air compressors, air dryers, transformers, ozone generators, etc.

将103m3/hr印染废水先经格栅除渣机除去废水中直径大于1.5mm的悬浮物后流入调节池,进行废水水质水量调节,使废水pH由12.1降低至10.8,水量降至85m3/hr,然后用污水泵将废水提升入混凝池,并在泵前投加硫酸亚铁液(来源于常州钢铁厂),每升废水用量为9mL,通过水泵叶轮搅拌进行混凝反应;经预沉池沉淀分离,沉淀污泥大部分回入混凝池,多余污泥排入污泥浓缩池,浓缩脱水后外运,澄清水流入酸化水解池,与回流的活性污泥混合,当池内溶解氧为低于0.2mg/L时,活性污泥中的兼氧微生物对大分子有机物进行酸化水解作用,将大分子难以生化物质降解为小分子可生化物质,提高废水的可生化性,酸化水解后混合液自流入深井曝气池,对废水进行好氧生物处理;由于深井的深度大,静水压力高,溶解氧浓度大,可快速、高效地将废水中的有机物氧化降解为CO2、H2O,深井处理液自流入脱气池脱除粘附在活性污泥上的微气泡后,入二沉池进行固液分离、沉淀污泥大部分回入深井、酸化水解池,多余污泥排入污泥浓缩池,浓缩脱水后泥并外运;二沉池的澄清水达标就直接排放,否则与需回用水一道自流入生物活性碳池,停留4h,在好氧条件下,利用活性炭与微生物的降解作用,去除废水中的有机物,处理水再经过滤、臭氧氧化、消毒灭菌,进一步氧化去除残剩的有害物质后,入回用水池,用加压泵送车间回用于生产。The 103m 3 /hr printing and dyeing wastewater is first removed by the grid slag remover to remove the suspended solids with a diameter greater than 1.5mm in the wastewater, and then flows into the adjustment tank to adjust the quality and quantity of the wastewater, so that the pH of the wastewater is reduced from 12.1 to 10.8, and the water volume is reduced to 85m 3 / hr, then use the sewage pump to lift the wastewater into the coagulation tank, and add ferrous sulfate liquid (from Changzhou Iron and Steel Works) before the pump, the amount of wastewater per liter is 9mL, and the coagulation reaction is carried out by stirring with the impeller of the water pump; Sedimentation and separation in the settling tank, most of the settled sludge is returned to the coagulation tank, and the excess sludge is discharged into the sludge thickening tank, concentrated and dehydrated, then transported outside, and the clarified water flows into the acidification hydrolysis tank, mixed with the returning activated sludge, and dissolved in the tank When the oxygen is lower than 0.2mg/L, the facultative microorganisms in the activated sludge will acidify and hydrolyze the macromolecular organic matter, degrade the macromolecular difficult-to-biochemical substances into small molecular biochemical substances, improve the biodegradability of wastewater, and acidify and hydrolyze Afterwards, the mixed liquid flows into the deep well aeration tank for aerobic biological treatment of the wastewater; due to the deep well depth, high hydrostatic pressure, and high dissolved oxygen concentration, the organic matter in the wastewater can be quickly and efficiently oxidized and degraded into CO 2 , H 2 O, the deep well treatment fluid flows into the degassing tank to remove microbubbles attached to the activated sludge, and then enters the secondary settling tank for solid-liquid separation. Discharge into the sludge concentration tank, concentrate and dehydrate the sludge and transport it outside; the clarified water in the secondary sedimentation tank will be discharged directly if it meets the standard, otherwise it will flow into the biological activated carbon pool together with the reused water, and stay for 4 hours. Under aerobic conditions, use activated carbon Degradation with microorganisms removes organic matter in wastewater, and the treated water is filtered, ozone oxidized, sterilized, and further oxidized to remove residual harmful substances. .

采用本项发明后,印染废水进出水各项水质指标如表2所示:After adopting this invention, the various water quality indexes of printing and dyeing wastewater inflow and outflow are as shown in Table 2:

表2废水处理效果表Table 2 Wastewater Treatment Effect Table

  项目 project   进水指标 Water intake index   出水指标 Water output index   CODcr(mg/L) CODcr(mg/L)   2108 2108   32 32   BOD5(mg/L) BOD5(mg/L)   785 785   3 3   悬浮物SS(mg/L) Suspended matter SS(mg/L)   632 632   7 7   总磷(mg/L) Total phosphorus (mg/L)   4.7 4.7   0.24 0.24   氨氮(mg/L) Ammonia nitrogen (mg/L)   4.58 4.58   0.13 0.13   色度(倍) Chromaticity (times)   512 512   2 2   pH pH   12.1 12.1   8.2 8.2

Claims (11)

1.一种印染废水深度处理与中水回用系统,其特征在于:由调节池(2),混凝池(3),预沉池(4),酸化水解池(5),深井(6),脱气池(7),二沉池(8),生物活性碳池(9),污泥浓缩池(10),污泥脱水池(11),过滤池(12),臭氧氧化池(13)组成。1. A printing and dyeing wastewater advanced treatment and reclaimed water system is characterized in that: by adjusting tank (2), coagulation tank (3), pre-sedimentation tank (4), acidification hydrolysis tank (5), deep well (6 ), degassing tank (7), secondary sedimentation tank (8), biological activated carbon tank (9), sludge thickening tank (10), sludge dewatering tank (11), filter tank (12), ozone oxidation tank ( 13) Composition. 2.根据权利要求1所述的一种印染废水深度处理与中水回用系统,其特征在于:所述的混凝池为矩形钢筋混凝土结构,池内安装混凝搅拌机二台,在快速搅拌下,加入混凝剂,使之与废水进行混凝反应。2. A printing and dyeing wastewater advanced treatment and reclaimed water system according to claim 1, characterized in that: the coagulation tank is a rectangular reinforced concrete structure, two coagulation mixers are installed in the tank, and the coagulation tank is quickly stirred , add coagulant to make coagulation reaction with wastewater. 3.根据权利要求1所述的一种印染废水深度处理与中水回用系统,其特征在于:所述的酸化水解池池内安装曝气管,用少量曝气法使废水和活性污泥的混合,并维持池内溶解氧0.2mg/L以下。3. A kind of printing and dyeing wastewater advanced treatment and reclaimed water reuse system according to claim 1, characterized in that: an aeration pipe is installed in the acidification hydrolysis pool, and a small amount of aeration method is used to make the waste water and activated sludge Mix and maintain the dissolved oxygen in the pool below 0.2mg/L. 4.根据权利要求1所述的一种印染废水深度处理与中水回用系统,其特征在于:所述的深井为同心圆钢结构,采用气体循环运行方式。4. A printing and dyeing wastewater advanced treatment and reclaimed water reuse system according to claim 1, characterized in that: said deep well is a concentric circular steel structure and adopts a gas circulation operation mode. 5.根据权利要求1所述的一种印染废水深度处理与中水回用系统,其特征在于:所述的二沉池池内安装中心传动刮泥和污泥回流泵。5. A printing and dyeing wastewater advanced treatment and reclaimed water reuse system according to claim 1, characterized in that: a central drive sludge scraper and a sludge return pump are installed in the secondary settling tank. 6.根据权利要求1所述的一种印染废水深度处理与中水回用系统,其特征在于:所述的深井曝气池使用螺杆空气压缩机对深井进行曝气供氧。6. A printing and dyeing wastewater advanced treatment and reclaimed water reuse system according to claim 1, characterized in that: said deep well aeration tank uses a screw air compressor to aerate and supply oxygen to the deep well. 7.根据权利要求1所述的一种印染废水深度处理与中水回用系统,其特征在于:所述的生物活性碳池:废水在池内停留3-5小时,池底部有微孔曝气器,池中部布置厚2米的活性碳滤层,处理水中残剩有机物通过活性碳滤层时被活性碳吸附,富集在活性碳上,活性碳上同时长满微生物,在有溶解氧的情况下,在微生物与活性碳的协同作用下,废水中的有机物能被高效地去除。7. A printing and dyeing wastewater advanced treatment and reclaimed water reuse system according to claim 1, characterized in that: the biologically activated carbon pool: the wastewater stays in the pool for 3-5 hours, and there are micropores for aeration at the bottom of the pool An activated carbon filter layer with a thickness of 2 meters is arranged in the middle of the pool. When the residual organic matter in the treated water passes through the activated carbon filter layer, it is absorbed by the activated carbon and enriched on the activated carbon. At the same time, the activated carbon is covered with microorganisms. In the presence of dissolved oxygen Under normal circumstances, under the synergistic effect of microorganisms and activated carbon, organic matter in wastewater can be efficiently removed. 8.根据权利要求1所述的一种印染废水深度处理与中水回用系统,其特征在于:所述的过滤池:内装石英砂滤料,处理水由上向下通过滤层,滤速为5-10米/秒,过滤除去处理水的悬浮物(SS),将处理水中的SS降低到10mg/L。8. A printing and dyeing wastewater advanced treatment and reclaimed water reuse system according to claim 1, characterized in that: the filter tank is equipped with quartz sand filter material, and the treated water passes through the filter layer from top to bottom. 5-10 m/s, filter to remove suspended solids (SS) in the treated water, and reduce the SS in the treated water to 10mg/L. 9.根据权利要求1所述的一种印染废水深度处理与中水回用方法,其特征在于:所述的臭氧氧化池:池底布置钛质微孔曝气器,臭氧由臭氧发生器供给,从钛质微孔曝气器释放出微小气泡与待处理水接触,含臭氧的空气溶入水中。9. A method for advanced treatment of printing and dyeing wastewater and reuse of reclaimed water according to claim 1, characterized in that: the ozone oxidation pool: a titanium microporous aerator is arranged at the bottom of the pool, and the ozone is supplied by an ozone generator , Tiny air bubbles released from the titanium microporous aerator contact the water to be treated, and the ozone-containing air dissolves into the water. 10.一种印染废水深度处理与中水回用方法,包括:10. A method for advanced treatment of printing and dyeing wastewater and reclaimed water, comprising: 印染废水先经格栅除渣机除去废水中直径大于1.5mm的悬浮物后流入调节池,进行废水水质水量调节,然后用污水泵将废水提升入混凝池,并在泵前投加无机混凝剂,搅拌进行混凝反应,经预沉池沉淀分离,沉淀污泥大部分回入混凝池,多余污泥排入污泥浓缩池,浓缩脱水后外运,澄清水流入酸化水解池,与回流的活性污泥混合,在缺氧条件下,活性污泥中的兼氧微生物对大分子有机物进行酸化水解作用,酸化水解后混合液自流入深井曝气池,对废水进行好氧生物处理;深井处理液自流入脱气池脱除粘附在活性污泥上的微气泡后,入二沉池进行固液分离,沉淀污泥大部分回入深井、酸化水解池,多余污泥排入污泥浓缩池,浓缩脱水后泥并外运;二沉池的澄清水达标就直接排放,否则与需回用水一道自流入生物活性碳池,在好氧条件下,去除废水中的有机物,处理水再经过滤池过滤、臭氧氧化池臭氧氧化、消毒灭菌,进一步氧化去除残剩的有害物质后,入回用水池,用加压泵送车间回用于生产。Printing and dyeing wastewater first passes through the grid deslagging machine to remove suspended solids with a diameter greater than 1.5mm in the wastewater, and then flows into the regulating tank to adjust the quality and quantity of the wastewater. Then the wastewater is lifted into the coagulation tank with a sewage pump, and inorganic mixing Coagulant, stirring for coagulation reaction, sedimentation and separation in the pre-sedimentation tank, most of the settled sludge is returned to the coagulation tank, and the excess sludge is discharged into the sludge concentration tank, concentrated and dehydrated, then exported, and the clarified water flows into the acidification hydrolysis tank. Mixed with the returning activated sludge, under anaerobic conditions, the facultative microorganisms in the activated sludge acidify and hydrolyze the macromolecular organic matter, after the acidification and hydrolysis, the mixed liquid flows into the deep well aeration tank for aerobic biological treatment of the wastewater ;The deep well treatment fluid flows into the degassing tank to remove the microbubbles attached to the activated sludge, and then enters the secondary settling tank for solid-liquid separation. Most of the settled sludge returns to the deep well and acidification hydrolysis tank, and the excess sludge is discharged into Sludge concentration tank, after concentration and dehydration, the sludge is transported outside; the clarified water in the secondary sedimentation tank will be discharged directly if it reaches the standard, otherwise it will flow into the biological activated carbon pool together with the reused water, and the organic matter in the wastewater will be removed under aerobic conditions. The water is then filtered through the filter tank, ozone oxidized in the ozone oxidation tank, disinfected and sterilized, and further oxidized to remove the residual harmful substances, and then enters the reuse pool, and is sent to the workshop by a pressurized pump for reuse in production. 11.根据权利要求10所述的一种印染废水深度处理与中水回用方法,其特征在于:所述的无机混凝剂为硫酸亚铁液,每升废水用量为8-10mL。11. A method for advanced treatment of printing and dyeing wastewater and reuse of reclaimed water according to claim 10, characterized in that: the inorganic coagulant is liquid ferrous sulfate, and the dosage per liter of wastewater is 8-10mL.
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