CN104045206A - UV/O3+BAF combined advanced oxidation sewage treatment equipment - Google Patents

UV/O3+BAF combined advanced oxidation sewage treatment equipment Download PDF

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CN104045206A
CN104045206A CN201410248505.XA CN201410248505A CN104045206A CN 104045206 A CN104045206 A CN 104045206A CN 201410248505 A CN201410248505 A CN 201410248505A CN 104045206 A CN104045206 A CN 104045206A
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filter material
area
sewage treatment
support layer
material layer
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王白杨
杨凌夕
陈聪
黄芽保
胡娇
麻超
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Nanchang University
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Nanchang University
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Abstract

The invention discloses a UV (ultraviolet)/O3+BAF (biological aerated filter) advanced oxidation sewage treatment facility which comprises a UV/O3 catalytic reaction region, a supporting layer and haydite filter material layer region and a water outlet region, wherein the supporting layer and haydite filter material layer region is provided with a BAF. By combining the UV catalytic O3 oxidation and microbial degradation technique, the facility lowers the sewage treatment cost and enhances the COD (chemical oxygen demand) removal rate.

Description

UV/O3+BAF组合式高级氧化污水处理设备UV/O3+BAF combined advanced oxidation sewage treatment equipment

技术领域 technical field

本发明涉及一种污水处理装置,尤其涉及一种UV/O3+BAF组合式高级氧化污水处理设备。 The invention relates to a sewage treatment device, in particular to a UV/O 3 +BAF combined advanced oxidation sewage treatment equipment.

背景技术 Background technique

曝气生物滤池是将接触氧化工艺和悬浮物过滤工艺结合在一起的污水处理工艺,其工艺原理为在滤池中装填一定量粒径较小的粒状滤料,滤料表面生长着生物膜,滤池内部曝气,污水流经时,由于滤料上附着高浓度生物膜量,利用其强氧化降解能力快速降解废水中的污染物,同时,利用滤料粒径较小的特点及生物膜的生物絮凝作用,截留污水中的大量悬浮物,且保证脱落的生物膜不会随水漂出,由此达到净化废水的目的。但是受微生物降解能力的限制,曝气生物滤池并不能处理含有大量难降解有机物的废水。其主要缺点是:(1)曝气生物滤池对进水的SS要求较高,需要采用对S有较高处理效果的预处理工艺。而且,进水的浓度不能太高,否则容易引起滤料结团、堵塞。(2)不能处理高浓度难降解有机废水,一般情况下,进水COD一般不能超过2000mg/L,这也就限制了其污水处理范围。 The biological aerated filter is a sewage treatment process that combines the contact oxidation process and the suspended solids filtration process. The process principle is to fill the filter with a certain amount of granular filter material with a small particle size, and a biofilm grows on the surface of the filter material. , the inside of the filter is aerated, and when the sewage flows through, due to the high concentration of biofilm attached to the filter material, its strong oxidative degradation ability is used to quickly degrade the pollutants in the wastewater. The biological flocculation of the membrane intercepts a large amount of suspended solids in the sewage, and ensures that the detached biofilm will not float out with the water, thereby achieving the purpose of purifying the wastewater. However, limited by the degradation ability of microorganisms, biological aerated filters cannot treat wastewater containing a large amount of refractory organic matter. Its main disadvantages are: (1) The biological aerated filter has high requirements on the SS of the influent, and needs to adopt a pretreatment process with a high treatment effect on S. Moreover, the concentration of the incoming water should not be too high, otherwise it will easily cause the filter material to agglomerate and block. (2) It cannot handle high-concentration refractory organic wastewater. In general, the influent COD cannot exceed 2000mg/L, which limits the scope of its sewage treatment.

发明内容 Contents of the invention

本发明的目的是提供一种UV/O3+BAF组合式高级氧化污水处理设备,它可以高效率、低成本地处理难生物降解有机废水。 The purpose of the present invention is to provide a UV/O 3 +BAF combined advanced oxidation sewage treatment equipment, which can treat refractory biodegradable organic wastewater with high efficiency and low cost.

本发明是这样来实现的,一种UV/O3+BAF组合式高级氧化污水处理设备,包括UV/O3催化反应区、承托层及陶粒滤料层区、出水区,其中UV/O3催化反应区含有气液混合泵、臭氧发生器、紫外灯管,承托层及陶粒滤料层区含有承托层、曝气管、填料、滤头,其特征是,UV/O3催化反应区底部连有入水管,入水管之前连有气液混合泵,气液混合泵与臭氧发生器连接;UV/O3催化反应区上部安装有一个反冲洗进水管和反冲洗进气管;承托层及陶粒滤料层区底部安装有承托层、滤头,承托层上布置滤头;承托层及陶粒滤料层区中部安装有曝气管;承托层及陶粒滤料层区上部为微生物附着生长的填料层;出水区为溢流装置,底部连有正常出水管和反冲洗出水管。 The present invention is achieved in this way. A UV/O 3 +BAF combined advanced oxidation sewage treatment equipment includes a UV/O 3 catalytic reaction zone, a supporting layer, a ceramsite filter material layer zone, and a water outlet zone, wherein the UV/O 3 The O 3 catalytic reaction area contains a gas-liquid mixing pump, an ozone generator, and an ultraviolet lamp. The supporting layer and the ceramsite filter material layer area include a supporting layer, an aeration tube, a filler, and a filter head. It is characterized in that the UV/O 3 The bottom of the catalytic reaction zone is connected to the water inlet pipe, and before the water inlet pipe is connected to the gas-liquid mixing pump, the gas-liquid mixing pump is connected to the ozone generator; the upper part of the UV/O 3 catalytic reaction zone is equipped with a backwash water inlet pipe and a backwash intake pipe The support layer and the filter head are installed at the bottom of the support layer and the ceramsite filter material layer area, and the filter head is arranged on the support layer; the aeration pipe is installed in the middle of the support layer and the ceramsite filter material layer area; The upper part of the ceramsite filter material layer area is a filler layer for the growth of microorganisms; the water outlet area is an overflow device, and the bottom is connected with a normal outlet pipe and a backwash outlet pipe.

进一步,所述反冲洗出水管的出水水位比正常出水管低。 Further, the outlet water level of the backwash outlet pipe is lower than the normal outlet pipe.

本发明的优点是:(1)紫外线催化效果好,O3的氧化能力好,UV/O3协同作用效果显著,降低了污水处理成本,COD的除去率高;(2)UV/O3技术中残余的过量O3可以上浮被微生物利用,尾气处理成本少,无二次污染。(3)UV/O3技术与成熟的BAF技术组合,处理效率高,经济实用,具有推广性;(4)设备运行过程中,各项关键指标实时监控,保证处理效果和安全性。 The advantages of the present invention are: (1) good ultraviolet catalysis effect, good O 3 oxidation ability, remarkable UV/O 3 synergistic effect, reduced sewage treatment cost, and high COD removal rate; (2) UV/O 3 technology Excess O 3 remaining in the gas can float up and be used by microorganisms, the cost of tail gas treatment is low, and there is no secondary pollution. (3) The combination of UV/O 3 technology and mature BAF technology has high processing efficiency, is economical and practical, and is popular; (4) During the operation of the equipment, various key indicators are monitored in real time to ensure the processing effect and safety.

附图说明 Description of drawings

   图1为本发明的结构示意图。 Figure 1 is a schematic structural view of the present invention.

在图中,1.气液混合泵   2.臭氧发生器   3.反冲洗进水管   4.承托层   5.曝气管   6.填料层   7.外壳   8.正常出水管   9.反冲洗出水管   10.滤头   11.反冲洗进气管   12.紫外灯管。 In the figure, 1. Gas-liquid mixing pump 2. Ozone generator 3. Backwash water inlet pipe 4. Supporting layer 5. Aeration pipe 6. Packing layer 7. Shell 8. Normal outlet pipe 9. Backwash outlet pipe 10 .Filter head 11.Backwash intake pipe 12.UV lamp.

具体实施方式 Detailed ways

如图1所示,一种UV/O3+BAF组合式高级氧化污水处理设备,包括一个外壳7,外壳7内分为UV/O3催化反应区、承托层及陶粒滤料层区、出水区,其中UV/O3催化反应区内设紫外灯管12, UV/O3催化反应区底部连有入水管,入水管之前连有气液混合泵1,气液混合泵1与臭氧发生器2连接;UV/O3催化反应区上部安装有一个反冲洗进水管3和反冲洗进气管11;承托层及陶粒滤料层区底部安装有承托层4、滤头10,承托层4上布置滤头10;承托层及陶粒滤料层区中部安装有曝气管5;承托层及陶粒滤料层区上部为微生物附着生长的填料层6;出水区为溢流装置,底部连有正常出水管8和反冲洗出水管9。所述反冲洗出水管9的出水水位比正常出水管8低。 As shown in Figure 1, a UV/O 3 +BAF combined advanced oxidation sewage treatment equipment includes a shell 7, and the shell 7 is divided into a UV/O 3 catalytic reaction zone, a supporting layer and a ceramsite filter material layer zone , water outlet area, wherein UV/O 3 catalytic reaction zone is provided with ultraviolet lamp 12, the bottom of UV/O 3 catalytic reaction zone is connected with water inlet pipe, before the water inlet pipe is connected with gas-liquid mixing pump 1, gas-liquid mixing pump 1 and ozone The generator 2 is connected; a backwash water inlet pipe 3 and a backwash inlet pipe 11 are installed on the upper part of the UV/O 3 catalytic reaction zone; a support layer 4 and a filter head 10 are installed on the bottom of the support layer and the ceramsite filter layer area, A filter head 10 is arranged on the support layer 4; an aeration pipe 5 is installed in the middle of the support layer and the ceramsite filter material layer area; the upper part of the support layer and the ceramsite filter material layer area is a filler layer 6 for the growth of microorganisms; the water outlet area It is an overflow device, and the bottom is connected with a normal outlet pipe 8 and a backwash outlet pipe 9. The outlet water level of the backwash outlet pipe 9 is lower than the normal outlet pipe 8 .

污水进水管道和臭氧发生器2一起接入气液混合泵1,根据污染物的浓度调节合适的臭氧和污水配比,被泵入催化反应池的污水和臭氧在紫外光线12的催化作用下发生反应,高浓度难生物降解有机物被降解为易生物降解有机物。 The sewage inlet pipe and the ozone generator 2 are connected to the gas-liquid mixing pump 1, and the appropriate ratio of ozone and sewage is adjusted according to the concentration of pollutants. The sewage and ozone pumped into the catalytic reaction tank are catalyzed by ultraviolet light 12 A reaction occurs, and high concentrations of refractory biodegradable organics are degraded into readily biodegradable organics.

含有易降解有机物污水通过承托层4(承托层4的一个作用在于支撑固定滤头10,另一个作用在于阻挡紫外光线进入曝气生物滤池)中的滤头10进入曝气生物滤池,曝气生物滤池主要包含填料层6与曝气管5,微生物附着在填料层6上生长,曝气管5通入新鲜空气,在微生物的作用下,易生物降解有机物被彻底分解,从而得到合乎排放标准的干净水。 Sewage containing easily degradable organic matter passes through the filter head 10 in the supporting layer 4 (one function of the supporting layer 4 is to support and fix the filter head 10, and the other function is to block ultraviolet rays from entering the biological aerated filter tank) and enter the biological aerated filter tank , the biological aerated filter mainly includes a packing layer 6 and an aeration tube 5, microorganisms adhere to the packing layer 6 and grow, and the aeration tube 5 is fed with fresh air. Under the action of microorganisms, the easily biodegradable organic matter is completely decomposed, thereby Get clean water that meets discharge standards.

催化反应池内未能反应完的少量臭氧上浮进入曝气生物滤池,自身发生氧化还原反应生成氧气,供给微生物生长繁殖,减少了臭氧排出对环境产生的污染,同时又有利于微生物的更新。 A small amount of unreacted ozone in the catalytic reaction tank floats up into the biological aerated filter, where it undergoes a redox reaction to generate oxygen, which supplies the growth and reproduction of microorganisms, reduces the pollution of the environment caused by ozone discharge, and is also conducive to the renewal of microorganisms.

反冲洗进水管3和反冲洗进气管11定期打开,用于净化曝气生物滤池,除去滤头上污泥等阻塞物质以及冲走已经死亡的微生物。 The backwash water inlet pipe 3 and the backwash air inlet pipe 11 are opened regularly to purify the biological aerated filter, to remove blocking substances such as sludge on the filter head and to wash away dead microorganisms.

Claims (1)

1.一种UV/O3+BAF组合式高级氧化污水处理设备,包括UV/O3催化反应区、承托层及陶粒滤料层区、出水区,其特征是UV/O3催化反应区内设紫外灯管, UV/O3催化反应区底部连有入水管,入水管之前连有气液混合泵,气液混合泵与臭氧发生器连接;UV/O3催化反应区上部安装有一个反冲洗进水管和反冲洗进气管;承托层及陶粒滤料层区底部安装有承托层、滤头,承托层上布置滤头;承托层及陶粒滤料层区中部安装有曝气管;承托层及陶粒滤料层区上部为微生物附着生长的填料层;出水区为溢流装置,底部连有正常出水管和反冲洗出水管。 1. A UV/O 3 +BAF combined advanced oxidation sewage treatment equipment, including UV/O 3 catalytic reaction zone, support layer and ceramsite filter material layer zone, water outlet zone, characterized by UV/O 3 catalytic reaction There is an ultraviolet lamp tube in the area, and a water inlet pipe is connected to the bottom of the UV/O 3 catalytic reaction area, and a gas-liquid mixing pump is connected before the water inlet pipe, and the gas-liquid mixing pump is connected to the ozone generator ; A backwash water inlet pipe and a backwash inlet pipe; the support layer and the filter head are installed at the bottom of the support layer and the ceramsite filter material layer area, and the filter head is arranged on the support layer; the middle part of the support layer and the ceramsite filter material layer area An aeration pipe is installed; the support layer and the upper part of the ceramsite filter material layer area are the filler layer for the growth of microorganisms; the water outlet area is an overflow device, and the bottom is connected with a normal outlet pipe and a backwash outlet pipe.
CN201410248505.XA 2014-06-06 2014-06-06 UV/O3+BAF combined advanced oxidation sewage treatment equipment Pending CN104045206A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106927617A (en) * 2015-12-29 2017-07-07 广东卓信环境科技股份有限公司 The integrated device and its method of a kind of sewage disposal
CN110183047A (en) * 2019-06-05 2019-08-30 郑州大学 A kind of photocatalysis and biological aerated filter coupling device
CN112142270A (en) * 2020-10-26 2020-12-29 武汉理工大学 Variable-flow drinking water advanced treatment device for simultaneous removal of antibiotics and resistance genes

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101070216A (en) * 2007-06-18 2007-11-14 华南理工大学 Integrated ozone and aeration biological filtering pool water treatment apparatus and method
CN201751397U (en) * 2010-01-29 2011-02-23 厦门绿邦膜技术有限公司 Sewage treatment device of ozone and aeration biological filter pool
CN102838259A (en) * 2012-09-18 2012-12-26 北京桑德环境工程有限公司 Depth treatment method and system of wastewater in industrial park
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106927617A (en) * 2015-12-29 2017-07-07 广东卓信环境科技股份有限公司 The integrated device and its method of a kind of sewage disposal
CN110183047A (en) * 2019-06-05 2019-08-30 郑州大学 A kind of photocatalysis and biological aerated filter coupling device
CN112142270A (en) * 2020-10-26 2020-12-29 武汉理工大学 Variable-flow drinking water advanced treatment device for simultaneous removal of antibiotics and resistance genes

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Application publication date: 20140917