CN104045206A - UV/O3+BAF combined advanced oxidation sewage treatment equipment - Google Patents
UV/O3+BAF combined advanced oxidation sewage treatment equipment Download PDFInfo
- Publication number
- 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
- Authority
- CN
- China
- Prior art keywords
- filter material
- area
- sewage treatment
- support layer
- material layer
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000010865 sewage Substances 0.000 title claims abstract description 18
- 230000003647 oxidation Effects 0.000 title claims abstract description 10
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 23
- 239000000463 material Substances 0.000 claims abstract description 18
- 238000006555 catalytic reaction Methods 0.000 claims abstract description 15
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims description 10
- 244000005700 microbiome Species 0.000 claims description 10
- 239000007788 liquid Substances 0.000 claims description 9
- 238000005273 aeration Methods 0.000 claims description 7
- 239000000945 filler Substances 0.000 claims description 4
- 238000000034 method Methods 0.000 abstract description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 2
- 230000015556 catabolic process Effects 0.000 abstract description 2
- 238000006731 degradation reaction Methods 0.000 abstract description 2
- 239000001301 oxygen Substances 0.000 abstract description 2
- 229910052760 oxygen Inorganic materials 0.000 abstract description 2
- 239000000126 substance Substances 0.000 abstract description 2
- 230000003197 catalytic effect Effects 0.000 abstract 1
- 230000000813 microbial effect Effects 0.000 abstract 1
- 239000002351 wastewater Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 3
- 239000005416 organic matter Substances 0.000 description 3
- 238000012856 packing Methods 0.000 description 3
- 239000003344 environmental pollutant Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 238000010525 oxidative degradation reaction Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000006479 redox reaction Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Physical Water Treatments (AREA)
Abstract
Description
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)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201410248505.XA CN104045206A (en) | 2014-06-06 | 2014-06-06 | UV/O3+BAF combined advanced oxidation sewage treatment equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201410248505.XA CN104045206A (en) | 2014-06-06 | 2014-06-06 | UV/O3+BAF combined advanced oxidation sewage treatment equipment |
Publications (1)
Publication Number | Publication Date |
---|---|
CN104045206A true CN104045206A (en) | 2014-09-17 |
Family
ID=51498662
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201410248505.XA Pending CN104045206A (en) | 2014-06-06 | 2014-06-06 | UV/O3+BAF combined advanced oxidation sewage treatment equipment |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN104045206A (en) |
Cited By (3)
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 |
Citations (5)
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 |
CN203307111U (en) * | 2013-05-06 | 2013-11-27 | 江苏正本净化节水科技实业有限公司 | Biological aerated filter |
CN103626360A (en) * | 2013-11-22 | 2014-03-12 | 华南理工大学 | Advanced treatment method of integrated catalytic ozonation-biological aerated filter water |
-
2014
- 2014-06-06 CN CN201410248505.XA patent/CN104045206A/en active Pending
Patent Citations (5)
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 |
CN203307111U (en) * | 2013-05-06 | 2013-11-27 | 江苏正本净化节水科技实业有限公司 | Biological aerated filter |
CN103626360A (en) * | 2013-11-22 | 2014-03-12 | 华南理工大学 | Advanced treatment method of integrated catalytic ozonation-biological aerated filter water |
Cited By (3)
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 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101376556B (en) | Ozone oxidation sterilizing and downflow type aerating biological filter combined waste water treatment apparatus | |
CN101219848A (en) | A method and device for deep purification of drinking water | |
CN102180556A (en) | Adsorption regeneration-photocatalysis advanced oxidation water treatment equipment | |
CN102515432A (en) | A method for removing algae toxins and odor substances in high-algae water source water | |
CN101323493A (en) | A wastewater treatment device based on ozone oxidation and biological aerated filter | |
CN201240972Y (en) | Waste water advanced treatment apparatus combining ozone oxidation and downflow type aerating biological filter pool | |
CN201292263Y (en) | Vertical flow type aerobic gas float filter chamber | |
CN104150657B (en) | A device and method for advanced treatment of tertiary effluent of sewage | |
CN102701544A (en) | External-mounting photocatalytic - biological fluidized bed reactor | |
CN101638285A (en) | Sewage purification processing system | |
CN104150656B (en) | Nanometer aeration condenses-stirs the apparatus and method of flocculating and purifying biological treatment of sewage | |
CN103964645B (en) | A kind of integrated deep water treatment device | |
CN104045206A (en) | UV/O3+BAF combined advanced oxidation sewage treatment equipment | |
CN104276722B (en) | Tail water carries mark system | |
CN104071952B (en) | A kind of breeding wastewater biochemical film processing method | |
CN206318832U (en) | Sewage treatment unit | |
CN205653303U (en) | Hospital passes catch disease district sewage treatment plant | |
CN101817616B (en) | Biologic unit combined treatment method for improving biological stability of drinking water quality | |
CN204342609U (en) | A kind of refractory organic industrial sewage treatment system | |
CN103723882A (en) | Ship wastewater treatment method and device | |
CN102807299A (en) | Method for treatment and reuse of dimethyl ether production waste water, and special apparatus thereof | |
CN204310916U (en) | Petrochemical wastewater advanced treatment system | |
CN203820587U (en) | Wastewater treatment device for pharmaceutical factory | |
CN108423883A (en) | The method and apparatus of hydroxyl radical free radical degradation mineralising quinolone antibiotics | |
CN210528675U (en) | Municipal sewage treatment system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20140917 |