CN103803695A - Method of Fenton-like photocatalytic reaction system coupled with zero-valent iron and TiO2 photocatalysis - Google Patents
Method of Fenton-like photocatalytic reaction system coupled with zero-valent iron and TiO2 photocatalysis Download PDFInfo
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- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 title claims abstract description 92
- 238000000034 method Methods 0.000 title claims abstract description 27
- 238000013032 photocatalytic reaction Methods 0.000 title claims abstract description 23
- 230000001699 photocatalysis Effects 0.000 title claims description 25
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 title description 6
- 238000007146 photocatalysis Methods 0.000 title description 4
- 238000006243 chemical reaction Methods 0.000 claims abstract description 72
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 42
- 229910010413 TiO 2 Inorganic materials 0.000 claims abstract description 39
- 239000002351 wastewater Substances 0.000 claims abstract description 35
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 24
- 239000003054 catalyst Substances 0.000 claims abstract description 23
- 239000011521 glass Substances 0.000 claims abstract description 21
- 238000005273 aeration Methods 0.000 claims abstract description 15
- 239000003344 environmental pollutant Substances 0.000 claims description 15
- 231100000719 pollutant Toxicity 0.000 claims description 15
- 229910021578 Iron(III) chloride Inorganic materials 0.000 claims description 12
- 239000000084 colloidal system Substances 0.000 claims description 12
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 claims description 12
- 239000010919 dye waste Substances 0.000 claims description 9
- 229960004887 ferric hydroxide Drugs 0.000 claims description 9
- IEECXTSVVFWGSE-UHFFFAOYSA-M iron(3+);oxygen(2-);hydroxide Chemical compound [OH-].[O-2].[Fe+3] IEECXTSVVFWGSE-UHFFFAOYSA-M 0.000 claims description 9
- 238000005189 flocculation Methods 0.000 claims description 8
- 230000016615 flocculation Effects 0.000 claims description 8
- 239000010865 sewage Substances 0.000 claims description 8
- 230000008878 coupling Effects 0.000 claims description 7
- 238000010168 coupling process Methods 0.000 claims description 7
- 238000005859 coupling reaction Methods 0.000 claims description 7
- 238000001556 precipitation Methods 0.000 claims description 7
- 239000010419 fine particle Substances 0.000 claims description 6
- 239000012535 impurity Substances 0.000 claims description 6
- 230000008569 process Effects 0.000 claims description 4
- 239000002253 acid Substances 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 3
- 238000005516 engineering process Methods 0.000 description 21
- 239000000243 solution Substances 0.000 description 18
- 229910052742 iron Inorganic materials 0.000 description 7
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 6
- 230000003647 oxidation Effects 0.000 description 6
- 238000007254 oxidation reaction Methods 0.000 description 6
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 6
- 230000002378 acidificating effect Effects 0.000 description 5
- VTLYFUHAOXGGBS-UHFFFAOYSA-N Fe3+ Chemical compound [Fe+3] VTLYFUHAOXGGBS-UHFFFAOYSA-N 0.000 description 4
- 230000003197 catalytic effect Effects 0.000 description 4
- 229910001447 ferric ion Inorganic materials 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- 230000009471 action Effects 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 238000004088 simulation Methods 0.000 description 3
- 239000012028 Fenton's reagent Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000003673 groundwater Substances 0.000 description 2
- MGZTXXNFBIUONY-UHFFFAOYSA-N hydrogen peroxide;iron(2+);sulfuric acid Chemical compound [Fe+2].OO.OS(O)(=O)=O MGZTXXNFBIUONY-UHFFFAOYSA-N 0.000 description 2
- -1 iron ions Chemical class 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- LQNUZADURLCDLV-UHFFFAOYSA-N nitrobenzene Chemical compound [O-][N+](=O)C1=CC=CC=C1 LQNUZADURLCDLV-UHFFFAOYSA-N 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 238000005215 recombination Methods 0.000 description 2
- 230000006798 recombination Effects 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000002195 synergetic effect Effects 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- 239000003513 alkali Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000004042 decolorization Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000409 membrane extraction Methods 0.000 description 1
- 238000000120 microwave digestion Methods 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 238000007619 statistical method Methods 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
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Abstract
本发明提供一种零价铁与TiO2光催化耦合的类芬顿光催化反应体系的方法,该方法步骤:配制1L浓度为10mg/L-100mg/L的模拟染料废水置于玻璃容器中,向该模拟染料废水中加入0.1g-2g Fe0,用浓度为1mol/L的HCl溶液调节所述模拟染料废水的pH=3,然后向所述染料废水中投加1g/L的TiO2催化剂,开启λ=254nm的紫外灯,将盛有模拟染料废水的玻璃容器置于所述紫外灯下,开启曝气泵,采用玻璃容器底部曝气方式驱动混合反应体系中的HCl溶液、TiO2催化剂和模拟染料废水,反应结束后,关闭紫外灯和曝气泵,往反应体系中加入2-10ml浓度为1mol/L的NaOH溶液,静置沉淀30-60min。本发明的效果是可降低反应体系中35%-50%的色度和浊度,出水水质可达到(GB18918-2002)一级A标准的要求。The invention provides a method of a Fenton-like photocatalytic reaction system coupled with zero-valent iron and TiO photocatalytically, the method steps: preparing 1L of simulated dye wastewater with a concentration of 10mg/L-100mg/L and placing it in a glass container, Add 0.1g-2g Fe 0 to the simulated dye wastewater, adjust the pH of the simulated dye wastewater to 3 with HCl solution with a concentration of 1mol/L, and then add 1g/L TiO 2 catalyst to the dye wastewater , turn on the ultraviolet lamp of λ=254nm, place the glass container containing the simulated dye wastewater under the ultraviolet lamp, turn on the aeration pump, and use the aeration mode at the bottom of the glass container to drive the HCl solution and the TiO catalyst in the mixed reaction system With the simulated dye wastewater, after the reaction, turn off the UV lamp and the aeration pump, add 2-10ml of NaOH solution with a concentration of 1mol/L to the reaction system, and let it settle for 30-60min. The effect of the invention is that it can reduce the chroma and turbidity in the reaction system by 35%-50%, and the effluent water quality can meet the requirements of the first grade A standard (GB18918-2002).
Description
技术领域technical field
本发明涉及无机功能材料和光催化废水处理技术,特别是一种零价铁与TiO2光催化耦合的类芬顿光催化反应体系的方法。The invention relates to an inorganic functional material and a photocatalytic wastewater treatment technology, in particular to a method of a Fenton-like photocatalytic reaction system in which zero-valent iron and TiO2 are photocatalytically coupled.
背景技术Background technique
随着世界经济的高速发展和工业的兴起,社会对水的需求量日益增大,地球上可用的淡水资源越来越少,许多国家都面临着水资源短缺的危机。近年来水污染也是越来越严重,在1998年的环境监测报告中全国176条城市河段中,绝大多数河段受到不同程度的污染。且在全国120个城市的地下水水质监测数据资料的统计分析中,这些城市的地下水也受到不同程度的污染。因此,近年来涌现出了许多新型高效节能的水处理工艺,如:光催化法、微波消解法、膜萃取法等。在众多新型水处理技术中,TiO2光催化技术以其独特的优势迅速成为21世纪水处理技术领域研究的热点课题之一。随着TiO2光催化技术的深入研究,表明将TiO2光催化技术与很多高级氧化技术耦合能够有效解决TiO2光催化氧化技术的缺陷,新型协同技术会表现出更高的催化活性。With the rapid development of the world economy and the rise of industry, the society's demand for water is increasing day by day, and the fresh water resources available on the earth are becoming less and less. Many countries are facing the crisis of water shortage. In recent years, water pollution has also become more and more serious. According to the environmental monitoring report in 1998, among the 176 urban river sections in the country, most of the river sections were polluted to varying degrees. And in the statistical analysis of groundwater quality monitoring data in 120 cities across the country, the groundwater in these cities is also polluted to varying degrees. Therefore, many new high-efficiency and energy-saving water treatment processes have emerged in recent years, such as photocatalysis, microwave digestion, and membrane extraction. Among many new water treatment technologies, TiO 2 photocatalysis technology has rapidly become one of the hot topics in the field of water treatment technology research in the 21st century due to its unique advantages. With the in-depth research of TiO 2 photocatalytic technology, it is shown that the coupling of TiO 2 photocatalytic technology and many advanced oxidation technologies can effectively solve the defects of TiO 2 photocatalytic oxidation technology, and the new synergistic technology will show higher catalytic activity.
芬顿(Fenton)技术是一项较为成熟高效的高级氧化技术。该技术是以芬顿试剂进行化学氧化的废水处理方法,Fenton试剂是由H2O2和Fe2+混合而成的一种氧化能力很强的氧化剂,其氧化机理主要是在酸性条件下(一般pH<3.5),利用Fe2+作为H2O2的催化剂,生成具有很强氧化电性且反应活性很高的羟基自由基(·OH),羟基自由基在水溶液中与难降解有机物生成有机自由基使之结构破坏,最终氧化分解。同时Fe2+被氧化成Fe3+产生混凝沉淀,将大量有机物凝结而去除。芬顿氧化法可有效地处理含硝基苯、ABS等有机物的废水以及用于废水的脱色、除恶臭。Fenton technology is a relatively mature and efficient advanced oxidation technology. This technology is a waste water treatment method based on chemical oxidation of Fenton's reagent. Fenton's reagent is a kind of oxidizing agent with strong oxidizing ability mixed by H 2 O 2 and Fe 2+ . The oxidation mechanism is mainly under acidic conditions ( Generally pH<3.5), using Fe 2+ as a catalyst for H 2 O 2 to generate hydroxyl radicals (·OH) with strong oxidative electrical properties and high reactivity, and hydroxyl radicals are generated in aqueous solution with refractory organic matter Organic free radicals destroy its structure and eventually oxidize and decompose. At the same time, Fe 2+ is oxidized to Fe 3+ to produce coagulation and precipitation, and a large amount of organic matter is condensed and removed. Fenton oxidation can effectively treat wastewater containing nitrobenzene, ABS and other organic substances, and can be used for decolorization and deodorization of wastewater.
发明内容Contents of the invention
本发明的目的在于提供一种零价铁与TiO2催化耦合的类芬顿光催化反应体系的方法,将Fe0与TiO2光催化技术相耦合,在一定的环境中组合成类芬顿光催化技术,可有效改善了光催化技术的催化活性,提高污染物的去除效率和出水水质,减少了芬顿技术铁泥的产生。The purpose of the present invention is to provide a method for a Fenton-like photocatalytic reaction system coupled with zero-valent iron and TiO catalysis, by coupling Fe 0 with TiO 2 photocatalytic technology, and combining it into a Fenton- like photocatalytic reaction system in a certain environment. Catalytic technology can effectively improve the catalytic activity of photocatalytic technology, improve the removal efficiency of pollutants and the quality of effluent water, and reduce the generation of iron sludge in Fenton technology.
为实现上述目的,本发明的一种零价铁与TiO2光催化耦合的类芬顿光催化反应体系的方法,该方法包括以下步骤:In order to achieve the above object, a kind of zero-valent iron of the present invention and TiO The method for the Fenton - like photocatalytic reaction system of photocatalytic coupling, the method may further comprise the steps:
(1)配制1L浓度为10mg/L-100mg/L的模拟染料废水置于玻璃容器中,向该模拟染料废水中加入0.1g-2g Fe0,用浓度为1mol/L的HCl溶液调节所述模拟染料废水的pH=3,然后向所述染料废水中投加1g/L的TiO2催化剂,开启λ=254nm的紫外灯,将盛有模拟染料废水的玻璃容器置于所述紫外灯下,开启曝气泵,采用玻璃容器底部曝气方式驱动混合反应体系中的HCl溶液、TiO2催化剂和模拟染料废水,由此实现了类芬顿光催化反应;(1) Prepare 1L of simulated dye wastewater with a concentration of 10mg/L-100mg/L and place it in a glass container, add 0.1g-2g Fe 0 to the simulated dye wastewater, and adjust the The pH=3 of simulated dye waste water, then in described dye waste water, add the TiO of 1g/L Catalyst , turn on the ultraviolet lamp of λ=254nm, the glass container that fills simulated dye waste water is placed under described ultraviolet lamp, Turn on the aeration pump, and use the aeration method at the bottom of the glass container to drive the HCl solution, TiO 2 catalyst and simulated dye wastewater in the mixed reaction system, thereby realizing the Fenton-like photocatalytic reaction;
(2)在上述反应结束后,往反应体系中加入2-10ml浓度为1mol/L的NaOH溶液,后续NaOH溶液的加入既中和反应体系中的H+,还与反应体系中的Fe3+生成氢氧化铁胶体;反应体系中存在的Cl-和Fe3+生成了氯化铁,由于氯化铁和氢氧化铁胶体都具有絮凝作用,则促进反应体系中TiO2催化剂、染料分子及细小颗粒杂质的沉淀,出水水质可达到《城镇污水处理厂污染物排放标准》(GB18918-2002)一级A标准的要求。(2) After the above reaction is completed, add 2-10ml of NaOH solution with a concentration of 1mol/L to the reaction system, and the subsequent addition of NaOH solution not only neutralizes the H + in the reaction system, but also reacts with Fe 3+ in the reaction system Ferric hydroxide colloid is generated; Cl - and Fe 3+ present in the reaction system generate ferric chloride, and both ferric chloride and ferric hydroxide colloid have flocculation, which promotes the TiO 2 catalyst, dye molecules and fine particles in the reaction system With the precipitation of particulate impurities, the effluent water quality can meet the requirements of the first-level A standard of the "Pollutant Discharge Standards for Urban Sewage Treatment Plants" (GB18918-2002).
所述反应体系的pH在反应过程是动态调节过程,在反应过程中,始终使反应体系维持为pH=3的酸性介质。所述零价铁(Fe0)在反应结束之后剩余的铁单质可直接取出,与反应体系分离。The pH of the reaction system is a dynamic adjustment process during the reaction process, and the reaction system is always maintained as an acidic medium with pH=3 during the reaction process. The remaining elemental iron of the zero-valent iron (Fe 0 ) after the reaction is finished can be directly taken out and separated from the reaction system.
本发明的效果是:Effect of the present invention is:
1、本发明将Fe0与TiO2光催化技术相耦合,在一定的环境中组合成类芬顿光催化技术,可有效改善了光催化技术的催化活性,提高污染物的去除效率和出水水质,减少了芬顿技术铁泥的产生。1. The present invention couples Fe 0 with TiO 2 photocatalytic technology, and combines it into Fenton-like photocatalytic technology in a certain environment, which can effectively improve the catalytic activity of photocatalytic technology, improve the removal efficiency of pollutants and the quality of effluent water , reducing the generation of Fenton technology iron slime.
2、本发明在酸性体系中,Fe0会释放出来二价铁离子(Fe2+);部分Fe2+在氧气的作用下被氧化成三价铁离子(Fe3+)。因此,该类芬顿光催化反应体系中同时存在紫外光、TiO2催化剂、污染物、Fe2+和Fe3+。Fe0释放出的Fe2+及转化的Fe3+同TiO2光催化耦合;能够捕获TiO2光生电子,减少光生电子-空穴的复合,能够增强TiO2光催化作用;TiO2光催化反应产生的羟基自由基(·OH)与Fe0释放出的Fe2+及转化的Fe3+耦合,组成类芬顿反应体系,进一步提高对污染物的处理效率。2. In the acidic system of the present invention, Fe 0 will release ferric ions (Fe 2+ ); part of Fe 2+ is oxidized into ferric ions (Fe 3+ ) under the action of oxygen. Therefore, ultraviolet light, TiO 2 catalyst, pollutants, Fe 2+ and Fe 3+ exist in the Fenton-like photocatalytic reaction system. The Fe 2+ released by Fe 0 and the converted Fe 3+ are photocatalytically coupled with TiO 2 ; it can capture TiO 2 photogenerated electrons, reduce the recombination of photogenerated electrons and holes, and enhance the photocatalytic effect of TiO 2 ; the photocatalytic reaction of TiO 2 The generated hydroxyl radicals (·OH) couple with the Fe 2+ released from Fe 0 and the converted Fe 3+ to form a Fenton-like reaction system, which further improves the treatment efficiency of pollutants.
3、在Fe0与TiO2光催化协同作用体系内产生的铁离子与后续NaOH的添加产生絮凝作用,可降低反应体系中35%-50%的色度和浊度,出水水质可达到《城镇污水处理厂污染物排放标准》(GB18918-2002)一级A标准的要求。3. The iron ions produced in the Fe 0 and TiO 2 photocatalytic synergy system and the subsequent addition of NaOH produce flocculation, which can reduce the chromaticity and turbidity in the reaction system by 35%-50%, and the effluent water quality can reach the "urban Sewage Treatment Plant Pollutant Discharge Standards" (GB18918-2002) Class A standard requirements.
本发明的效果是零价铁(Fe0)与TiO2光催化协同作用对污染物的去除效率相对于单一的TiO2光催化作用提高了40%,其铁泥的产生量相较于芬顿技术减少了50%。The effect of the present invention is that the photocatalytic synergistic effect of zero-valent iron (Fe 0 ) and TiO 2 increases the removal efficiency of pollutants by 40% compared with that of a single TiO 2 photocatalytic effect, and the amount of iron sludge produced is compared with that of Fenton Technology reduced by 50%.
具体实施方式Detailed ways
结合下列实施例对本发明的零价铁与TiO2光催化耦合的类芬顿光催化反应体系的方法加以说明:The method of the Fenton-like photocatalytic reaction system coupled with the photocatalysis of zero-valent iron of the present invention and TiO2 is illustrated in conjunction with the following examples:
本发明零价铁与TiO2光催化耦合的类芬顿光催化反应体系的方法作用机理如下:The method action mechanism of the Fenton-like photocatalytic reaction system of the photocatalytic coupling of zero-valent iron and TiO of the present invention is as follows:
TiO2+hv(紫外光)→e-+h+ TiO 2 +hv(ultraviolet light)→e - +h +
e-+O2→·O2 - e - +O 2 →·O 2 -
·O2 -+H+→HOO··O 2 - +H + →HOO·
2HOO·→O2+H2O2 2HOO→O 2 +H 2 O 2
H2O2+·O2 -→·OH+OH-+O2 H 2 O 2 +·O 2 − →·OH+OH − +O 2
h++H2O→·OH+·H+ h + +H 2 O→·OH+·H +
h++OH-→·OHh + +OH - → OH
Fe0+2H+→Fe2++H2 Fe 0 +2H + →Fe 2+ +H 2
Fe2++O2→Fe3+ Fe 2+ +O 2 →Fe 3+
Fe2++H2O2→Fe3++·OH+OH- Fe 2+ +H 2 O 2 →Fe 3+ + OH+OH -
Fe3++·H2O2→·OOH·+Fe2++H+ Fe 3+ +·H 2 O 2 →·OOH·+Fe 2+ +H +
HOO·+H2O2·→H2O+·OH+O2 HOO·+H 2 O 2 ·→H 2 O+·OH+O 2
本发明的零价铁与TiO2光催化耦合的类芬顿光催化反应体系的方法是将零价铁(Fe0)与TiO2光催化技术耦合,在酸性体系中,零价铁(Fe0)会释放出来二价铁离子(Fe2+),部分Fe2+在氧气的作用下被氧化成三价铁离子(Fe3+)。因此,该类芬顿光催化反应体系中同时存在紫外光、TiO2催化剂、污染物、Fe2+和Fe3+。Fe0释放出的Fe2+及转化的Fe3+同TiO2光催化耦合;能够捕获TiO2光生电子,减少光生电子-空穴的复合,能够增强TiO2光催化作用;TiO2光催化反应产生的羟基自由基(·OH)与Fe0释放出的Fe2+及转化的Fe3+耦合,组成类芬顿反应体系,进一步提高对污染物的处理效率。并且,在Fe0与TiO2光催化协同作用体系内产生的铁离子经过加碱可产生成絮凝作用,可降低反应体系中35%-50%的色度和浊度,出水水质可达到《城镇污水处理厂污染物排放标准》(GB18918-2002)一级A标准的要求。The method of the Fenton-like photocatalytic reaction system of the photocatalytic coupling of zero-valent iron and TiO 2 of the present invention is to couple zero-valent iron (Fe 0 ) with TiO 2 photocatalytic technology, and in an acidic system, zero-valent iron (Fe 0 ) will release ferric ions (Fe 2+ ), and part of Fe 2+ will be oxidized to ferric ions (Fe 3+ ) under the action of oxygen. Therefore, ultraviolet light, TiO 2 catalyst, pollutants, Fe 2+ and Fe 3+ exist in the Fenton-like photocatalytic reaction system. The Fe 2+ released by Fe 0 and the converted Fe 3+ are photocatalytically coupled with TiO 2 ; they can capture the photogenerated electrons of TiO 2 , reduce the recombination of photogenerated electrons and holes, and enhance the photocatalytic effect of TiO 2 ; the photocatalytic reaction of TiO 2 The generated hydroxyl radicals (·OH) couple with the Fe 2+ released from Fe 0 and the converted Fe 3+ to form a Fenton-like reaction system, which further improves the treatment efficiency of pollutants. Moreover, the iron ions produced in the photocatalytic synergy system of Fe 0 and TiO 2 can produce flocculation after adding alkali, which can reduce the chromaticity and turbidity in the reaction system by 35%-50%, and the effluent water quality can reach "urban Sewage Treatment Plant Pollutant Discharge Standards" (GB18918-2002) Class A standard requirements.
本发明的零价铁与TiO2光催化耦合的类芬顿光催化反应体系的方法,该方法包括以下步骤:Zero-valent iron of the present invention and TiO The method for the Fenton - like photocatalytic reaction system of photocatalytic coupling, the method comprises the following steps:
(1)配制1L浓度为10mg/L-100mg/L的模拟染料废水置于玻璃容器中,向该模拟染料废水中加入0.1g-2g Fe0,用浓度为1mol/L的HCl溶液调节所述模拟染料废水的pH=3,然后向所述染料废水中投加1g/L的TiO2催化剂,开启λ=254nm的紫外灯,将盛有模拟染料废水的玻璃容器置于所述紫外灯下,开启曝气泵,采用玻璃容器底部曝气方式驱动混合反应体系中的HCl溶液、TiO2催化剂和模拟染料废水,由此实现了类芬顿光催化反应;(1) Prepare 1L of simulated dye wastewater with a concentration of 10mg/L-100mg/L and place it in a glass container, add 0.1g-2g Fe 0 to the simulated dye wastewater, and adjust the The pH=3 of simulated dye waste water, then in described dye waste water, add the TiO of 1g/L Catalyst , turn on the ultraviolet lamp of λ=254nm, the glass container that fills simulated dye waste water is placed under described ultraviolet lamp, Turn on the aeration pump, and use the aeration method at the bottom of the glass container to drive the HCl solution, TiO 2 catalyst and simulated dye wastewater in the mixed reaction system, thereby realizing the Fenton-like photocatalytic reaction;
(2)在上述反应结束后,往反应体系中加入2-10ml浓度为1mol/L的NaOH溶液,后续NaOH溶液的加入既中和反应体系中的H+,还与反应体系中的Fe3+生成氢氧化铁胶体;反应体系中存在的Cl-和Fe3+生成了氯化铁,由于氯化铁和氢氧化铁胶体都具有絮凝作用,则促进反应体系中TiO2催化剂、染料分子及细小颗粒杂质的沉淀,可降低反应体系中35%-50%的色度和浊度,出水水质可达到《城镇污水处理厂污染物排放标准》(GB18918-2002)一级A标准的要求。(2) After the above reaction is completed, add 2-10ml of NaOH solution with a concentration of 1mol/L to the reaction system, and the subsequent addition of NaOH solution not only neutralizes the H + in the reaction system, but also reacts with Fe 3+ in the reaction system Ferric hydroxide colloid is generated; Cl - and Fe 3+ present in the reaction system generate ferric chloride, and both ferric chloride and ferric hydroxide colloid have flocculation, which promotes the TiO 2 catalyst, dye molecules and fine particles in the reaction system The precipitation of particulate impurities can reduce the chromaticity and turbidity in the reaction system by 35%-50%, and the effluent water quality can meet the requirements of the first-level A standard of the "Pollutant Discharge Standards for Urban Sewage Treatment Plants" (GB18918-2002).
所述反应体系的pH在反应过程是动态调节过程,在反应过程中,始终使反应体系维持为pH=3的酸性介质。所述零价铁(Fe0)在反应结束之后剩余的铁单质可直接取出,与反应体系分离。The pH of the reaction system is a dynamic adjustment process during the reaction process, and the reaction system is always maintained as an acidic medium with pH=3 during the reaction process. The remaining elemental iron of the zero-valent iron (Fe 0 ) after the reaction is finished can be directly taken out and separated from the reaction system.
实施例1:Example 1:
(1)配制1L浓度为10mg/L的模拟染料废水置于体积V大于1L的玻璃容器中,向该模拟染料废水中加入0.1gFe0,用浓度为1mol/L的HCl溶液调节该模拟染料废水的pH=3,然后向该染料废水中投加1g/L的TiO2催化剂。开启λ=254nm的紫外灯,将盛有模拟染料废水的玻璃容器置于紫外光环境中,开启曝气泵,采用玻璃容器底部曝气方式驱动混合反应体系中的HCl溶液、TiO2催化剂和模拟染料废水,由此实现了类芬顿光催化反应。(1) Prepare 1L of simulated dye wastewater with a concentration of 10mg/L and place it in a glass container with a volume V greater than 1L, add 0.1gFe 0 to the simulated dye wastewater, and adjust the simulated dye wastewater with a concentration of 1mol/L HCl solution pH = 3, and then add 1g/L of TiO 2 catalyst to the dye wastewater. Turn on the ultraviolet lamp at λ=254nm, place the glass container containing the simulated dye wastewater in the ultraviolet light environment, turn on the aeration pump, and use the aeration method at the bottom of the glass container to drive the HCl solution, TiO 2 catalyst and simulation in the mixed reaction system. Dye wastewater, thereby realizing a Fenton-like photocatalytic reaction.
(2)在上述反应结束后,往反应体系中加入2ml浓度为1mol/L的NaOH溶液,后续NaOH溶液的加入既中和反应体系中的H+,还与反应体系中的Fe3+生成氢氧化铁胶体;反应体系中存在的Cl-和Fe3+生成了氯化铁,氯化铁和氢氧化铁胶体都具有絮凝作用,可有效的促进反应体系中TiO2催化剂、染料分子及细小颗粒杂质的沉淀,可降低反应体系中35%-50%的色度和浊度,出水水质可达到《城镇污水处理厂污染物排放标准》(GB18918-2002)一级A标准的要求。(2) After the above reaction is completed, add 2ml of NaOH solution with a concentration of 1mol/L to the reaction system, and the subsequent addition of NaOH solution will not only neutralize the H + in the reaction system, but also generate hydrogen with Fe 3+ in the reaction system Iron oxide colloid; Cl - and Fe 3+ present in the reaction system generate ferric chloride, and both ferric chloride and ferric hydroxide colloid have flocculation, which can effectively promote TiO 2 catalyst, dye molecules and fine particles in the reaction system The precipitation of impurities can reduce the chromaticity and turbidity in the reaction system by 35%-50%, and the effluent water quality can meet the requirements of the first-level A standard of "Pollutant Discharge Standards for Urban Sewage Treatment Plants" (GB18918-2002).
实施例2:Example 2:
(1)配制1L浓度为50mg/L的模拟染料废水置于体积V大于1L的玻璃容器中,向该模拟染料废水中加入1g Fe0,用浓度为1mol/L的HCl溶液调节该模拟染料废水的pH=3,然后向该染料废水中投加1g/L的TiO2催化剂。开启λ=254nm的紫外灯,将盛有模拟染料废水的玻璃容器置于紫外光环境中,开启曝气泵,采用玻璃容器底部曝气方式驱动混合反应体系中的HCl溶液、TiO2催化剂和模拟染料废水,由此实现了类芬顿光催化反应。(1) Prepare 1L of simulated dye wastewater with a concentration of 50mg/L and place it in a glass container with a volume V greater than 1L, add 1g Fe 0 to the simulated dye wastewater, and adjust the simulated dye wastewater with a concentration of 1mol/L HCl solution pH = 3, and then add 1g/L of TiO 2 catalyst to the dye wastewater. Turn on the ultraviolet lamp at λ=254nm, place the glass container containing the simulated dye wastewater in the ultraviolet light environment, turn on the aeration pump, and use the aeration method at the bottom of the glass container to drive the HCl solution, TiO 2 catalyst and simulation in the mixed reaction system. Dye wastewater, thereby realizing a Fenton-like photocatalytic reaction.
(2)在上述反应结束后,往反应体系中加入5ml浓度为1mol/L的NaOH溶液,后续NaOH溶液的加入既中和反应体系中的H+,还与反应体系中的Fe3+生成氢氧化铁胶体;反应体系中存在的Cl-和Fe3+生成了氯化铁,氯化铁和氢氧化铁胶体都具有絮凝作用,可有效的促进反应体系中TiO2催化剂、染料分子及细小颗粒杂质的沉淀,从而降低反应体系35%的色度和浊度,出水水质可达到《城镇污水处理厂污染物排放标准》(GB18918-2002)一级A标准的要求。(2) After the above reaction is completed, add 5ml of NaOH solution with a concentration of 1mol/L to the reaction system, and the subsequent addition of NaOH solution will not only neutralize the H + in the reaction system, but also generate hydrogen with Fe 3+ in the reaction system Iron oxide colloid; Cl - and Fe 3+ present in the reaction system generate ferric chloride, and both ferric chloride and ferric hydroxide colloid have flocculation, which can effectively promote TiO 2 catalyst, dye molecules and fine particles in the reaction system Precipitation of impurities, thereby reducing the chromaticity and turbidity of the reaction system by 35%, and the quality of the effluent water can meet the requirements of the first-class A standard of the "Pollutant Discharge Standards for Urban Sewage Treatment Plants" (GB18918-2002).
实施例3:Example 3:
(1)配制1L浓度为100mg/L的模拟染料废水置于体积V大于1L的玻璃容器中,向该模拟染料废水中加入2g Fe0,用浓度为1mol/L的HCl溶液调节该模拟染料废水的pH=3,然后向该染料废水中投加1g/L的TiO2催化剂。开启λ=254nm的紫外灯,将盛有模拟染料废水的玻璃容器置于紫外光环境中,开启曝气泵,采用玻璃容器底部曝气方式驱动混合反应体系中的HCl溶液、TiO2催化剂和模拟染料废水,由此实现了类芬顿光催化反应。(1) Prepare 1L of simulated dye wastewater with a concentration of 100mg/L and place it in a glass container with a volume V greater than 1L, add 2g Fe 0 to the simulated dye wastewater, and adjust the simulated dye wastewater with a concentration of 1mol/L HCl solution pH = 3, and then add 1g/L of TiO 2 catalyst to the dye wastewater. Turn on the ultraviolet lamp at λ=254nm, place the glass container containing the simulated dye wastewater in the ultraviolet light environment, turn on the aeration pump, and use the aeration method at the bottom of the glass container to drive the HCl solution, TiO 2 catalyst and simulation in the mixed reaction system. Dye wastewater, thereby realizing a Fenton-like photocatalytic reaction.
(2)在上述反应结束后,往反应体系中加入10ml浓度为1mol/L的NaOH溶液,后续NaOH溶液的加入既中和反应体系中的H+,还与反应体系中的Fe3+生成氢氧化铁胶体;反应体系中存在的Cl-和Fe3+生成了氯化铁,氯化铁和氢氧化铁胶体都具有絮凝作用,可有效的促进反应体系中TiO2催化剂、染料分子及细小颗粒杂质的沉淀,从而降低反应体系50%的色度和浊度,出水水质可达到《城镇污水处理厂污染物排放标准》(GB18918-2002)一级A标准的要求。(2) After the above reaction is completed, add 10ml of NaOH solution with a concentration of 1mol/L to the reaction system, and the subsequent addition of NaOH solution will not only neutralize the H + in the reaction system, but also generate hydrogen with Fe 3+ in the reaction system Iron oxide colloid; Cl - and Fe 3+ present in the reaction system generate ferric chloride, and both ferric chloride and ferric hydroxide colloid have flocculation, which can effectively promote TiO 2 catalyst, dye molecules and fine particles in the reaction system Precipitation of impurities, thereby reducing the chromaticity and turbidity of the reaction system by 50%, and the quality of the effluent can meet the requirements of the first-level A standard of the "Pollutant Discharge Standard for Urban Sewage Treatment Plants" (GB18918-2002).
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