CN103586083A - Preparation method of nonhomogeneous Fenton reagent - Google Patents

Preparation method of nonhomogeneous Fenton reagent Download PDF

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CN103586083A
CN103586083A CN201310467357.6A CN201310467357A CN103586083A CN 103586083 A CN103586083 A CN 103586083A CN 201310467357 A CN201310467357 A CN 201310467357A CN 103586083 A CN103586083 A CN 103586083A
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陶庭先
王洁
吴之传
戴军森
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Anhui Polytechnic University
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Abstract

本发明公开了一种非均相Fenton试剂的制备方法,包括以下步骤:a、将载体纤维置于金属盐溶液中40-90℃水浴;b、加入碱调节pH至碱性,生成氢氧化物,洗涤,抽滤;c、将滤出的固体置于烘箱内加热2-12h,冷却至室温,即可得到所需非均相Fenton试剂,本发明所制备的Fenton试剂,直接用于染料溶液的光降解实验中,成功解决了传统的Fenton试剂,试剂投放量大,回收分离困难,活性组分流失,二次污染严重的问题。可适用于大规模生产,有广泛的应用前景。

Figure 201310467357

The invention discloses a preparation method of heterogeneous Fenton's reagent, which comprises the following steps: a. placing the carrier fiber in a metal salt solution in a water bath at 40-90°C; b. adding alkali to adjust the pH to alkaline to generate hydroxide , washing, and suction filtration; c, the filtered solid is placed in an oven and heated for 2-12h, and cooled to room temperature to obtain the required heterogeneous Fenton reagent. The Fenton reagent prepared by the present invention is directly used in dye solution In the photodegradation experiment, the problems of the traditional Fenton reagent, large dosage of reagent, difficult recovery and separation, loss of active components and serious secondary pollution were successfully solved. It is suitable for mass production and has wide application prospects.

Figure 201310467357

Description

一种非均相Fenton试剂的制备方法A kind of preparation method of heterogeneous phase Fenton's reagent

技术领域:Technical field:

本发明属于复合材料制备技术领域,特别涉及一种非均相Fenton试剂的制备方法。 The invention belongs to the technical field of composite material preparation, in particular to a preparation method of heterogeneous Fenton reagent.

背景技术:Background technique:

Fenton反应作为一种高级的化学氧化技术,实质是使用Fe2+和H2O2组成的Fenton试剂,通过反应产生的具有强氧化性的HO·来氧化降解废水中的有机物。因为可以高效的处理各种高浓度,难降解的有机废水,成为环境水处理越来越重要的方法。但是传统的均相Fenton法有不可避免的缺点:第一、试剂投入量大,未完全反应Fe2+在反应结束后形成铁泥,不仅浪费了大量化学药品也在反应结束后形成二次污染;第二,反应需要在酸性条件下进行,不仅增加了反应工艺也对反应设备有一定的腐蚀;第三,均相Fenton法下催化剂回收困难。为了克服这些缺点,现有技术对传统的Fenton法进行了改良,目前研究最多的是在均相Fenton法的基础上,利用物理吸附的原理对活性组分的固定化,但是在反应中仍然需要通过加酸调节pH,才能使反应体系有较大的降解效果,对设备腐蚀严重,二次污染严重。尤其是催化活性组分流失问题依然存在。 As an advanced chemical oxidation technology, the Fenton reaction essentially uses the Fenton reagent composed of Fe 2+ and H 2 O 2 to oxidize and degrade organic matter in wastewater through the HO with strong oxidizing properties produced by the reaction. Because it can efficiently treat various high-concentration and refractory organic wastewater, it has become an increasingly important method for environmental water treatment. However, the traditional homogeneous Fenton method has unavoidable shortcomings: first, the amount of reagent input is large, and iron sludge is formed after the incomplete reaction of Fe 2+ after the reaction, which not only wastes a lot of chemicals but also causes secondary pollution after the reaction ; Second, the reaction needs to be carried out under acidic conditions, which not only increases the reaction process but also corrodes the reaction equipment to a certain extent; third, it is difficult to recover the catalyst under the homogeneous Fenton method. In order to overcome these shortcomings, the existing technology has improved the traditional Fenton method. At present, the most researched method is based on the homogeneous Fenton method, using the principle of physical adsorption to immobilize the active components, but in the reaction still needs Only by adding acid to adjust the pH can the reaction system have a greater degradation effect, which will seriously corrode the equipment and cause serious secondary pollution. In particular, the problem of loss of catalytically active components still exists.

发明内容:Invention content:

本发明为了解决催化活性组分流失和酸液腐蚀设备,针对性的提出一种非均相Fenton试剂的制备方法。将具有配位功能的载体纤维浸在金属盐溶液中,利用配位沉淀法将金属氧化物沉积在纤维表面形成非均相Fenton试剂。该制备方法简单,适用于规模化生产。 In order to solve the loss of catalytically active components and acid solution corrosion equipment, the present invention specifically proposes a preparation method of a heterogeneous Fenton reagent. The carrier fiber with coordination function is immersed in the metal salt solution, and the metal oxide is deposited on the surface of the fiber by the coordination precipitation method to form a heterogeneous Fenton reagent. The preparation method is simple and suitable for large-scale production.

本发明提供的一种的非均相Fenton试剂的制备方法,包括以下步骤: A kind of preparation method of the heterogeneous Fenton's reagent provided by the invention comprises the following steps:

步骤一、将载体纤维置于金属盐溶液中40-90 ℃水浴,得到金属离子负载纤维; Step 1, placing the carrier fiber in a metal salt solution in a water bath at 40-90°C to obtain a metal ion-loaded fiber;

步骤二、加入碱液调节pH至碱性,生成氢氧化物,洗涤,抽滤,得到金属氢氧化物负载纤维; Step 2, adding lye to adjust the pH to alkaline, generating hydroxide, washing, and suction filtration to obtain metal hydroxide-loaded fibers;

步骤三、将滤出的固体置于烘箱内加热2-12 h,冷却至室温,得到金属氧化物负载纤维,即非均相Fenton试剂。 Step 3: Heat the filtered solid in an oven for 2-12 h, and cool to room temperature to obtain metal oxide-loaded fibers, namely heterogeneous Fenton reagent.

所述的载体纤维为具有强配位能力的腈纶螯合纤维。 The carrier fiber is an acrylic chelate fiber with strong coordination ability.

所述的金属盐溶液是含有Fe3+,Cu2+中的任意一种金属离子配置的浓度为0.05-0.11 mol/L的水溶液。 The metal salt solution is an aqueous solution containing any one of Fe 3+ and Cu 2+ metal ions with a concentration of 0.05-0.11 mol/L.

所述的碱液可以是氢氧化钠,氢氧化钾,氨水中的任意一种。 Described lye can be sodium hydroxide, potassium hydroxide, any one in ammoniacal liquor.

所述的金属氢氧化物是氢氧化铁,氢氧化铜的任意一种。 Described metal hydroxide is iron hydroxide, any one of copper hydroxide.

所述的金属氧化物为氧化铁,氧化铜的任意一种。 The metal oxide is any one of iron oxide and copper oxide.

腈纶螯合纤维将具有催化功能的纳米金属氧化物负载在纤维表面。纳米结构的催化剂因为具有较大的比表面积而表现出较大的催化活性;与载体纤维配位方式结合,结合牢固,有效地避免催化剂随水体流失,也方便回收利用。利用具有配位功能的腈纶螯合纤维作为载体,廉价易得,性质稳定,无毒无害,可多次重复使用,节约能源,不产生二次污染。 The acrylic chelating fiber loads nanometer metal oxides with catalytic function on the surface of the fiber. The nanostructured catalyst exhibits greater catalytic activity due to its larger specific surface area; it is combined with the carrier fiber in a coordinated manner, and the combination is firm, which effectively prevents the loss of the catalyst with the water body and is also convenient for recycling. The acrylic chelate fiber with coordination function is used as a carrier, which is cheap and easy to obtain, stable in nature, non-toxic and harmless, can be reused many times, saves energy, and does not produce secondary pollution.

将制备出的非均相Fenton试剂用于染料的光-Fenton催化降解实验,具体步骤:在光催化反应仪中,将制备好的非均相Fenton试剂加入到染料和H2O2的混合溶液中,进行光-Fenton反应,通过比较反应前后染料的吸光度的变化计算降解率来判断催化剂的活性和染料的降解程度。 The prepared heterogeneous Fenton reagent is used in the photo-Fenton catalytic degradation experiment of dyes. The specific steps are: in the photocatalytic reaction apparatus, the prepared heterogeneous Fenton reagent is added to the mixed solution of dye and H 2 O 2 In the photo-Fenton reaction, the degradation rate is calculated by comparing the change of the absorbance of the dye before and after the reaction to judge the activity of the catalyst and the degree of degradation of the dye.

本方法制备的非均相Fenton试剂,对50 mg/L的活性红,活性黄,甲基橙三种染料进行光催化降解研究表明,在不需要酸液调节pH的情况下,在中性条件下即可反应,操作更加简单,对设备的腐蚀性减小,并且对三种水溶性染料的降解率都能达到98%以上;非均相Fenton通过简单的过滤就可以实现催化剂的回收问题,可以重复循环使用多次,有效的防止了催化剂活性组分的流失问题,实现了在低温(10-25 ℃)常压下对染料溶液的绿色高效降解。该技术发明为低成本降解染料废水提供了一种新的参考。 The heterogeneous Fenton reagent prepared by this method, the photocatalytic degradation research of 50 mg/L reactive red, reactive yellow, and methyl orange three dyes showed that under neutral conditions, no acid solution was needed to adjust the pH The reaction can be carried out immediately, the operation is simpler, the corrosion to the equipment is reduced, and the degradation rate of the three water-soluble dyes can reach more than 98%; the heterogeneous Fenton can realize the recovery of the catalyst through simple filtration, It can be reused many times, effectively preventing the loss of catalyst active components, and realizing the green and efficient degradation of dye solution at low temperature (10-25 °C) and normal pressure. This technical invention provides a new reference for low-cost degradation of dye wastewater.

附图说明:Description of drawings:

图1 Fe3+的浓度对催化剂活性的影响图; Figure 1 Effect diagram of the concentration of Fe 3+ on the catalyst activity;

图2 水浴温度对催化剂活性的影响图; Fig. 2 The effect diagram of water bath temperature on catalyst activity;

图3 烘干时间对催化剂活性的影响图; Fig. 3 The impact diagram of drying time on catalyst activity;

图4 Fe2O3/腈纶螯合纤维对活性红染料的降解效果图; Figure 4 Fe 2 O 3 / acrylic chelate fiber degradation effect diagram of reactive red dye;

图5 Fe2O3/腈纶螯合纤维催化剂的重复使用性; Figure 5 Fe 2 O 3 / the reusability of acrylic fiber chelate fiber catalyst;

图6 Fe2O3/腈纶螯合纤维催化剂的普遍适用性; The universal applicability of Fig. 6 Fe 2 O 3 / acrylic fiber chelate fiber catalyst;

图7 CuO/腈纶螯合纤维对活性红染料的降解效果图; Figure 7 CuO/acrylic chelate fiber degradation effect diagram of reactive red dye;

图8 非均相Fenton试剂的电镜照片:(a) Fe2O3/腈纶螯合纤维,(b) CuO/腈纶螯合纤维; Figure 8 Electron micrographs of heterogeneous Fenton reagent: (a) Fe 2 O 3 /acrylic chelate fiber, (b) CuO/acrylic chelate fiber;

图9非均相光-Fenton催化降解染料示意图。 Fig. 9 Schematic diagram of heterogeneous photo-Fenton catalytic degradation of dyes.

具体实施方案 specific implementation plan

实施例1:非均相Fenton试剂——Fe2O3/腈纶螯合纤维的制备 Embodiment 1: the preparation of heterogeneous Fenton's reagent---Fe 2 O 3 / acrylic fiber chelate fiber

将0.50 g载体纤维置于50 mL的Fe3+溶液中,70 ℃水浴下配位反应3 h,得到Fe3+-腈纶螯合纤维;加入碱液调节pH至碱性,生成Fe(OH)3/腈纶螯合纤维;洗涤,抽滤,将滤出的固体置于烘箱内加热分解,冷却至室温,得到Fe2O3/腈纶螯合纤维催化剂。 Put 0.50 g of carrier fibers in 50 mL of Fe 3+ solution, and perform a coordination reaction in a water bath at 70 °C for 3 h to obtain Fe 3+ -acrylic fiber chelate fibers; add lye to adjust the pH to alkaline to generate Fe(OH) 3 /Acrylic chelate fiber; washing, suction filtration, heating and decomposing the filtered solid in an oven, cooling to room temperature to obtain Fe 2 O 3 /acrylic chelate fiber catalyst.

研究不同浓度的Fe3+制备出的Fenton试剂的催化活性的影响。保持其他制备条件不变,调节Fe3+的浓度范围从0.05 mol/L~0.11 mol/L制备出的催化剂对活性红染料进行光Fenton催化降解实验,计算降解率结果如图1所示。由图可知,由0.10 mol/L的Fe3+溶液制备出的Fenton试剂光催化效果最好,活性最高。 The effect of different concentrations of Fe 3+ on the catalytic activity of Fenton's reagent was studied. Keeping other preparation conditions unchanged, adjusting the concentration range of Fe 3+ from 0.05 mol/L to 0.11 mol/L, the prepared catalyst was subjected to the photo-Fenton catalytic degradation experiment of reactive red dye, and the calculated degradation rate results are shown in Figure 1. It can be seen from the figure that the Fenton reagent prepared from 0.10 mol/L Fe 3+ solution has the best photocatalytic effect and the highest activity.

实施例2:非均相Fenton试剂——Fe2O3/腈纶螯合纤维的制备 Embodiment 2: the preparation of heterogeneous Fenton's reagent---Fe 2 O 3 / acrylic fiber chelate fiber

如实施例1,不同之处在于水浴温度范围从40-90 ℃。光催化反应后,计算降解率结果如图2所示。由图可知,在70 ℃下制备出的Fenton试剂光催化效果最好,活性最高。 As in Example 1, the difference is that the temperature of the water bath ranges from 40-90°C. After the photocatalytic reaction, the calculated degradation rate results are shown in Figure 2. It can be seen from the figure that the Fenton reagent prepared at 70 °C has the best photocatalytic effect and the highest activity.

实施例3:非均相Fenton试剂——Fe2O3/腈纶螯合纤维的制备 Embodiment 3: the preparation of heterogeneous Fenton's reagent--- Fe2O3 /acrylic fiber chelate fiber

如实施例1,不同之处在于烘干时间范围从2-12 h。光催化反应后,计算降解率结果如图3所示。由图可知,在6 h下制备出的Fenton试剂光催化效果最好,活性最高。 As in Example 1, the difference is that the drying time ranges from 2-12 h. After the photocatalytic reaction, the calculated degradation rate results are shown in Figure 3. It can be seen from the figure that the Fenton reagent prepared under 6 h has the best photocatalytic effect and the highest activity.

实施例4:Fe2O3/腈纶螯合纤维对活性红染料的降解实验 Embodiment 4: Degradation experiment of Fe2O3 /acrylic fiber chelate fiber to reactive red dye

配置浓度为50 mg/L的活性红染料溶液,在最大吸收波长(λmax=530 nm)处,测得吸光度为A0,取30 mL染料溶液加入双氧水和0.03 gFe2O3/腈纶螯合纤维催化剂,混合均匀后,在光催化反应仪中进行,光源是300 W的Xe灯。同时进行对照实验。每隔20 min,在溶液的最大吸收波长处测定吸光度At,计算降解率D,降解率的计算公式D=(1-At/A0)×100%。将降解率随时间的变化关系列于图4中。由图可知活性红染料在100 min时的降解率就可以接近100%。 Prepare a reactive red dye solution with a concentration of 50 mg/L. At the maximum absorption wavelength (λ max =530 nm), the measured absorbance is A 0 . Take 30 mL of the dye solution and add hydrogen peroxide and 0.03 gFe 2 O 3 /acrylic chelate After the fiber catalyst is mixed evenly, it is carried out in a photocatalytic reactor, and the light source is a 300 W Xe lamp. At the same time, a control experiment was carried out. Every 20 minutes, measure the absorbance A t at the maximum absorption wavelength of the solution, and calculate the degradation rate D, the calculation formula of the degradation rate D=(1-A t /A 0 )×100%. The change relationship of the degradation rate with time is listed in Figure 4. It can be seen from the figure that the degradation rate of reactive red dye can be close to 100% in 100 min.

实施例5:Fe2O3/腈纶螯合纤维的重复使用性 Embodiment 5: the reusability of Fe 2 O 3 / acrylic fiber chelate fiber

准备一组染料浓度和双氧水含量完全相同的混合溶液,加入0.03 g Fe2O3/腈纶螯合纤维催化剂进行光催化反应。反应结束后,过滤分离并用蒸馏水洗涤催化剂,用于下一次的反应。实验结果见图5,由图可知,催化剂重复使用第7次时,染料的降解率仍在80%以上,说明本方法制备出的非均相Fenton试剂成功解决了催化活性组分的流失问题,可以通过简单过滤实现多次重复使用。 Prepare a group of mixed solutions with the same dye concentration and hydrogen peroxide content, and add 0.03 g Fe 2 O 3 /acrylic chelate fiber catalyst for photocatalytic reaction. After the reaction, the catalyst was separated by filtration and washed with distilled water for the next reaction. The experimental results are shown in Figure 5. It can be seen from the figure that when the catalyst is reused for the 7th time, the degradation rate of the dye is still above 80%, indicating that the heterogeneous Fenton reagent prepared by this method has successfully solved the problem of the loss of catalytically active components. It can be reused many times by simple filtering.

实施例6:Fe2O3/腈纶螯合纤维的普遍适用性 Embodiment 6: the universal applicability of Fe2O3 /acrylic chelate fiber

将0.03 g Fe2O3/腈纶螯合纤维催化剂分别用于降解活性黄,活性红和甲基橙染料溶液,实验结果如图6所示。由图可知,本方法制备出的催化剂对活性黄,活性红和甲基橙三种水溶性染料都能实现100%的降解,说明本方法制备出的非均相Fenton试剂具有高的催化活性。 0.03 g Fe 2 O 3 /acrylic chelate fiber catalyst was used to degrade reactive yellow, reactive red and methyl orange dye solutions respectively, and the experimental results are shown in Figure 6. As can be seen from the figure, the catalyst prepared by this method can achieve 100% degradation of reactive yellow, reactive red and methyl orange three water-soluble dyes, indicating that the heterogeneous Fenton reagent prepared by this method has high catalytic activity.

  the

实施例7:非均相Fenton试剂——CuO/腈纶螯合纤维的制备 Embodiment 7: the preparation of heterogeneous Fenton's reagent---CuO/acrylic fiber chelate fiber

将0.50 g载体纤维置于50 mL 0.10 mol/L的Cu2+溶液中,50 ℃水浴下配位反应2 h,得到Cu2+-腈纶螯合纤维;加入碱液调节pH至碱性,生成Cu (OH)2/腈纶螯合纤维;洗涤,抽滤,将滤出的固体置于烘箱内4 h加热,冷却至室温,得到CuO/腈纶螯合纤维催化剂。 Put 0.50 g of carrier fibers in 50 mL of 0.10 mol/L Cu 2+ solution, and perform a coordination reaction in a water bath at 50 °C for 2 h to obtain Cu 2+ -acrylic fiber chelate fibers; add lye to adjust the pH to alkaline, and generate Cu (OH) 2 /acrylic chelate fiber; washing, suction filtration, heating the filtered solid in an oven for 4 h, and cooling to room temperature to obtain CuO/acrylic chelate fiber catalyst.

  the

实施例8:CuO/腈纶螯合纤维对活性红染料的降解实验 Embodiment 8: Degradation experiment of CuO/acrylic fiber chelate fiber to reactive red dye

如实施例4,不同之处在于催化剂为CuO/腈纶螯合纤维,将降解率随时间的变化关系列于图7中。由图可知活性红染料在120 min时的降解率就可以接近100%。 As in Example 4, the difference is that the catalyst is CuO/acrylic chelate fiber, and the relationship of the degradation rate with time is shown in Figure 7. It can be seen from the figure that the degradation rate of reactive red dye can be close to 100% in 120 min.

Claims (6)

1. a preparation method for heterogeneous Fenton reagent, is characterized in that, the method comprises the following steps:
Step 1, carrier fibre is placed in to metal salt solution 40-90 ℃ water-bath, obtains metal ion carrying fiber;
Step 2, add alkali lye to regulate pH to alkalescence, generate hydroxide, washing, suction filtration, obtains metal hydroxides carrying fiber;
Step 3, the solid leaching is placed in baking oven and heats 2-12 h, be cooled to room temperature, obtain metal oxide supported fiber, i.e. heterogeneous Fenton reagent.
2. the preparation method who states according to step 1 in claim 1, is characterized in that: described carrier fibre is the acrylic fibers chelate fibre with strong coordination ability.
3. according to the preparation method described in step 1 in claim 1, it is characterized in that: described metal salt solution is to contain Fe 3+, Cu 2+in the concentration of any one metal ion configuration be the aqueous solution of 0.05-0.11 mol/L.
4. according to the preparation method described in step 2 in claim 1, it is characterized in that: described alkali lye can be NaOH, potassium hydroxide, any one in ammoniacal liquor.
5. according to the preparation method described in step 2 in claim 1, it is characterized in that: described metal hydroxides is iron hydroxide, any one of Kocide SD.
6. according to the preparation method described in step 3 in claim 1, it is characterized in that: described metal oxide is iron oxide, any one of cupric oxide.
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CN107983351A (en) * 2017-11-27 2018-05-04 中国地质大学(武汉) A kind of iron/copper bi-metal oxide and preparation method thereof
CN108855148A (en) * 2018-06-15 2018-11-23 宁夏宝塔化工中心实验室(有限公司) A kind of preparation method of compound soil type acidic catalyst
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CN112675910A (en) * 2021-01-11 2021-04-20 燕山大学 Amyloid fiber ferric hydroxide heterogeneous Fenton catalyst and preparation method and application thereof
CN113499789A (en) * 2021-04-09 2021-10-15 黑龙江大学 Preparation method of tungsten disulfide/Naberlite heterogeneous Fenton-like catalyst

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CN105312055A (en) * 2015-11-26 2016-02-10 江苏大学 Preparation method and application of Fenton-like catalyst
CN106552627A (en) * 2016-11-10 2017-04-05 浙江理工大学 A kind of preparation method and applications based on cupric oxide modified carbon fiber
CN106552627B (en) * 2016-11-10 2019-04-23 浙江理工大学 A kind of preparation method based on copper oxide modified carbon fiber and its application
CN107983351A (en) * 2017-11-27 2018-05-04 中国地质大学(武汉) A kind of iron/copper bi-metal oxide and preparation method thereof
CN108855148A (en) * 2018-06-15 2018-11-23 宁夏宝塔化工中心实验室(有限公司) A kind of preparation method of compound soil type acidic catalyst
CN109158105A (en) * 2018-09-16 2019-01-08 天津大学 Core-shell structure Fe3O4@Cu(OH)xThe synthetic method of magnetic nanoparticle
CN110227463A (en) * 2019-05-31 2019-09-13 浙江工业大学 A kind of novel fenton catalyst and preparation method thereof for degradable organic pollutant waste water
CN112675910A (en) * 2021-01-11 2021-04-20 燕山大学 Amyloid fiber ferric hydroxide heterogeneous Fenton catalyst and preparation method and application thereof
CN112675910B (en) * 2021-01-11 2022-03-25 燕山大学 Amyloid fiber ferric hydroxide heterogeneous Fenton catalyst and preparation method and application thereof
CN113499789A (en) * 2021-04-09 2021-10-15 黑龙江大学 Preparation method of tungsten disulfide/Naberlite heterogeneous Fenton-like catalyst

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