CN110743604B - Preparation method of organic sewage efficient photodegradation catalyst - Google Patents
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- 239000003054 catalyst Substances 0.000 title claims abstract description 49
- 238000001782 photodegradation Methods 0.000 title claims abstract description 28
- 239000010865 sewage Substances 0.000 title claims abstract description 21
- 238000002360 preparation method Methods 0.000 title claims abstract description 12
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims abstract description 54
- 229910000019 calcium carbonate Inorganic materials 0.000 claims abstract description 27
- JMANVNJQNLATNU-UHFFFAOYSA-N oxalonitrile Chemical compound N#CC#N JMANVNJQNLATNU-UHFFFAOYSA-N 0.000 claims abstract description 17
- NWONKYPBYAMBJT-UHFFFAOYSA-L zinc sulfate Chemical compound [Zn+2].[O-]S([O-])(=O)=O NWONKYPBYAMBJT-UHFFFAOYSA-L 0.000 claims abstract description 17
- 229960001763 zinc sulfate Drugs 0.000 claims abstract description 17
- 229910000368 zinc sulfate Inorganic materials 0.000 claims abstract description 17
- 238000003837 high-temperature calcination Methods 0.000 claims abstract description 12
- 238000000227 grinding Methods 0.000 claims abstract description 9
- 239000000843 powder Substances 0.000 claims abstract description 8
- 238000001816 cooling Methods 0.000 claims abstract description 7
- 239000002243 precursor Substances 0.000 claims abstract description 7
- 238000001027 hydrothermal synthesis Methods 0.000 claims abstract description 4
- 238000001035 drying Methods 0.000 claims abstract description 3
- 239000002002 slurry Substances 0.000 claims description 30
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 20
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 14
- 238000000034 method Methods 0.000 claims description 8
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical group F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 claims description 5
- 229910000040 hydrogen fluoride Inorganic materials 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 5
- -1 polytetrafluoroethylene Polymers 0.000 claims description 2
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims description 2
- 239000004810 polytetrafluoroethylene Substances 0.000 claims description 2
- 239000002351 wastewater Substances 0.000 claims 5
- 238000001704 evaporation Methods 0.000 claims 1
- 238000002156 mixing Methods 0.000 claims 1
- 238000007873 sieving Methods 0.000 claims 1
- LQNUZADURLCDLV-UHFFFAOYSA-N nitrobenzene Chemical compound [O-][N+](=O)C1=CC=CC=C1 LQNUZADURLCDLV-UHFFFAOYSA-N 0.000 abstract description 12
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 abstract description 6
- 239000011787 zinc oxide Substances 0.000 abstract description 3
- 238000011068 loading method Methods 0.000 abstract 1
- 229910052799 carbon Inorganic materials 0.000 description 4
- 239000003344 environmental pollutant Substances 0.000 description 4
- 235000011187 glycerol Nutrition 0.000 description 4
- 239000011941 photocatalyst Substances 0.000 description 4
- 231100000719 pollutant Toxicity 0.000 description 4
- 239000002131 composite material Substances 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000006731 degradation reaction Methods 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 239000002957 persistent organic pollutant Substances 0.000 description 2
- 230000001699 photocatalysis Effects 0.000 description 2
- 238000013033 photocatalytic degradation reaction Methods 0.000 description 2
- 230000027756 respiratory electron transport chain Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000032683 aging Effects 0.000 description 1
- 238000010504 bond cleavage reaction Methods 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000004408 titanium dioxide Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
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- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/24—Nitrogen compounds
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Abstract
Description
技术领域technical field
本发明涉及光降解催化剂技术领域,尤其涉及一种有机污水高效光降解催化剂的制备方法。The invention relates to the technical field of photodegradation catalysts, in particular to a preparation method of a high-efficiency photodegradation catalyst for organic sewage.
背景技术Background technique
光催化降解就是利用辐射、光催化剂在反应体系中产生的活性极强的自由基,再通过自由基与有机污染物之间的加合、取代、电子转移等过程将污染物全部降解为无机物的过程。Photocatalytic degradation is the use of highly active free radicals generated by radiation and photocatalysts in the reaction system, and then through the addition, substitution, and electron transfer between free radicals and organic pollutants. All pollutants are degraded into inorganic substances. the process of.
光催化剂氧化还原机理主要是催化剂受光照射,吸收光能,发生电子跃迁,生成电子-空穴对,对吸附于表面的污染物直接进行氧化还原,或氧化表面吸附的氢氧根(OH-),生成强氧化性的氢氧自由基(·OH),将污染物氧化。The redox mechanism of photocatalysts is mainly that the catalyst is irradiated by light, absorbs light energy, undergoes electron transition, generates electron-hole pairs, directly redoxes the pollutants adsorbed on the surface, or oxidizes the hydroxide (OH-) adsorbed on the surface. , generating strong oxidizing hydroxyl radicals ( OH), oxidizing pollutants.
光催化降解卤代有机污染物(HOPs)的机理总体表现为电子转移特征,即光激发催化剂产生的活性物种如eaq、eCB或·OH、hVB等分别将HOPs还原成阴离子自由基或氧化成阳离子自由基,并通过C—X键断裂实现降解。The mechanism of photocatalytic degradation of halogenated organic pollutants (HOPs) is generally characterized by electron transfer, that is, the active species generated by photo-excited catalysts, such as eaq, eCB or OH, hVB, etc., reduce HOPs to anionic radicals or oxidize them to cations, respectively. free radicals, and degradation is achieved through C-X bond cleavage.
2009年,新型的具有石墨相的无金属氮化碳光催化剂被开发出来,该催化剂的氧化效率较低。在此基础上国内外做了大量的相关研究,其中,中国发明专利CN105536846A公开了一种二氧化钛/氮化碳复合光催化剂,有效提高了光生电子与正电荷分离能力,光催化氧化效率显著提升。本发明为了进一步提升催化剂的光催化氧化效率,提供了一种有机污水高效光降解催化剂的制备方法。In 2009, a new metal-free carbon nitride photocatalyst with a graphitic phase was developed, which exhibits low oxidation efficiency. On this basis, a lot of related research has been done at home and abroad. Among them, Chinese invention patent CN105536846A discloses a titanium dioxide/carbon nitride composite photocatalyst, which effectively improves the separation ability of photogenerated electrons and positive charges, and the photocatalytic oxidation efficiency is significantly improved. In order to further improve the photocatalytic oxidation efficiency of the catalyst, the present invention provides a preparation method of a high-efficiency photodegradation catalyst for organic sewage.
发明内容SUMMARY OF THE INVENTION
基于背景技术存在的技术问题,本发明提出了一种有机污水高效光降解催化剂的制备方法。Based on the technical problems existing in the background art, the present invention proposes a preparation method of a high-efficiency photodegradation catalyst for organic sewage.
本发明的技术方案如下:The technical scheme of the present invention is as follows:
一种有机污水高效光降解催化剂的制备方法,包括以下步骤:A preparation method of an organic sewage high-efficiency photodegradation catalyst, comprising the following steps:
A、将纤维状的轻质碳酸钙加入乙醇中;A, adding fibrous light calcium carbonate to ethanol;
B、向乙醇中加入助磨剂,分散均匀后得到浆料;B, add grinding aid to ethanol, and obtain slurry after dispersing uniformly;
C、对浆料进行反复研磨,过800目筛,取浆液;C. Grind the slurry repeatedly, pass through an 800-mesh sieve, and get the slurry;
D、在浆液中加入将硫酸锌、氮化碳和催化剂,混合均匀后置于聚四氟乙烯内衬的水热反应器中,在220-250℃条件下,水热反应18-24h,将溶液蒸发、干燥,研磨后得到前驱体粉末;D. Add zinc sulfate, carbon nitride and catalyst to the slurry, mix them evenly, and place them in a polytetrafluoroethylene-lined hydrothermal reactor. The solution is evaporated, dried, and ground to obtain precursor powder;
E、经过高温煅烧和自然冷却后即可得到有机污水高效光降解催化剂。E. High-efficiency photodegradation catalyst for organic sewage can be obtained after high temperature calcination and natural cooling.
优选的,所述的步骤A中,所述的纤维状的轻质碳酸钙,长径比为(60-120):1。Preferably, in the step A, the fibrous light calcium carbonate has an aspect ratio of (60-120):1.
优选的,所述的步骤B中,所述的助磨剂为甘油。Preferably, in the step B, the grinding aid is glycerol.
优选的,所述的步骤C中,所述的浆液中,轻质碳酸钙的质量浓度为1-3%。Preferably, in the step C, in the slurry, the mass concentration of light calcium carbonate is 1-3%.
优选的,所述的步骤D中,所述的催化剂为氟化氢。Preferably, in the step D, the catalyst is hydrogen fluoride.
优选的,所述的步骤D中,催化剂的加入量为硫酸锌加入量的10-20%。Preferably, in the step D, the added amount of the catalyst is 10-20% of the added amount of zinc sulfate.
优选的,所述的步骤D中,硫酸锌和氮化碳的加入量与浆液中轻质碳酸钙的质量比分别为(8-15):100和(1-2.5):100。Preferably, in the step D, the added amount of zinc sulfate and carbon nitride and the mass ratio of light calcium carbonate in the slurry are (8-15):100 and (1-2.5):100, respectively.
优选的,所述的步骤E中,所述的高温煅烧的温度为500-550℃,时间为1.5-2h。Preferably, in the step E, the temperature of the high-temperature calcination is 500-550° C., and the time is 1.5-2 h.
本发明的有益之处在于:本发明的有机污水高效光降解催化剂的制备方法,将纤维状的轻质碳酸钙研磨后得到微米级碳酸钙片状模板,然后加入硫酸锌、氮化碳和催化剂,进行水热反应,干燥、研磨后得到前驱体粉末,再经过高温煅烧和自然冷却即可得到有机污水高效光降解催化剂。该催化剂是由纳米级氧化锌和氮化碳混合负载在碳酸钙上,形成氧化锌/氮化碳/碳酸钙复合光降解催化剂,该催化剂具有高效、快速的特点,在使用浓度为0.05-0.2mg/L的条件下,30min对2mg/L硝基苯的去除率即可达到98%以上。The advantages of the present invention are: in the preparation method of the organic sewage efficient photodegradation catalyst of the present invention, the fibrous light calcium carbonate is ground to obtain a micron-scale calcium carbonate sheet template, and then zinc sulfate, carbon nitride and a catalyst are added. , hydrothermal reaction, drying and grinding to obtain precursor powder, and then high-temperature calcination and natural cooling to obtain a high-efficiency photodegradation catalyst for organic sewage. The catalyst is a composite photodegradation catalyst composed of nano-scale zinc oxide and carbon nitride mixed on calcium carbonate to form a zinc oxide/carbon nitride/calcium carbonate composite photodegradation catalyst. The catalyst has the characteristics of high efficiency and rapidity. Under the condition of mg/L, the removal rate of 2mg/L nitrobenzene can reach more than 98% in 30min.
具体实施方式Detailed ways
实施例1Example 1
一种有机污水高效光降解催化剂的制备方法,包括以下步骤:A preparation method of an organic sewage high-efficiency photodegradation catalyst, comprising the following steps:
A、将纤维状的轻质碳酸钙加入乙醇中;A, adding fibrous light calcium carbonate to ethanol;
B、向乙醇中加入体积比为1.5%的甘油,分散均匀后得到浆料;B. Add 1.5% glycerol by volume to ethanol, and disperse uniformly to obtain slurry;
C、对浆料进行反复研磨,过800目筛,取浆液;C. Grind the slurry repeatedly, pass through an 800-mesh sieve, and get the slurry;
D、在浆液中加入将硫酸锌、氮化碳和催化剂,混合均匀后置于聚四氟乙烯内衬的水热反应器中,在230-240℃条件下,水热反应22h,将溶液蒸发、干燥,研磨后得到前驱体粉末;D. Add zinc sulfate, carbon nitride and catalyst to the slurry, mix them evenly, and place them in a polytetrafluoroethylene lined hydrothermal reactor. , dried, and ground to obtain precursor powder;
E、经过高温煅烧和自然冷却后即可得到有机污水高效光降解催化剂。E. High-efficiency photodegradation catalyst for organic sewage can be obtained after high temperature calcination and natural cooling.
所述的步骤A中,所述的纤维状的轻质碳酸钙,长径比为(60-120):1。In the step A, the fibrous light calcium carbonate has an aspect ratio of (60-120):1.
所述的步骤C中,所述的浆液中,轻质碳酸钙的质量浓度为1.8%。In the step C, in the slurry, the mass concentration of light calcium carbonate is 1.8%.
所述的步骤D中,所述的催化剂为氟化氢,加入量为硫酸锌加入量的15%。In the step D, the catalyst is hydrogen fluoride, and the added amount is 15% of the added amount of zinc sulfate.
硫酸锌和氮化碳的加入量与浆液中轻质碳酸钙的质量比分别为12:100和1.8:100。The mass ratios of zinc sulfate and carbon nitride to light calcium carbonate in the slurry were 12:100 and 1.8:100, respectively.
所述的步骤E中,所述的高温煅烧的温度为530℃,时间为1.8h。In the step E, the temperature of the high-temperature calcination is 530°C, and the time is 1.8h.
实施例2Example 2
一种有机污水高效光降解催化剂的制备方法,包括以下步骤:A preparation method of an organic sewage high-efficiency photodegradation catalyst, comprising the following steps:
A、将纤维状的轻质碳酸钙加入乙醇中;A, adding fibrous light calcium carbonate to ethanol;
B、向乙醇中加入体积比为3.2%的甘油,分散均匀后得到浆料;B. Add 3.2% glycerin by volume to ethanol, and disperse uniformly to obtain slurry;
C、对浆料进行反复研磨,过800目筛,取浆液;C. Grind the slurry repeatedly, pass through an 800-mesh sieve, and get the slurry;
D、在浆液中加入将硫酸锌、氮化碳和催化剂,混合均匀后置于聚四氟乙烯内衬的水热反应器中,在240-250℃条件下,水热反应18h,将溶液蒸发、干燥,研磨后得到前驱体粉末;D. Add zinc sulfate, carbon nitride and catalyst to the slurry, mix them evenly, and place them in a polytetrafluoroethylene-lined hydrothermal reactor. Under the condition of 240-250 °C, the hydrothermal reaction is carried out for 18 hours, and the solution is evaporated. , dried, and ground to obtain precursor powder;
E、经过高温煅烧和自然冷却后即可得到有机污水高效光降解催化剂。E. High-efficiency photodegradation catalyst for organic sewage can be obtained after high temperature calcination and natural cooling.
所述的步骤A中,所述的纤维状的轻质碳酸钙,长径比为(60-120):1。In the step A, the fibrous light calcium carbonate has an aspect ratio of (60-120):1.
所述的步骤C中,所述的浆液中,轻质碳酸钙的质量浓度为3%。In the step C, in the slurry, the mass concentration of light calcium carbonate is 3%.
所述的步骤D中,所述的催化剂为氟化氢,加入量为硫酸锌加入量的10%。In the step D, the catalyst is hydrogen fluoride, and the added amount is 10% of the added amount of zinc sulfate.
硫酸锌和氮化碳的加入量与浆液中轻质碳酸钙的质量比分别为15:100和1:100。The mass ratios of zinc sulfate and carbon nitride to light calcium carbonate in the slurry were 15:100 and 1:100, respectively.
所述的步骤E中,所述的高温煅烧的温度为550℃,时间为1.5h。In the step E, the temperature of the high-temperature calcination is 550°C, and the time is 1.5h.
实施例3Example 3
一种有机污水高效光降解催化剂的制备方法,包括以下步骤:A preparation method of an organic sewage high-efficiency photodegradation catalyst, comprising the following steps:
A、将纤维状的轻质碳酸钙加入乙醇中;A, adding fibrous light calcium carbonate to ethanol;
B、向乙醇中加入体积比为1.1%的甘油,分散均匀后得到浆料;B. Add 1.1% glycerol by volume to ethanol, and disperse uniformly to obtain slurry;
C、对浆料进行反复研磨,过800目筛,取浆液;C. Grind the slurry repeatedly, pass through an 800-mesh sieve, and get the slurry;
D、在浆液中加入将硫酸锌、氮化碳和催化剂,混合均匀后置于聚四氟乙烯内衬的水热反应器中,在220-225℃条件下,水热反应24h,将溶液蒸发、干燥,研磨后得到前驱体粉末;D. Add zinc sulfate, carbon nitride and catalyst to the slurry, mix them evenly, and place them in a polytetrafluoroethylene-lined hydrothermal reactor. Under the condition of 220-225 °C, hydrothermally react for 24 hours, and evaporate the solution , dried, and ground to obtain precursor powder;
E、经过高温煅烧和自然冷却后即可得到有机污水高效光降解催化剂。E. High-efficiency photodegradation catalyst for organic sewage can be obtained after high temperature calcination and natural cooling.
所述的步骤A中,所述的纤维状的轻质碳酸钙,长径比为(60-120):1。In the step A, the fibrous light calcium carbonate has an aspect ratio of (60-120):1.
所述的步骤C中,所述的浆液中,轻质碳酸钙的质量浓度为1%。In the step C, in the slurry, the mass concentration of light calcium carbonate is 1%.
所述的步骤D中,所述的催化剂为氟化氢,加入量为硫酸锌加入量的20%。In the step D, the catalyst is hydrogen fluoride, and the added amount is 20% of the added amount of zinc sulfate.
硫酸锌和氮化碳的加入量与浆液中轻质碳酸钙的质量比分别为8:100和2.5:100。The mass ratios of zinc sulfate and carbon nitride to light calcium carbonate in the slurry were 8:100 and 2.5:100, respectively.
所述的步骤E中,所述的高温煅烧的温度为500℃,时间为2h。In the step E, the temperature of the high-temperature calcination is 500°C, and the time is 2h.
将以上实施例1-3的0.5g催化剂粉末球磨分散在10L的水中制备成分散液,将该分散液加入1L污染物为硝基苯的有机污水中。此时,水体中催化剂的浓度为0.1mg/L,硝基苯浓度为2mg/mL,将污水置于光照强度为0.51W/m2@340nm的Q-SUN老化箱体中分别进行30min、60min、120min测试,测试硝基苯的残留量,并与对比例(中国发明专利CN105536846A实施例1制备的催化剂)进行对比测试,得到如下测试数据:0.5 g of the catalyst powder of the above Examples 1-3 was ball-milled and dispersed in 10 L of water to prepare a dispersion liquid, and the dispersion liquid was added to 1 L of organic sewage whose pollutant was nitrobenzene. At this time, the concentration of catalyst in the water body was 0.1mg/L, and the concentration of nitrobenzene was 2mg/mL. The sewage was placed in a Q-SUN aging box with a light intensity of 0.51W/m 2 @340nm for 30min and 60min respectively. , 120min test, test the residual amount of nitrobenzene, and carry out comparative test with comparative example (the catalyzer of Chinese invention patent CN105536846A embodiment 1 preparation), obtain following test data:
由以上测试数据可以知道,本发明的有机污水高效光降解催化剂对硝基苯有非常好的光降解效果,且降解速度非常快。It can be known from the above test data that the high-efficiency photodegradation catalyst for organic sewage of the present invention has a very good photodegradation effect on nitrobenzene, and the degradation speed is very fast.
以上所述,仅为本发明较佳的具体实施方式,但本发明的保护范围并不局限于此,任何熟悉本技术领域的技术人员在本发明揭露的技术范围内,根据本发明的技术方案及其发明构思加以等同替换或改变,都应涵盖在本发明的保护范围之内。The above description is only a preferred embodiment of the present invention, but the protection scope of the present invention is not limited to this. The equivalent replacement or change of the inventive concept thereof shall be included within the protection scope of the present invention.
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