CN116920830B - Ozonolysis photocatalyst coating and preparation method and application thereof - Google Patents
Ozonolysis photocatalyst coating and preparation method and application thereof Download PDFInfo
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- CN116920830B CN116920830B CN202311129749.1A CN202311129749A CN116920830B CN 116920830 B CN116920830 B CN 116920830B CN 202311129749 A CN202311129749 A CN 202311129749A CN 116920830 B CN116920830 B CN 116920830B
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- 239000011941 photocatalyst Substances 0.000 title claims abstract description 94
- 238000000576 coating method Methods 0.000 title claims abstract description 71
- 239000011248 coating agent Substances 0.000 title claims abstract description 66
- 238000002360 preparation method Methods 0.000 title abstract description 20
- 238000005949 ozonolysis reaction Methods 0.000 title description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 86
- 238000000354 decomposition reaction Methods 0.000 claims abstract description 52
- 239000000463 material Substances 0.000 claims abstract description 48
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical group [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 claims abstract description 26
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- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 claims abstract description 16
- CTENFNNZBMHDDG-UHFFFAOYSA-N Dopamine hydrochloride Chemical compound Cl.NCCC1=CC=C(O)C(O)=C1 CTENFNNZBMHDDG-UHFFFAOYSA-N 0.000 claims abstract description 9
- 229960001149 dopamine hydrochloride Drugs 0.000 claims abstract description 9
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- 238000001179 sorption measurement Methods 0.000 description 4
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- VCJMYUPGQJHHFU-UHFFFAOYSA-N iron(3+);trinitrate Chemical compound [Fe+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O VCJMYUPGQJHHFU-UHFFFAOYSA-N 0.000 description 2
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/48—Silver or gold
- B01J23/50—Silver
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/007—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by irradiation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/8671—Removing components of defined structure not provided for in B01D53/8603 - B01D53/8668
- B01D53/8675—Ozone
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/26—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/80—Employing electric, magnetic, electromagnetic or wave energy, or particle radiation
- B01D2259/804—UV light
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
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- Chemical Kinetics & Catalysis (AREA)
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- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Environmental & Geological Engineering (AREA)
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Abstract
本发明涉及臭氧分解控制领域和催化化学领域,具体涉及一种臭氧分解光催化剂涂层,负载材料、粘接层和光催化剂;负载材料表面包裹粘接层;光催化剂通过粘接层附着在负载材料表面;粘接层包括硅溶胶与多糖混合物、盐酸多巴胺或单宁酸中的一种;光催化剂为纳米银;本发明还提供一种臭氧分解光催化剂涂层的制备方法以及臭氧分解光催化剂涂层在臭氧处理中的应用;本发明可提高臭氧降解速率,制备过程简易且制备过程中无污染物产生,形成稳定的超疏水表面,具有高抗冲击性能且不影响催化活性,具有较好的稳定性能。
The invention relates to the field of ozone decomposition control and the field of catalytic chemistry, specifically to an ozone decomposition photocatalyst coating, a load material, an adhesive layer and a photocatalyst; the surface of the load material is wrapped with an adhesive layer; the photocatalyst is attached to the load material through the adhesive layer surface; the adhesive layer includes one of a mixture of silica sol and polysaccharide, dopamine hydrochloride or tannic acid; the photocatalyst is nanosilver; the invention also provides a preparation method of an ozone decomposition photocatalyst coating and an ozone decomposition photocatalyst coating. The application of the layer in ozone treatment; the present invention can increase the ozone degradation rate, has a simple preparation process and no pollutants are generated during the preparation process, forms a stable superhydrophobic surface, has high impact resistance and does not affect the catalytic activity, and has good Stable performance.
Description
技术领域Technical field
本发明涉及臭氧分解控制领域和催化化学领域,具体涉及一种臭氧分解光催化剂涂层及其制备方法和应用。The invention relates to the field of ozone decomposition control and catalytic chemistry, and specifically to an ozone decomposition photocatalyst coating and its preparation method and application.
背景技术Background technique
臭氧作为光化学反应后的产物,是常见的室内空气污染物之一,具有强氧化性,高浓度的臭氧能强烈刺激机体黏膜组织,引起心血管和呼吸系统疾病,对人体健康构成巨大威胁。臭氧对生态系统有着强烈的破坏,不仅会减弱植物光合作用效率,甚至杀死细胞,使植物叶片坏死、过早脱落,造成农作物减产以及潜在的粮食供应问题等。因此,研究臭氧的消除对于保护人体健康和维护生态环境具有重要的意义。Ozone, as a product of photochemical reactions, is one of the common indoor air pollutants. It has strong oxidizing properties. High concentrations of ozone can strongly stimulate the body's mucosal tissues, cause cardiovascular and respiratory diseases, and pose a huge threat to human health. Ozone has strong damage to the ecosystem. It will not only weaken the photosynthesis efficiency of plants, but even kill cells, causing plant leaves to become necrotic and fall off prematurely, causing crop yield reduction and potential food supply problems. Therefore, studying the elimination of ozone is of great significance for protecting human health and maintaining the ecological environment.
目前,国内外的臭氧去除技术主要包括热分解、活性炭吸附、溶剂吸收、辐射分解法和催化分解法。光催化臭氧分解技术通过光催化剂上的活性位点加速臭氧分解为氧气,具有分解效率高和生态友好性的优势而成为极具应用前景的方法。其中,负载型光催化剂可以将光催化剂负载在载体上,以增加光催化剂的稳定性和活性,从而提高臭氧氧化反应的效率。耐臭氧污染物的反应速率限制了臭氧化,光催化臭氧化能很好地克服这些缺点。At present, ozone removal technologies at home and abroad mainly include thermal decomposition, activated carbon adsorption, solvent absorption, radiation decomposition and catalytic decomposition. Photocatalytic ozone decomposition technology accelerates the decomposition of ozone into oxygen through active sites on the photocatalyst. It has the advantages of high decomposition efficiency and eco-friendliness, making it a promising method. Among them, the supported photocatalyst can support the photocatalyst on the carrier to increase the stability and activity of the photocatalyst, thereby improving the efficiency of the ozone oxidation reaction. The reaction rate of ozone-resistant pollutants limits ozonation, and photocatalytic ozonation can well overcome these shortcomings.
开发高效光催化剂对于光催化臭氧化处理有机废水具有重要意义。Yang等合成了具有不同优先暴露晶面(ZnO-棒和ZnO-盘)的ZnO纳米复合材料,暴露的{0001}面和氧空位促进了光生电荷的分离和转移,并改善了臭氧分子在光催化剂表面的吸附和活化。Gmurek等通过单金属和双金属(Cu/Pd)负载TiO2纳米粒子增强基于光催化的过程,在可见光下可以获得优异的光催化臭氧化效率,用于抗生素抗性基因和兼性病原菌去除。Wang等采用一步氧化还原法在泡沫镍表面原位生长NiFeOOH纳米片,在波长为365nm的UV LED灯激发下将臭氧高效地转化为羟基自由基,在超短保留时间内表现出显着的光催化灭活效率。The development of efficient photocatalysts is of great significance for the photocatalytic ozonation treatment of organic wastewater. Yang et al. synthesized ZnO nanocomposites with different preferentially exposed crystal faces (ZnO-rods and ZnO-disks). The exposed {0001} faces and oxygen vacancies promoted the separation and transfer of photogenerated charges and improved the performance of ozone molecules in light. Adsorption and activation of catalyst surfaces. Gmurek et al. enhanced the photocatalysis-based process by monometallic and bimetallic (Cu/Pd)-loaded TiO2 nanoparticles, and could obtain excellent photocatalytic ozonation efficiency under visible light for the removal of antibiotic resistance genes and facultative pathogens. Wang et al. used a one-step redox method to grow NiFeOOH nanosheets in situ on the surface of nickel foam, and efficiently converted ozone into hydroxyl radicals under the excitation of a UV LED lamp with a wavelength of 365 nm, showing significant light emission in an ultra-short retention time. Catalytic inactivation efficiency.
然而,光催化剂的暴露面和表面缺陷对光催化臭氧化性能的影响却很少被提及,尤其是光催化剂对高湿环境尤为敏感,在高湿环境下水分子与臭氧竞争吸附会阻隔光催化剂表面催化氧化臭氧的活性位点,导致臭氧降解效率降低,并且水汽侵蚀导致光催化剂不稳定很容易失活,涂层容易脱落,严重影响了光催化剂的使用寿命。However, the impact of the exposed surface and surface defects of the photocatalyst on the photocatalytic ozonation performance has rarely been mentioned. In particular, the photocatalyst is particularly sensitive to high-humidity environments. In high-humidity environments, the competitive adsorption of water molecules and ozone will block the photocatalyst. The surface catalytically oxidizes the active sites of ozone, resulting in a reduction in ozone degradation efficiency, and water vapor erosion causes the photocatalyst to be unstable and easily deactivated, and the coating is easy to fall off, seriously affecting the service life of the photocatalyst.
现有技术中有方法选取硫酸锰、硝酸铁、硝酸铜以及硝酸银的不同配比溶液与分子筛粉末混合得到负载型分子筛粉末,通过将负载分子筛的粉末和在凝胶的表面使用三甲基氯硅烷进行处理,进一步提高了气凝胶的疏水性。另有一种疏水性常温分解臭氧光催化剂的制备方法,该方法将高温活化后的臭氧分解光催化剂与硅烷偶联剂水解溶液混合,使得硅烷偶联剂上硅烷氧基基团接枝到光催化剂表面,经过高温处理,得到疏水性常温分解臭氧光催化剂。还有关于纳米三氧化二铝杂化改性苯乙烯-二乙烯基苯共聚物疏水光催化剂载体的制备方法,该制备方法中通过引入经由十七氟癸基三甲氧基硅烷改性的纳米三氧化二铝,通过无机纳米粒子自身优良的力学性能,大幅提高SDB疏水光催化剂载体的抗压强度及疏水性。In the prior art, there are methods to select solutions of different proportions of manganese sulfate, ferric nitrate, copper nitrate and silver nitrate and mix them with molecular sieve powder to obtain loaded molecular sieve powder. By combining the loaded molecular sieve powder and using trimethyl chloride on the surface of the gel, Silane treatment further improves the hydrophobicity of the aerogel. There is another method for preparing a hydrophobic room-temperature ozone decomposition photocatalyst. This method mixes the high-temperature activated ozone decomposition photocatalyst with the silane coupling agent hydrolysis solution, so that the silane oxygen group on the silane coupling agent is grafted to the photocatalyst. The surface is treated at high temperature to obtain a hydrophobic photocatalyst for decomposing ozone at room temperature. There is also a method for preparing a nano-alumina hybrid modified styrene-divinylbenzene copolymer hydrophobic photocatalyst carrier. In this preparation method, nano-alumina modified by heptadecafluorodecyltrimethoxysilane is introduced. Aluminum oxide, through the excellent mechanical properties of inorganic nanoparticles, greatly improves the compressive strength and hydrophobicity of SDB hydrophobic photocatalyst carrier.
在光催化剂或载体表面修饰超疏水涂层能够有效改善稳定性问题,抑制涂层吸水脱落,但是操作过程复杂,成本增加,易阻塞活性位点导致降解效率变低,甚至一些含氟疏水改性剂会导致二次污染。由于载体深层孔隙的光穿透力较低,涂覆在多孔基材上的光光催化剂无法产生足够的ROS来催化臭氧分解。这种情况下,不仅会造成光催化剂的浪费,细菌也会侵入深层孔隙中存活,并在适宜的培养条件下繁殖,造成二次污染。Modifying a superhydrophobic coating on the surface of a photocatalyst or carrier can effectively improve stability problems and prevent the coating from absorbing water and falling off. However, the operation process is complicated, the cost increases, and the active sites are easily blocked, resulting in lower degradation efficiency. Even some fluorine-containing hydrophobic modifications Agents can cause secondary pollution. Due to the low light penetration of the deep pores of the carrier, the photocatalyst coated on the porous substrate cannot generate enough ROS to catalyze ozone decomposition. In this case, not only will the photocatalyst be wasted, but bacteria will also invade deep pores to survive and reproduce under suitable culture conditions, causing secondary pollution.
发明内容Contents of the invention
针对现有技术的不足,本发明的目的之一在于提供一种适应高湿度环境的疏水型臭氧分解光催化剂涂层。合成的催化材料可在短时间内实现对臭氧的高效分解,且制备方法简单、稳定性好、使用寿命长。In view of the shortcomings of the existing technology, one of the purposes of the present invention is to provide a hydrophobic ozone decomposition photocatalyst coating suitable for high humidity environments. The synthesized catalytic material can achieve efficient decomposition of ozone in a short time, and has a simple preparation method, good stability and long service life.
本发明的目的之二在于提供一种臭氧分解光催化剂涂层的制备方法,该涂层的制备方法可在纳米银光催化剂表面原位形成疏水性,无需额外使用疏水改性剂,对环境友好,解决了现有负载型臭氧分解光催化剂在高湿环境下光催化剂的催化活性大幅降低,额外疏水改性操作过程复杂,带来环境污染,易阻塞活性位点导致臭氧降解效率变低的问题。The second object of the present invention is to provide a preparation method for an ozone decomposition photocatalyst coating. The preparation method of the coating can form hydrophobicity in situ on the surface of the nanosilver photocatalyst without the need for additional hydrophobic modifiers, and is environmentally friendly. , which solves the problems of existing supported ozone decomposition photocatalysts, such as the catalytic activity of the photocatalyst being greatly reduced in a high-humidity environment, the additional hydrophobic modification process being complicated, causing environmental pollution, and the active sites being easily blocked, resulting in low ozone degradation efficiency. .
本发明的目的之三在于提供臭氧分解光催化剂涂层在臭氧处理中的应用。The third object of the present invention is to provide the application of ozone decomposition photocatalyst coating in ozone treatment.
本发明的目的之一,采用以下方案实现:One of the purposes of the present invention is achieved by adopting the following solutions:
一种臭氧分解光催化剂涂层,包括:负载材料、粘接层和光催化剂;An ozone decomposition photocatalyst coating, including: a load material, an adhesive layer and a photocatalyst;
所述负载材料表面包裹粘接层;所述光催化剂通过所述粘接层附着在所述负载材料表面;The surface of the load material is wrapped with an adhesive layer; the photocatalyst is attached to the surface of the load material through the adhesive layer;
所述粘接层包括硅溶胶与多糖混合物、盐酸多巴胺或单宁酸中的一种;The adhesive layer includes one of a mixture of silica sol and polysaccharide, dopamine hydrochloride or tannic acid;
所述光催化剂为纳米银。The photocatalyst is nanosilver.
可选的,负载材料为泡沫金属网、棉织物、蜂窝活性炭或海绵中的一种,具有高比表面积的优点。Optionally, the load material is one of foam metal mesh, cotton fabric, honeycomb activated carbon or sponge, which has the advantage of high specific surface area.
可选的,泡沫金属网的孔径≤400μm。泡沫金属网的孔径≤400μm,可提高纳米银在泡沫金属网的负载量,进而提高臭氧的光催化性能。同时避免孔径过高导致表面粗糙度降低影响涂层超疏水效果。Optional, the pore size of the foam metal mesh is ≤400μm. The pore size of the foam metal mesh is ≤400 μm, which can increase the loading capacity of nanosilver on the foam metal mesh, thereby improving the photocatalytic performance of ozone. At the same time, it is avoided that the surface roughness is reduced due to excessive pore diameter and affects the superhydrophobic effect of the coating.
可选的,硅溶胶与多糖混合物中硅溶胶与多糖的摩尔比为1:7-9。选用硅溶胶与多糖的摩尔比为1:7-9,形成的共混溶液稳定性和粘附性最优,比例过低会导致溶液粘附性差,比例过高会导致溶液硬化影响使用。Optionally, the molar ratio of silica sol to polysaccharide in the mixture of silica sol and polysaccharide is 1:7-9. The molar ratio of silica sol to polysaccharide is selected to be 1:7-9 to form a blended solution with optimal stability and adhesion. If the ratio is too low, the solution will have poor adhesion, and if the ratio is too high, the solution will harden and affect its use.
本发明的目的之二,采用以下方案实现:The second object of the present invention is achieved by adopting the following solutions:
一种臭氧分解光催化剂涂层的制备方法,包括以下步骤:A preparation method for an ozone decomposition photocatalyst coating, including the following steps:
(1)将负载材料浸泡在粘接剂中,并调节粘接剂pH,然后取出负载材料进行紫外光照射使负载材料表面包裹一层粘接层;所述粘接剂为硅溶胶与多糖混合液、盐酸多巴胺或单宁酸中的一种;(1) Soak the load material in the adhesive and adjust the pH of the adhesive, then take out the load material and irradiate it with ultraviolet light to coat the surface of the load material with an adhesive layer; the adhesive is a mixture of silica sol and polysaccharide One of liquid, dopamine hydrochloride or tannic acid;
(2)将AgNO3加入乙醇水溶液中,拌匀,得混合溶液A;(2) Add AgNO 3 to the ethanol aqueous solution and mix well to obtain mixed solution A;
(3)向步骤(2)的混合溶液A中滴加氨溶液,直至混合溶液A底部沉淀完全消失,得混合溶液B;(3) Add ammonia solution dropwise to mixed solution A in step (2) until the precipitate at the bottom of mixed solution A completely disappears to obtain mixed solution B;
(4)向步骤(3)的混合溶液B中加入葡萄糖溶液得到混合溶液C;向混合溶液C中浸入步骤(1)处理后的负载材料,超声处理,然后取出负载材料,冲洗;重复浸入、超声处理、取出负载材料、冲洗的操作,最后将负载材料烘干;(4) Add glucose solution to mixed solution B in step (3) to obtain mixed solution C; immerse the load material treated in step (1) into mixed solution C, perform ultrasonic treatment, then take out the load material, rinse; repeat immersion, Ultrasonic treatment, removal of the load material, rinsing operations, and finally drying of the load material;
(5)将步骤(4)中干燥的负载材料进行紫外光照射,制得。(5) The loaded material dried in step (4) is irradiated with ultraviolet light to obtain.
使用葡萄糖作为试剂,该技术中葡萄糖具备双功能特性,不仅可以作为纳米银的还原剂,将银离子还原为纳米银;同时葡萄糖吸附在涂层表面可作为超疏水前体,进行UV照射时能够发生化学脱氧和交联,使得涂层表面形成超疏水表面。避免了现有技术涂层表面超疏水需额外添加疏水改性剂,操作复杂,涂层不均匀的缺点。Glucose is used as a reagent. In this technology, glucose has dual-functional properties. It can not only be used as a reducing agent for nano-silver, reducing silver ions to nano-silver; at the same time, glucose adsorbed on the surface of the coating can be used as a superhydrophobic precursor, which can be used during UV irradiation. Chemical deoxidation and cross-linking occur, resulting in a superhydrophobic surface on the coating surface. It avoids the shortcomings of the prior art that the super-hydrophobic coating surface requires additional hydrophobic modifiers, complicated operations, and uneven coating.
进一步地,步骤(1)中粘接剂浓度为2-5mg/mL。选用粘接剂溶液浓度为2-5mg/mL,可在负载材料表面形成足够厚的粘附膜,可提高纳米银在负载材料上负载的稳定性,浓度太高,粘附膜层过厚会包裹纳米银,影响臭氧降解效果;浓度太低,粘附膜层过薄容易脱落,材料稳定性差。Further, the concentration of the adhesive in step (1) is 2-5 mg/mL. The concentration of the adhesive solution selected is 2-5 mg/mL, which can form a thick enough adhesive film on the surface of the load material and improve the stability of the nano-silver loading on the load material. If the concentration is too high, the adhesive film layer will be too thick. Wrapping nano-silver affects the ozone degradation effect; the concentration is too low, the adhesive film layer is too thin and easy to fall off, and the material stability is poor.
进一步地,步骤(1)中粘接剂pH为7.5-10.0。选用pH范围为7.5-10.0,是因为制备的粘附膜粘附性能和稳定性最优。Further, the pH of the adhesive in step (1) is 7.5-10.0. The pH range of 7.5-10.0 was chosen because the prepared adhesive film has the best adhesion performance and stability.
进一步地,步骤(1)中紫外光照射强度为500-1000W,照射时间为15-35min。选用紫外光照射强度范围为500-1000W,可加快粘接剂在负载材料表面的聚合,并形成稳定的粘附膜层,缩短聚合时间。照射强度过低,会影响粘接剂的聚合效果,粘附膜层过薄稳定性差。照射强度过高,会破坏内部分子结构,无法形成粘附膜层。Further, in step (1), the ultraviolet light irradiation intensity is 500-1000W, and the irradiation time is 15-35 minutes. The ultraviolet light irradiation intensity range is selected to be 500-1000W, which can accelerate the polymerization of the adhesive on the surface of the load material, form a stable adhesive film layer, and shorten the polymerization time. If the irradiation intensity is too low, it will affect the polymerization effect of the adhesive, and the adhesive film layer will be too thin and have poor stability. Excessive irradiation intensity will destroy the internal molecular structure and prevent the formation of an adhesive film.
进一步地,步骤(1)中粘接层厚度为5-60nm。粘接层厚度为5-60nm,是因为该区间厚度的粘附膜不仅能够粘附足量的纳米银,还能够稳定地固定在负载材料上防止脱落。粘附膜层过厚会包裹纳米银,影响臭氧降解效果;浓度太低,粘附膜层过薄容易脱落,材料稳定性差。Further, the thickness of the adhesive layer in step (1) is 5-60 nm. The thickness of the adhesive layer is 5-60nm because the adhesive film with a thickness in this range can not only adhere to a sufficient amount of nanosilver, but can also be stably fixed on the load material to prevent it from falling off. If the adhesive film layer is too thick, it will wrap the nano-silver, which will affect the ozone degradation effect; if the concentration is too low, the adhesive film layer will fall off if it is too thin, and the material stability will be poor.
进一步地,步骤(2)中乙醇水溶液中乙醇的体积浓度百分比为9-13%。乙醇水溶液中乙醇的体积浓度百分比选用为9-13%,能够控制pH值微碱性,纳米银还原效果最优,还可缩短反应时间。乙醇体积浓度过低,会使反应时间过长且纳米银还原量较少。乙醇体积浓度过高,pH过高,反应过快,产生大量黑色的银粒沉淀,不易得到优质纳米银。Further, the volume concentration percentage of ethanol in the ethanol aqueous solution in step (2) is 9-13%. The volume concentration percentage of ethanol in the ethanol aqueous solution is selected to be 9-13%, which can control the slightly alkaline pH value, optimize the reduction effect of nanosilver, and shorten the reaction time. If the ethanol volume concentration is too low, the reaction time will be too long and the amount of nanosilver reduced will be small. The ethanol volume concentration is too high, the pH is too high, the reaction is too fast, and a large amount of black silver particles are precipitated, making it difficult to obtain high-quality nanosilver.
进一步地,步骤(2)中AgNO3在乙醇水溶液中的质量浓度百分比为2-3.5%。将一定量的AgNO3加入上述体积浓度的乙醇水溶液以后,形成混合溶液,AgNO3的质量浓度过高,造成剩余浪费,浓度过低,使得纳米银的浓度降低,造成负载材料上纳米银负载量少,影响臭氧降解效果。Further, the mass concentration percentage of AgNO 3 in the aqueous ethanol solution in step (2) is 2-3.5%. After a certain amount of AgNO 3 is added to the ethanol aqueous solution with the above volume concentration, a mixed solution is formed. The mass concentration of AgNO 3 is too high, resulting in residual waste, and the concentration is too low, resulting in a reduction in the concentration of nanosilver, resulting in a large loading of nanosilver on the load material. Less, affecting the ozone degradation effect.
进一步地,步骤(4)的混合溶液C中银离子与葡萄糖的摩尔比为0.15-0.25:1。将银离子与葡萄糖按照摩尔比为0.15-0.25:1比例混合,葡萄糖可充分将银离子还原成纳米银,同时,减少葡萄糖的剩余,避免造成浪费。比例过高会导致银离子还原不完全。Further, the molar ratio of silver ions to glucose in the mixed solution C of step (4) is 0.15-0.25:1. Mix silver ions and glucose at a molar ratio of 0.15-0.25:1. Glucose can fully reduce silver ions into nanosilver, while reducing the remaining glucose to avoid waste. Too high a ratio will lead to incomplete reduction of silver ions.
进一步地,步骤(4)中于75-90℃条件下进行超声处理6-12min/次。在上述温度条件范围内,纳米银颗粒形貌和尺寸均匀,可提高纳米银在负载材料上负载的稳定性和负载速度,进而提高材料的臭氧降解性能。Further, in step (4), ultrasonic treatment is performed at 75-90°C for 6-12 min/time. Within the above temperature range, the morphology and size of nanosilver particles are uniform, which can improve the stability and loading speed of nanosilver loading on the load material, thereby improving the ozone degradation performance of the material.
进一步地,步骤(5)中紫外光波长为365nm,照射强度为500-1500W,照射时间为10-30min。紫外光波长选用为365nm,是因为该波段的紫外光能够最高效激发纳米银的LSPR效应,照射强度选用500-1000W是因为可使涂层表面亲水吸附物葡萄糖在纳米银的LSPR作用下被充分脱氧和交联,将涂层由超亲水性转变为超疏水性。照射强度过低葡萄糖反应不完全会导致涂层表面超疏水性下降。照射强度过高会造成纳米银颗粒的形变,影响臭氧降解效果。Further, in step (5), the wavelength of ultraviolet light is 365nm, the irradiation intensity is 500-1500W, and the irradiation time is 10-30 minutes. The wavelength of ultraviolet light is selected as 365nm because the ultraviolet light in this band can most efficiently stimulate the LSPR effect of nanosilver. The irradiation intensity is selected as 500-1000W because it can make the hydrophilic adsorbent glucose on the surface of the coating be absorbed by the LSPR of nanosilver. Fully deoxidized and cross-linked to transform the coating from super hydrophilic to super hydrophobic. If the irradiation intensity is too low and the glucose reaction is incomplete, the superhydrophobicity of the coating surface will decrease. Excessive irradiation intensity will cause the deformation of silver nanoparticles and affect the ozone degradation effect.
本发明的目的之三,采用以下方案实现:The third object of the present invention is achieved by adopting the following solutions:
臭氧分解光催化剂涂层在臭氧处理中的应用,光催化剂结合紫外光用于常温高湿环境下空气中臭氧的协同催化分解,具体来说,光催化剂涂层用于高湿环境下的臭氧分解反应过程中,反应温度为25℃,相对湿度不低于80%,臭氧浓度不低于40ppm。Application of ozone decomposition photocatalyst coating in ozone treatment. Photocatalyst combined with ultraviolet light is used for synergistic catalytic decomposition of ozone in the air under normal temperature and high humidity environment. Specifically, photocatalyst coating is used for ozone decomposition under high humidity environment. During the reaction process, the reaction temperature is 25°C, the relative humidity is not less than 80%, and the ozone concentration is not less than 40ppm.
本发明的有益效果为:The beneficial effects of the present invention are:
1.本发明臭氧分解光催化剂涂层在表面形成疏水层,水基溶液制备,绿色环保,无需要使用有毒的疏水改性剂;1. The ozone decomposition photocatalyst coating of the present invention forms a hydrophobic layer on the surface, and the water-based solution is prepared, which is green and environmentally friendly, and does not require the use of toxic hydrophobic modifiers;
2.本发明臭氧分解光催化剂涂层中具有特定波长响应的纳米银颗粒,产生强烈的等离子体激元效应,可以还原臭氧,达到快速分解,同时本征疏水性使其适应高湿度环境,保持臭氧分解活性;2. The nano-silver particles with specific wavelength response in the ozone decomposition photocatalyst coating of the present invention produce a strong plasmon effect, which can reduce ozone and achieve rapid decomposition. At the same time, its intrinsic hydrophobicity makes it adaptable to high humidity environments and maintain Ozonolysis activity;
3.本发明臭氧分解光催化剂涂层通过对环境友好的粘接剂粘合负载材料和纳米银光催化剂,提高了材料的高抗冲击性能且不影响催化活性,能够成功克服疏水涂层容易脱落的问题,从而延长光催化剂的使用寿命。负载材料和纳米银均具有高比表面积,为臭氧分解提供了更多的活性位点,提高分解效率。3. The ozone decomposition photocatalyst coating of the present invention binds the load material and the nano-silver photocatalyst with an environmentally friendly adhesive, which improves the high impact resistance of the material without affecting the catalytic activity, and can successfully overcome the easy falling off of the hydrophobic coating. problem, thereby extending the service life of the photocatalyst. Both the loading material and nanosilver have high specific surface areas, which provide more active sites for ozone decomposition and improve the decomposition efficiency.
附图说明Description of drawings
图1-2分别为实施例1光催化剂涂层紫外照射前、后的SEM图。Figures 1-2 are respectively SEM images of the photocatalyst coating before and after ultraviolet irradiation in Example 1.
图3-4分别为实施例1光催化剂涂层紫外照射前、后的静态接触角检测结果图。Figures 3-4 are respectively the static contact angle detection results of the photocatalyst coating before and after ultraviolet irradiation in Example 1.
图5为实施例1光催化剂涂层的XRD谱图;Figure 5 is the XRD spectrum of the photocatalyst coating in Example 1;
图6为实施例1光催化剂涂层的漫反射紫外可见光吸收光谱图。Figure 6 is a diffuse reflection ultraviolet-visible light absorption spectrum chart of the photocatalyst coating in Example 1.
图7-8分别为实施例1光催化剂涂层紫外照射前、后的XPS分峰图。Figures 7-8 are respectively XPS peak diagrams before and after ultraviolet irradiation of the photocatalyst coating in Example 1.
图9为实施例1不同再生次数光催化剂的臭氧去除效果图。Figure 9 is a diagram showing the ozone removal effect of the photocatalyst with different regeneration times in Example 1.
具体实施方式Detailed ways
下面结合具体实施方式对本发明作进一步的详细描述。但不应将此理解为本发明上述主题的范围仅限于以下的实施例,凡基于本发明内容所实现的技术均属于本发明的范围。The present invention will be described in further detail below in conjunction with specific embodiments. However, this should not be understood to mean that the scope of the above-mentioned subject matter of the present invention is limited to the following embodiments. All technologies implemented based on the contents of the present invention belong to the scope of the present invention.
实施例1Example 1
一种臭氧分解光催化剂涂层,其制备方法包括以下步骤:An ozone decomposition photocatalyst coating, its preparation method includes the following steps:
(1)将清洁的泡沫金属网浸泡在pH=8.5的4mg/mL硅溶胶与多糖的混合溶液中,硅溶胶与多糖的摩尔比为1:8;然后取出泡沫金属网进行紫外光照射30min,照射强度990W,使泡沫金属网表面包裹厚度为50nm的粘接层;泡沫金属网的孔径300μm;(1) Soak the clean metal foam mesh in a mixed solution of 4 mg/mL silica sol and polysaccharide with pH = 8.5. The molar ratio of silica sol to polysaccharide is 1:8; then take out the metal foam mesh and irradiate it with UV light for 30 minutes. The irradiation intensity is 990W, so that the surface of the foam metal mesh is wrapped with an adhesive layer with a thickness of 50 nm; the pore size of the foam metal mesh is 300 μm;
(2)将AgNO3加入体积浓度为12%的乙醇水溶液中,AgNO3在乙醇水溶液中的质量浓度为3%,拌匀,得混合溶液A;(2) Add AgNO 3 to an ethanol aqueous solution with a volume concentration of 12%. The mass concentration of AgNO 3 in the ethanol aqueous solution is 3%. Mix well to obtain mixed solution A;
(3)向步骤(2)的混合溶液A中滴加质量浓度为2%的氨溶液,直至混合溶液A底部沉淀完全消失,得混合溶液B;(3) Add an ammonia solution with a mass concentration of 2% to the mixed solution A in step (2) dropwise until the precipitate at the bottom of the mixed solution A completely disappears to obtain the mixed solution B;
(4)向步骤(3)的混合溶液B中加入葡萄糖溶液得到混合溶液C,混合溶液C中银离子与葡萄糖的摩尔比为0.22:1;向混合溶液C中浸入步骤(1)处理后的泡沫金属网,并于80℃条件下进行超声处理7min,超声功率100W,频率45kHz,然后取出泡沫金属网,用水冲洗;重复浸入、超声处理、取出泡沫金属网、用水冲洗操作4遍,最后将泡沫金属网于室温条件下真空干燥烘干;(4) Add glucose solution to mixed solution B in step (3) to obtain mixed solution C. The molar ratio of silver ions to glucose in mixed solution C is 0.22:1; immerse the foam treated in step (1) into mixed solution C. metal mesh, and perform ultrasonic treatment at 80°C for 7 minutes, ultrasonic power 100W, frequency 45kHz, then take out the foam metal mesh and rinse with water; repeat the immersion, ultrasonic treatment, take out the foam metal mesh, rinse with water 4 times, and finally remove the foam The metal mesh is vacuum dried at room temperature;
(5)将步骤(4)中干燥泡沫金属网采用365nm紫外LED灯进行紫外照射20min,照射强度1000W,制得。(5) Use a 365nm UV LED lamp to irradiate the dry foam metal mesh in step (4) for 20 minutes with an irradiation intensity of 1000W to prepare it.
实施例1光催化剂涂层紫外照射前后扫描电镜对比见图1-2。实施例1光催化剂涂层紫外照射前后的静态接触角检测结果见图3-4。实施例1光催化剂涂层的XRD谱见图5。实施例1光催化剂涂层的漫反射紫外可见光吸收光谱见图6。实施例1光催化剂涂层紫外照射前后的XPS分峰图见图7-8。实施例1不同再生次数光催化剂的臭氧去除效果见图9。The comparison of scanning electron microscopy before and after UV irradiation of the photocatalyst coating in Example 1 is shown in Figure 1-2. The static contact angle detection results of the photocatalyst coating in Example 1 before and after UV irradiation are shown in Figure 3-4. The XRD spectrum of the photocatalyst coating in Example 1 is shown in Figure 5. The diffuse reflection UV-visible light absorption spectrum of the photocatalyst coating in Example 1 is shown in Figure 6. The XPS peak diagrams of the photocatalyst coating before and after UV irradiation in Example 1 are shown in Figures 7-8. The ozone removal effect of the photocatalyst with different regeneration times in Example 1 is shown in Figure 9.
实施例2Example 2
一种臭氧分解光催化剂涂层,其制备方法包括以下步骤:An ozone decomposition photocatalyst coating, its preparation method includes the following steps:
(1)将清洁的棉织物浸泡在pH=8.0的2.5mg/mL碱性盐酸多巴胺溶液中,然后取出棉织物进行紫外照射20min,照射强度800W,使棉织物表面包裹厚度为30nm的粘接层;(1) Soak the clean cotton fabric in 2.5mg/mL alkaline dopamine hydrochloride solution with pH=8.0, then take out the cotton fabric and irradiate it with UV for 20 minutes at an intensity of 800W to wrap the surface of the cotton fabric with an adhesive layer with a thickness of 30nm. ;
(2)将AgNO3加入体积浓度为10%的乙醇水溶液中,AgNO3在乙醇水溶液中的质量浓度为2.5%,拌匀,得混合溶液A;(2) Add AgNO 3 to an ethanol aqueous solution with a volume concentration of 10%. The mass concentration of AgNO 3 in the ethanol aqueous solution is 2.5%. Mix well to obtain mixed solution A;
(3)向步骤(2)的混合溶液A中滴加质量浓度为2%的氨溶液,直至混合溶液A底部沉淀完全消失,得混合溶液B;(3) Add an ammonia solution with a mass concentration of 2% to the mixed solution A in step (2) dropwise until the precipitate at the bottom of the mixed solution A completely disappears to obtain the mixed solution B;
(4)向步骤(3)的混合溶液B中加入葡萄糖溶液得到混合溶液C,混合溶液C中银离子与葡萄糖的摩尔比为0.20:1;向混合溶液C中浸入步骤(1)处理后的棉织物,并于80℃条件下进行超声处理7min,超声功率100W,频率45kHz,然后取出棉织物,用水冲洗;重复浸入、超声处理、取出棉织物、用水冲洗操作4遍,最后将棉织物于室温条件下真空干燥烘干;(4) Add glucose solution to mixed solution B in step (3) to obtain mixed solution C. The molar ratio of silver ions to glucose in mixed solution C is 0.20:1; immerse the cotton treated in step (1) into mixed solution C. fabric, and perform ultrasonic treatment at 80°C for 7 minutes, ultrasonic power 100W, frequency 45kHz, then take out the cotton fabric and rinse with water; repeat the immersion, ultrasonic treatment, take out the cotton fabric, rinse with water 4 times, and finally put the cotton fabric at room temperature Vacuum drying under certain conditions;
(5)将步骤(4)中干燥棉织物采用365nm高压汞灯进行紫外照射15min,照射强度1490W,制得。(5) The dried cotton fabric in step (4) is irradiated with ultraviolet rays using a 365nm high-pressure mercury lamp for 15 minutes at an irradiation intensity of 1490W to obtain the product.
实施例3Example 3
一种臭氧分解光催化剂涂层,其制备方法包括以下步骤:An ozone decomposition photocatalyst coating, its preparation method includes the following steps:
(1)将清洁的泡沫金属网浸泡在pH=9.0的4mg/mL硅溶胶与多糖的混合溶液中,硅溶胶与多糖的摩尔比为1:8;然后取出泡沫金属网进行紫外照射16min,照射强度990W,使泡沫金属网表面包裹厚度为40nm的粘接层;泡沫金属网的孔径300μm;(1) Soak the clean metal foam mesh in a mixed solution of 4 mg/mL silica sol and polysaccharide with pH = 9.0. The molar ratio of silica sol to polysaccharide is 1:8; then take out the metal foam mesh and perform UV irradiation for 16 minutes. The strength is 990W, and the surface of the foam metal mesh is wrapped with an adhesive layer with a thickness of 40nm; the pore size of the foam metal mesh is 300 μm;
(2)将AgNO3加入体积浓度为10%的乙醇水溶液中,AgNO3在乙醇水溶液中的质量浓度为2.5%,拌匀,得混合溶液A;(2) Add AgNO 3 to an ethanol aqueous solution with a volume concentration of 10%. The mass concentration of AgNO 3 in the ethanol aqueous solution is 2.5%. Mix well to obtain mixed solution A;
(3)向步骤(2)的混合溶液A中滴加质量浓度为2%的氨溶液,直至混合溶液A底部沉淀完全消失,得混合溶液B;(3) Add an ammonia solution with a mass concentration of 2% to the mixed solution A in step (2) dropwise until the precipitate at the bottom of the mixed solution A completely disappears to obtain the mixed solution B;
(4)向步骤(3)的混合溶液B中加入葡萄糖溶液得到混合溶液C,混合溶液C中银离子与葡萄糖的摩尔比为0.18:1;向混合溶液C中浸入步骤(1)处理后的泡沫金属网,并于89℃条件下进行超声处理7min,超声功率100W,频率45kHz,然后取出泡沫金属网,用水冲洗;重复浸入、超声处理、取出泡沫金属网、用水冲洗操作4遍,最后将泡沫金属网于室温条件下真空干燥烘干;(4) Add glucose solution to mixed solution B in step (3) to obtain mixed solution C. The molar ratio of silver ions to glucose in mixed solution C is 0.18:1; immerse the foam treated in step (1) into mixed solution C. metal mesh, and perform ultrasonic treatment at 89°C for 7 minutes, ultrasonic power 100W, frequency 45kHz, then take out the foam metal mesh and rinse with water; repeat the immersion, ultrasonic treatment, take out the foam metal mesh, rinse with water 4 times, and finally remove the foam The metal mesh is vacuum dried at room temperature;
(5)将步骤(4)中干燥泡沫金属网采用365nm紫外LED灯进行紫外照射15min,照射强度1490W,制得。(5) The dry foam metal mesh in step (4) is irradiated with ultraviolet rays using a 365nm ultraviolet LED lamp for 15 minutes, and the irradiation intensity is 1490W.
实施例4Example 4
一种臭氧分解光催化剂涂层,其制备方法包括以下步骤:An ozone decomposition photocatalyst coating, its preparation method includes the following steps:
(1)将清洁的海绵浸泡在pH=7.6的2.1mg/mL单宁酸溶液中,然后取出海绵进行紫外照射25min,照射强度600W,使海绵表面包裹厚度为25nm的粘接层;(1) Soak the clean sponge in a 2.1mg/mL tannic acid solution with pH=7.6, then take out the sponge and irradiate it with ultraviolet light for 25 minutes at an intensity of 600W to wrap the sponge surface with an adhesive layer with a thickness of 25nm;
(2)将AgNO3加入体积浓度为12%的乙醇水溶液中,AgNO3在乙醇水溶液中的质量浓度为3.4%,拌匀,得混合溶液A;(2) Add AgNO 3 to an ethanol aqueous solution with a volume concentration of 12%. The mass concentration of AgNO 3 in the ethanol aqueous solution is 3.4%. Mix well to obtain mixed solution A;
(3)向步骤(2)的混合溶液A中滴加质量浓度为2%的氨溶液,直至混合溶液A底部沉淀完全消失,得混合溶液B;(3) Add an ammonia solution with a mass concentration of 2% to the mixed solution A in step (2) dropwise until the precipitate at the bottom of the mixed solution A completely disappears to obtain the mixed solution B;
(4)向步骤(3)的混合溶液B中加入葡萄糖溶液得到混合溶液C,混合溶液C中银离子与葡萄糖的摩尔比为0.18:1;向混合溶液C中浸入步骤(1)处理后的海绵,并于85℃条件下进行超声处理7min,超声功率100W,频率45kHz,然后取出海绵,用水冲洗;重复浸入、超声处理、取出海绵、用水冲洗操作4遍,最后将海绵于室温条件下真空干燥烘干;(4) Add glucose solution to mixed solution B in step (3) to obtain mixed solution C. The molar ratio of silver ions to glucose in mixed solution C is 0.18:1; immerse the sponge treated in step (1) into mixed solution C. , and perform ultrasonic treatment at 85°C for 7 minutes, ultrasonic power 100W, frequency 45kHz, then take out the sponge and rinse with water; repeat the immersion, ultrasonic treatment, take out the sponge, and rinse with water 4 times, and finally vacuum dry the sponge at room temperature. drying;
(5)将步骤(4)中海绵采用365nm紫外LED灯进行紫外照射15min,照射强度1490W,制得。(5) UV-irradiate the sponge in step (4) using a 365nm UV LED lamp for 15 minutes with an irradiation intensity of 1490W to prepare the sponge.
实施例5Example 5
一种臭氧分解光催化剂涂层,其制备方法包括以下步骤:An ozone decomposition photocatalyst coating, its preparation method includes the following steps:
(1)将清洁的棉织物浸泡在pH=8.5的3mg/mL碱性盐酸多巴胺溶液中,然后取出棉织物进行紫外照射30min,照射强度990W,使棉织物表面包裹厚度为30nm的粘接层;(1) Soak the clean cotton fabric in 3mg/mL alkaline dopamine hydrochloride solution with pH=8.5, then take out the cotton fabric and irradiate it with ultraviolet rays for 30 minutes at an irradiation intensity of 990W, so that the surface of the cotton fabric is wrapped with an adhesive layer with a thickness of 30nm;
(2)将AgNO3加入体积浓度为10%的乙醇水溶液中,AgNO3在乙醇水溶液中的质量浓度为2.1%,拌匀,得混合溶液A;(2) Add AgNO 3 to an ethanol aqueous solution with a volume concentration of 10%. The mass concentration of AgNO 3 in the ethanol aqueous solution is 2.1%. Mix well to obtain mixed solution A;
(3)向步骤(2)的混合溶液A中滴加质量浓度为2%的氨溶液,直至混合溶液A底部沉淀完全消失,得混合溶液B;(3) Add an ammonia solution with a mass concentration of 2% to the mixed solution A in step (2) dropwise until the precipitate at the bottom of the mixed solution A completely disappears to obtain the mixed solution B;
(4)向步骤(3)的混合溶液B中加入葡萄糖溶液得到混合溶液C,混合溶液C中银离子与葡萄糖的摩尔比为0.24:1;向混合溶液C中浸入步骤(1)处理后的棉织物,并于85℃条件下进行超声处理7min,超声功率100W,频率45kHz,然后取出棉织物,用水冲洗;重复浸入、超声处理、取出棉织物、用水冲洗操作4遍,最后将棉织物于室温条件下真空干燥烘干;(4) Add glucose solution to mixed solution B in step (3) to obtain mixed solution C. The molar ratio of silver ions to glucose in mixed solution C is 0.24:1; immerse the cotton treated in step (1) into mixed solution C. fabric, and perform ultrasonic treatment at 85°C for 7 minutes, ultrasonic power 100W, frequency 45kHz, then take out the cotton fabric and rinse with water; repeat the immersion, ultrasonic treatment, take out the cotton fabric, rinse with water 4 times, and finally put the cotton fabric at room temperature Vacuum drying under certain conditions;
(5)将步骤(4)中海绵采用365nm高压汞灯进行紫外照射15min,照射强度1490W,制得。(5) The sponge in step (4) is irradiated with ultraviolet rays using a 365nm high-pressure mercury lamp for 15 minutes at an irradiation intensity of 1490W to prepare the sponge.
实施例6Example 6
一种臭氧分解光催化剂涂层,其制备方法包括以下步骤:An ozone decomposition photocatalyst coating, its preparation method includes the following steps:
(1)将清洁的蜂窝活性炭浸泡在pH=9.5的3.5mg/mL碱性单宁酸溶液中,然后取出蜂窝活性炭进行紫外照射16min,照射强度800W,使蜂窝活性炭表面包裹厚度为20nm的粘接层;(1) Soak the clean honeycomb activated carbon in a 3.5mg/mL alkaline tannic acid solution with pH=9.5, then take out the honeycomb activated carbon and conduct UV irradiation for 16 minutes with an irradiation intensity of 800W to coat the surface of the honeycomb activated carbon with an adhesive layer with a thickness of 20nm. layer;
(2)将AgNO3加入体积浓度为11%的乙醇水溶液中,AgNO3在乙醇水溶液中的质量浓度为2.1%,拌匀,得混合溶液A;(2) Add AgNO 3 to an ethanol aqueous solution with a volume concentration of 11%. The mass concentration of AgNO 3 in the ethanol aqueous solution is 2.1%. Mix well to obtain mixed solution A;
(3)向步骤(2)的混合溶液A中滴加质量浓度为2%的氨溶液,直至混合溶液A底部沉淀完全消失,得混合溶液B;(3) Add an ammonia solution with a mass concentration of 2% to the mixed solution A in step (2) dropwise until the precipitate at the bottom of the mixed solution A completely disappears to obtain the mixed solution B;
(4)向步骤(3)的混合溶液B中加入葡萄糖溶液得到混合溶液C,混合溶液C中银离子与葡萄糖的摩尔比为0.20:1;向混合溶液C中浸入步骤(1)处理后的蜂窝活性炭,并于76℃条件下进行超声处理7min,超声功率100W,频率45kHz,然后取出蜂窝活性炭,用水冲洗;重复浸入、超声处理、取出蜂窝活性炭、用水冲洗操作4遍,最后将蜂窝活性炭于室温条件下真空干燥烘干;(4) Add glucose solution to mixed solution B in step (3) to obtain mixed solution C. The molar ratio of silver ions to glucose in mixed solution C is 0.20:1; immerse the honeycomb treated in step (1) into mixed solution C. Activated carbon, and ultrasonic treatment at 76°C for 7 minutes, ultrasonic power 100W, frequency 45kHz, then take out the honeycomb activated carbon, rinse with water; repeat the immersion, ultrasonic treatment, take out the honeycomb activated carbon, rinse with water 4 times, and finally put the honeycomb activated carbon at room temperature Vacuum drying under certain conditions;
(5)将步骤(4)中海绵采用365nm高压汞灯进行紫外照射25min,照射强度1490W,制得。(5) The sponge in step (4) is irradiated with ultraviolet rays using a 365nm high-pressure mercury lamp for 25 minutes at an irradiation intensity of 1490W to prepare the sponge.
实施例7Example 7
一种臭氧分解光催化剂涂层,其制备方法包括以下步骤:An ozone decomposition photocatalyst coating, its preparation method includes the following steps:
(1)将清洁的泡沫金属网浸泡在pH=9.5的2.5mg/mL碱性盐酸多巴胺溶液中,然后取出泡沫金属网进行紫外照射25min,照射强度800W,使蜂窝活性炭表面包裹厚度为40nm的粘接层;泡沫金属网的孔径300μm;(1) Soak the clean metal foam mesh in 2.5 mg/mL alkaline dopamine hydrochloride solution with pH = 9.5, then take out the metal foam mesh and conduct UV irradiation for 25 minutes with an irradiation intensity of 800W to coat the honeycomb activated carbon surface with adhesive with a thickness of 40 nm. Connection layer; the pore size of the foam metal mesh is 300μm;
(2)将AgNO3加入体积浓度为10%的乙醇水溶液中,AgNO3在乙醇水溶液中的质量浓度为2.5%,拌匀,得混合溶液A;(2) Add AgNO 3 to an ethanol aqueous solution with a volume concentration of 10%. The mass concentration of AgNO 3 in the ethanol aqueous solution is 2.5%. Mix well to obtain mixed solution A;
(3)向步骤(2)的混合溶液A中滴加质量浓度为2%的氨溶液,直至混合溶液A底部沉淀完全消失,得混合溶液B;(3) Add an ammonia solution with a mass concentration of 2% to the mixed solution A in step (2) dropwise until the precipitate at the bottom of the mixed solution A completely disappears to obtain the mixed solution B;
(4)向步骤(3)的混合溶液B中加入葡萄糖溶液得到混合溶液C,混合溶液C中银离子与葡萄糖的摩尔比为0.24:1;向混合溶液C中浸入步骤(1)处理后的泡沫金属网,并于76℃条件下进行超声处理7min,超声功率100W,频率45kHz,然后取出泡沫金属网,用水冲洗;重复浸入、超声处理、取出泡沫金属网、用水冲洗操作4遍,最后将泡沫金属网于室温条件下真空干燥烘干;(4) Add glucose solution to mixed solution B in step (3) to obtain mixed solution C. The molar ratio of silver ions to glucose in mixed solution C is 0.24:1; immerse the foam treated in step (1) into mixed solution C. metal mesh, and perform ultrasonic treatment at 76°C for 7 minutes, ultrasonic power 100W, frequency 45kHz, then take out the foam metal mesh and rinse with water; repeat immersion, ultrasonic treatment, take out the foam metal mesh, rinse with water 4 times, and finally remove the foam The metal mesh is vacuum dried at room temperature;
(5)将步骤(4)中海绵采用365nm高压汞灯进行紫外照射25min,照射强度1490W,制得。(5) The sponge in step (4) is irradiated with ultraviolet rays using a 365nm high-pressure mercury lamp for 25 minutes at an irradiation intensity of 1490W to prepare the sponge.
对比例1Comparative example 1
一种臭氧分解光催化剂涂层,其制备方法包括以下步骤:An ozone decomposition photocatalyst coating, its preparation method includes the following steps:
(1)将清洁的泡沫金属网浸泡在pH=8.5的4mg/mL硅溶胶与多糖的混合溶液中,然后取出泡沫金属网进行紫外光照射30min,照射强度1000W,使泡沫金属网表面包裹厚度为50nm的粘接层;(1) Soak the clean metal foam mesh in a mixed solution of 4 mg/mL silica sol and polysaccharide with pH = 8.5, then take out the metal foam mesh and irradiate it with UV light for 30 minutes at an intensity of 1000W, so that the surface coating thickness of the metal foam mesh is 50nm adhesive layer;
(2)将AgNO3加入体积浓度为8%的乙醇水溶液中,AgNO3在乙醇水溶液中的质量浓度为1.8%,拌匀,得混合溶液A;(2) Add AgNO 3 to an ethanol aqueous solution with a volume concentration of 8%. The mass concentration of AgNO 3 in the ethanol aqueous solution is 1.8%. Mix well to obtain mixed solution A;
(3)向步骤(2)的混合溶液A中滴加质量浓度为2%的氨溶液,直至混合溶液A底部沉淀完全消失,得混合溶液B;(3) Add an ammonia solution with a mass concentration of 2% to the mixed solution A in step (2) dropwise until the precipitate at the bottom of the mixed solution A completely disappears to obtain the mixed solution B;
(4)向步骤(3)的混合溶液B中加入葡萄糖溶液得到混合溶液C,混合溶液C中银离子与葡萄糖的摩尔比为0.27:1;向混合溶液C中浸入步骤(1)处理后的泡沫金属网,并于60℃条件下进行超声处理7min,超声功率100W,频率45kHz,然后取出泡沫金属网,用水冲洗;重复浸入、超声处理、取出泡沫金属网、用水冲洗操作4遍,最后将泡沫金属网于室温条件下真空干燥烘干;(4) Add glucose solution to mixed solution B in step (3) to obtain mixed solution C. The molar ratio of silver ions to glucose in mixed solution C is 0.27:1; immerse the foam treated in step (1) into mixed solution C. metal mesh, and perform ultrasonic treatment at 60°C for 7 minutes, ultrasonic power 100W, frequency 45kHz, then take out the foam metal mesh and rinse with water; repeat the immersion, ultrasonic treatment, take out the foam metal mesh, rinse with water 4 times, and finally remove the foam The metal mesh is vacuum dried at room temperature;
(5)将步骤(4)中干燥泡沫金属网采用365nm紫外LED灯进行紫外照射15min,照射强度1000W,制得。(5) Use a 365nm UV LED lamp to irradiate the dry foam metal mesh in step (4) for 15 minutes with an irradiation intensity of 1000W to prepare it.
对比例2Comparative example 2
以尾气脱除臭氧使用的锰系光催化剂作为对比例,光催化剂为Pd/Mn/分子筛,其中Pd含量为0.5wt%,MnO2含量为14.5wt%。Taking the manganese photocatalyst used to remove ozone from tail gas as a comparative example, the photocatalyst is Pd/Mn/molecular sieve, in which the Pd content is 0.5wt% and the MnO2 content is 14.5wt%.
对比例3Comparative example 3
在实施例1制备基础上,未进行步骤(5)中的紫外照射。Based on the preparation in Example 1, the ultraviolet irradiation in step (5) was not performed.
性能测试:Performance Testing:
对实施例1-7和对比例1-3光催化剂涂层进行催化分解臭氧的性能测试,测试方法和条件如下所示:The photocatalyst coatings of Examples 1-7 and Comparative Examples 1-3 were tested for their catalytic decomposition of ozone performance. The test methods and conditions are as follows:
测试方法:将臭氧气体通入一个横向设置的静态反应腔体,反应腔体的前端设置进气口,尾端出口连接臭氧检测器,反应腔体内从前到后,沿气流方向依次径向设置气体混合通道、紫外灯组,光催化剂涂层板和紫外灯组,光催化剂涂层板有3组,每个光催化剂涂层板将反应腔体隔成前后两个设有紫外灯组的小腔体,紫外灯波长为365nm。Test method: Pour ozone gas into a static reaction chamber set horizontally. An air inlet is set at the front end of the reaction chamber, and an ozone detector is connected to the tail outlet. Gases are arranged radially in the reaction chamber from front to back along the direction of air flow. Mixing channel, UV lamp group, photocatalyst coating plate and UV lamp group. There are 3 groups of photocatalyst coating plates. Each photocatalyst coating plate divides the reaction chamber into two small chambers with UV lamp groups at the front and rear. body, the wavelength of UV lamp is 365nm.
对照组:365nm紫外光分解臭氧、可见光分解臭氧、254nm紫外光分解臭氧。Control group: 365nm ultraviolet light decomposes ozone, visible light decomposes ozone, and 254nm ultraviolet light decomposes ozone.
测试条件:Test Conditions:
反应气中臭氧浓度为40ppm、温度为25℃,相对湿度为90%;记录5分钟后对应的臭氧分解率,如表1所示。The ozone concentration in the reaction gas is 40 ppm, the temperature is 25°C, and the relative humidity is 90%; the corresponding ozone decomposition rate after 5 minutes is recorded, as shown in Table 1.
表1臭氧分解率Table 1 Ozone decomposition rate
综合实施例1-5可以看出,本发明提供的臭氧分解光催化剂涂层的制备方法得到的臭氧分解光催化剂涂层具有很高的催化效果,臭氧分解率可达99%以上,较优条件下可达100%。而实施例6-7的臭氧分解效果有所降低,但分解率也可达到95%以上,表明反应温度是光催化剂合成的重要影响参数,较高的反应温度能调节光催化剂的紫外吸收范围更好地契合365nm紫外光,能够提高光催化剂在湿度环境下对臭氧的降解率。对比例2-3中普通的锰系光催化剂和表面未疏水处理的涂层在高湿环境下臭氧分解效率明显下降甚至失活,表明疏水催化剂能够抵抗水分子的竞争吸附,提高臭氧分解能力。通过对照实验可以发现,本发明所提供的方法较单独光催化能够实现在高湿度下优异的臭氧分解效率。Based on Examples 1-5, it can be seen that the ozone decomposition photocatalyst coating obtained by the preparation method of the ozone decomposition photocatalyst coating provided by the present invention has a very high catalytic effect, and the ozone decomposition rate can reach more than 99%, under better conditions. down to 100%. The ozone decomposition effect of Examples 6-7 has been reduced, but the decomposition rate can also reach more than 95%, indicating that the reaction temperature is an important influencing parameter for the synthesis of photocatalysts, and a higher reaction temperature can adjust the UV absorption range of the photocatalyst to be wider. It is well suited to 365nm ultraviolet light and can improve the ozone degradation rate of photocatalysts in humid environments. In Comparative Example 2-3, the ozone decomposition efficiency of ordinary manganese photocatalysts and coatings without hydrophobic treatment on the surface significantly decreased or even became deactivated in a high-humidity environment, indicating that the hydrophobic catalyst can resist the competitive adsorption of water molecules and improve the ozone decomposition ability. Through comparative experiments, it can be found that the method provided by the present invention can achieve excellent ozone decomposition efficiency under high humidity compared with photocatalysis alone.
上述实施例和对比例所制备的光催化涂层疏水性能对比数据如下表2。Comparative data on the hydrophobic properties of the photocatalytic coatings prepared in the above examples and comparative examples are as follows in Table 2.
表2光催化涂层疏水性能Table 2 Hydrophobic properties of photocatalytic coating
涂层结合力参照相关标准:GB/T 1720-79(89)《漆膜附着力测定法(划圈法)》、GB/T9286-1998《色漆和清漆漆膜的划格试验》。The coating adhesion refers to relevant standards: GB/T 1720-79 (89) "Determination of paint film adhesion (circle method)", GB/T9286-1998 "Cross-hatch test of paint and varnish films".
涂层吸水率参照相关标准:GB/T 1738-1979《绝缘漆漆膜吸水率测定法》。The coating water absorption rate refers to the relevant standards: GB/T 1738-1979 "Method for determination of water absorption rate of insulating paint films".
通过上表得知,实施例1-7中的光催化剂涂层在较大比表面积的情况下进行365nm紫外照射后润湿性能发生明显转变,照射后光催化剂涂层的疏水角均在150°以上,证明365nm紫外照射能够显著增强涂层的疏水性;对比例1中反应温度较低,照射后其疏水角虽然增大,但是增幅低于实施例1-7,证明反应温度会影响光催化剂的紫外吸收强度,对光催化剂涂层的疏水性能有较大影响;实施例6-7比较于对比例1表明可以通过紫外照射时间的适当延长提高疏水性。实施例1-7和对比例1具有非常低的吸水率,均在9%以内,而比例2普通的锰系光催化剂和对比例3均具有亲水性,吸水率超过50%,表明吸水率受涂层疏水性的影响。It can be seen from the above table that the wettability of the photocatalyst coatings in Examples 1-7 changed significantly after 365nm ultraviolet irradiation with a large specific surface area. After irradiation, the hydrophobic angles of the photocatalyst coatings were all at 150°. Above, it is proved that 365nm ultraviolet irradiation can significantly enhance the hydrophobicity of the coating; the reaction temperature in Comparative Example 1 is lower, and although the hydrophobic angle increases after irradiation, the increase is lower than that of Examples 1-7, proving that the reaction temperature will affect the photocatalyst The UV absorption intensity has a great influence on the hydrophobicity of the photocatalyst coating; Examples 6-7 compared with Comparative Example 1 show that the hydrophobicity can be improved by appropriately extending the UV irradiation time. Examples 1-7 and Comparative Example 1 have very low water absorption rates, both within 9%, while the ordinary manganese photocatalyst in Example 2 and Comparative Example 3 are both hydrophilic, with a water absorption rate exceeding 50%, indicating that the water absorption rate is Affected by the hydrophobicity of the coating.
对于本领域的技术人员来说,可根据以上描述的技术方案以及构思,做出其它各种相应的改变以及变形,而所有的这些改变以及变形都应该属于本发明权利要求的保护范围之内。For those skilled in the art, various other corresponding changes and modifications can be made based on the technical solutions and concepts described above, and all of these changes and modifications should fall within the protection scope of the claims of the present invention.
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Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2005288429A (en) * | 2004-03-11 | 2005-10-20 | Japan Vilene Co Ltd | Ozone decomposition material, method for producing ozone decomposition material, method for decomposing ozone, and method for regenerating ozone decomposition material |
CN1785507A (en) * | 2005-11-22 | 2006-06-14 | 天津化工研究设计院 | Ozone decomposition catalyst and its preparation method |
CN102513106A (en) * | 2011-11-23 | 2012-06-27 | 苏州工业园区安泽汶环保技术有限公司 | Room-temperature efficient ozone decomposition catalyst and preparation method thereof |
CN112012009A (en) * | 2020-08-27 | 2020-12-01 | 中物院成都科学技术发展中心 | Super-hydrophobic sterilization material and preparation method thereof |
CN113145110A (en) * | 2021-05-08 | 2021-07-23 | 贵州省材料产业技术研究院 | Silica sol modified ozone catalytic oxidation material and preparation method thereof |
CN114210341A (en) * | 2021-12-29 | 2022-03-22 | 南京工大环境科技有限公司 | Preparation method of high-hydrophobicity ozonolysis catalyst |
CN114308123A (en) * | 2021-12-29 | 2022-04-12 | 中欧电子材料国际创新中心(合肥)有限公司 | Photocatalytic coating material and preparation method thereof |
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Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2005288429A (en) * | 2004-03-11 | 2005-10-20 | Japan Vilene Co Ltd | Ozone decomposition material, method for producing ozone decomposition material, method for decomposing ozone, and method for regenerating ozone decomposition material |
CN1785507A (en) * | 2005-11-22 | 2006-06-14 | 天津化工研究设计院 | Ozone decomposition catalyst and its preparation method |
CN102513106A (en) * | 2011-11-23 | 2012-06-27 | 苏州工业园区安泽汶环保技术有限公司 | Room-temperature efficient ozone decomposition catalyst and preparation method thereof |
CN112012009A (en) * | 2020-08-27 | 2020-12-01 | 中物院成都科学技术发展中心 | Super-hydrophobic sterilization material and preparation method thereof |
CN113145110A (en) * | 2021-05-08 | 2021-07-23 | 贵州省材料产业技术研究院 | Silica sol modified ozone catalytic oxidation material and preparation method thereof |
CN114210341A (en) * | 2021-12-29 | 2022-03-22 | 南京工大环境科技有限公司 | Preparation method of high-hydrophobicity ozonolysis catalyst |
CN114308123A (en) * | 2021-12-29 | 2022-04-12 | 中欧电子材料国际创新中心(合肥)有限公司 | Photocatalytic coating material and preparation method thereof |
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