CN106807451B - A kind of flexible platinum-formaldehyde room temperature oxidation catalyst and preparation method thereof - Google Patents
A kind of flexible platinum-formaldehyde room temperature oxidation catalyst and preparation method thereof Download PDFInfo
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- CN106807451B CN106807451B CN201710036633.1A CN201710036633A CN106807451B CN 106807451 B CN106807451 B CN 106807451B CN 201710036633 A CN201710036633 A CN 201710036633A CN 106807451 B CN106807451 B CN 106807451B
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- 239000003054 catalyst Substances 0.000 title claims abstract description 64
- 230000003647 oxidation Effects 0.000 title claims abstract description 39
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 39
- 238000002360 preparation method Methods 0.000 title claims abstract description 18
- ZFBYFCMUNLWXTK-UHFFFAOYSA-N formaldehyde;platinum Chemical compound [Pt].O=C ZFBYFCMUNLWXTK-UHFFFAOYSA-N 0.000 title claims 4
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 claims abstract description 112
- 229920000742 Cotton Polymers 0.000 claims abstract description 88
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Substances [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims abstract description 82
- 229910010413 TiO 2 Inorganic materials 0.000 claims abstract description 63
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N titanium dioxide Inorganic materials O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims abstract description 60
- 239000002131 composite material Substances 0.000 claims abstract description 45
- 238000000576 coating method Methods 0.000 claims abstract description 21
- 239000011248 coating agent Substances 0.000 claims abstract description 18
- 239000002245 particle Substances 0.000 claims abstract description 10
- 238000011068 loading method Methods 0.000 claims abstract description 9
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 39
- 239000002253 acid Substances 0.000 claims description 37
- YRKCREAYFQTBPV-UHFFFAOYSA-N acetylacetone Chemical compound CC(=O)CC(C)=O YRKCREAYFQTBPV-UHFFFAOYSA-N 0.000 claims description 36
- 238000003756 stirring Methods 0.000 claims description 35
- 239000000243 solution Substances 0.000 claims description 30
- 239000000463 material Substances 0.000 claims description 27
- 239000002585 base Substances 0.000 claims description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 23
- 239000003638 chemical reducing agent Substances 0.000 claims description 22
- 239000008139 complexing agent Substances 0.000 claims description 21
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 18
- VXUYXOFXAQZZMF-UHFFFAOYSA-N titanium(IV) isopropoxide Chemical compound CC(C)O[Ti](OC(C)C)(OC(C)C)OC(C)C VXUYXOFXAQZZMF-UHFFFAOYSA-N 0.000 claims description 16
- 230000002378 acidificating effect Effects 0.000 claims description 15
- 239000007864 aqueous solution Substances 0.000 claims description 14
- 239000011259 mixed solution Substances 0.000 claims description 11
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 10
- 238000001035 drying Methods 0.000 claims description 10
- 239000012670 alkaline solution Substances 0.000 claims description 9
- 238000005406 washing Methods 0.000 claims description 9
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 7
- 239000012279 sodium borohydride Substances 0.000 claims description 7
- 229910000033 sodium borohydride Inorganic materials 0.000 claims description 7
- 239000001509 sodium citrate Substances 0.000 claims description 7
- 239000010936 titanium Substances 0.000 claims description 7
- 229910052719 titanium Inorganic materials 0.000 claims description 7
- -1 titanium alkoxide Chemical class 0.000 claims description 7
- HRXKRNGNAMMEHJ-UHFFFAOYSA-K trisodium citrate Chemical compound [Na+].[Na+].[Na+].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O HRXKRNGNAMMEHJ-UHFFFAOYSA-K 0.000 claims description 7
- 229940038773 trisodium citrate Drugs 0.000 claims description 7
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 6
- 239000003513 alkali Substances 0.000 claims description 6
- 239000000835 fiber Substances 0.000 claims description 6
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims description 5
- 229910052700 potassium Inorganic materials 0.000 claims description 5
- 239000011591 potassium Substances 0.000 claims description 5
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 4
- 229910021529 ammonia Inorganic materials 0.000 claims description 3
- 239000002082 metal nanoparticle Substances 0.000 claims description 3
- 238000002791 soaking Methods 0.000 claims description 3
- 239000000126 substance Substances 0.000 claims description 3
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 2
- YHWCPXVTRSHPNY-UHFFFAOYSA-N butan-1-olate;titanium(4+) Chemical compound [Ti+4].CCCC[O-].CCCC[O-].CCCC[O-].CCCC[O-] YHWCPXVTRSHPNY-UHFFFAOYSA-N 0.000 claims description 2
- 229910017604 nitric acid Inorganic materials 0.000 claims description 2
- SOQBVABWOPYFQZ-UHFFFAOYSA-N oxygen(2-);titanium(4+) Chemical compound [O-2].[O-2].[Ti+4] SOQBVABWOPYFQZ-UHFFFAOYSA-N 0.000 claims description 2
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 claims 2
- ZGTMUACCHSMWAC-UHFFFAOYSA-L EDTA disodium salt (anhydrous) Chemical compound [Na+].[Na+].OC(=O)CN(CC([O-])=O)CCN(CC(O)=O)CC([O-])=O ZGTMUACCHSMWAC-UHFFFAOYSA-L 0.000 claims 1
- 239000006185 dispersion Substances 0.000 abstract description 4
- 239000010970 precious metal Substances 0.000 abstract description 4
- 238000000034 method Methods 0.000 description 26
- 229910052697 platinum Inorganic materials 0.000 description 15
- 230000003197 catalytic effect Effects 0.000 description 10
- CLSUSRZJUQMOHH-UHFFFAOYSA-L platinum dichloride Chemical compound Cl[Pt]Cl CLSUSRZJUQMOHH-UHFFFAOYSA-L 0.000 description 9
- FPCJKVGGYOAWIZ-UHFFFAOYSA-N butan-1-ol;titanium Chemical compound [Ti].CCCCO.CCCCO.CCCCO.CCCCO FPCJKVGGYOAWIZ-UHFFFAOYSA-N 0.000 description 8
- 239000002105 nanoparticle Substances 0.000 description 8
- 239000008367 deionised water Substances 0.000 description 6
- 229910021641 deionized water Inorganic materials 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 229910000510 noble metal Inorganic materials 0.000 description 6
- 238000000151 deposition Methods 0.000 description 5
- 239000011521 glass Substances 0.000 description 5
- 238000000746 purification Methods 0.000 description 5
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 4
- 239000000969 carrier Substances 0.000 description 4
- KCXVZYZYPLLWCC-UHFFFAOYSA-N EDTA Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O KCXVZYZYPLLWCC-UHFFFAOYSA-N 0.000 description 3
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- 238000007598 dipping method Methods 0.000 description 2
- 238000001523 electrospinning Methods 0.000 description 2
- 238000000445 field-emission scanning electron microscopy Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- BDOYKFSQFYNPKF-UHFFFAOYSA-N 2-[2-[bis(carboxymethyl)amino]ethyl-(carboxymethyl)amino]acetic acid;sodium Chemical compound [Na].[Na].OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O BDOYKFSQFYNPKF-UHFFFAOYSA-N 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- 241001391944 Commicarpus scandens Species 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- LLQPHQFNMLZJMP-UHFFFAOYSA-N Fentrazamide Chemical compound N1=NN(C=2C(=CC=CC=2)Cl)C(=O)N1C(=O)N(CC)C1CCCCC1 LLQPHQFNMLZJMP-UHFFFAOYSA-N 0.000 description 1
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 229920005372 Plexiglas® Polymers 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 229910000420 cerium oxide Inorganic materials 0.000 description 1
- 238000006298 dechlorination reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000008098 formaldehyde solution Substances 0.000 description 1
- 238000002173 high-resolution transmission electron microscopy Methods 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 229910052809 inorganic oxide Inorganic materials 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910000000 metal hydroxide Inorganic materials 0.000 description 1
- 150000004692 metal hydroxides Chemical class 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- BMMGVYCKOGBVEV-UHFFFAOYSA-N oxo(oxoceriooxy)cerium Chemical compound [Ce]=O.O=[Ce]=O BMMGVYCKOGBVEV-UHFFFAOYSA-N 0.000 description 1
- 230000001699 photocatalysis Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000012694 precious metal precursor Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000011946 reduction process Methods 0.000 description 1
- 229910052814 silicon oxide Inorganic materials 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 239000004408 titanium dioxide Substances 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
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- 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
- B01J31/38—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24 of titanium, zirconium or hafnium
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- 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
- B01D53/8668—Removing organic compounds not provided for in B01D53/8603 - B01D53/8665
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- B01J35/00—Catalysts, in general, characterised by their form or physical properties
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- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/64—Pore diameter
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/45—Gas separation or purification devices adapted for specific applications
- B01D2259/4508—Gas separation or purification devices adapted for specific applications for cleaning air in buildings
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Abstract
本发明涉及一种柔性Pt甲醛室温氧化催化剂及其制备方法,具体涉及一种Pt/TiO2/棉花纤维的柔性复合甲醛室温氧化催化剂及其制备方法。该催化剂包括脱脂棉花纤维载体、纳米TiO2表面涂层和分散在TiO2涂层表面的Pt活性组分,其中Pt活性组分以零价形式存在,粒径范围1‑10 nm,负载量为0.05‑2 wt%。本发明提供的Pt/TiO2/棉花纤维复合甲醛室温氧化催化剂具有分等级中孔‑大孔结构、轻质和柔性等特点,Pt与TiO2涂层及载体棉花纤维间结合牢固,活性组分单质Pt在TiO2涂层表面分散性好、粒径小,室温即可高效催化分解甲醛,贵金属Pt用量小、气阻小,适合于各类空气净化器中使用。The invention relates to a flexible Pt formaldehyde room temperature oxidation catalyst and a preparation method thereof, in particular to a Pt/TiO 2 /cotton fiber flexible composite formaldehyde room temperature oxidation catalyst and a preparation method thereof. The catalyst includes degreased cotton fiber carrier, nano- TiO2 surface coating and Pt active component dispersed on the surface of TiO2 coating, wherein the Pt active component exists in the form of zero valence, the particle size range is 1‑10 nm, and the loading capacity is 0.05‑2 wt%. The Pt/ TiO2 /cotton fiber composite formaldehyde oxidation catalyst at room temperature provided by the invention has the characteristics of hierarchical mesopore-macropore structure, light weight and flexibility, and the combination between Pt and TiO2 coating and carrier cotton fiber is firm, and the active component Elemental Pt has good dispersion and small particle size on the surface of TiO 2 coating. It can efficiently catalyze and decompose formaldehyde at room temperature. The amount of precious metal Pt is small and the gas resistance is small, which is suitable for use in various air purifiers.
Description
技术领域technical field
本发明涉及一种Pt/TiO2/棉花纤维复合甲醛室温氧化催化剂,属于室内空气净化领域。The invention relates to a Pt/TiO 2 /cotton fiber composite formaldehyde oxidation catalyst at room temperature, which belongs to the field of indoor air purification.
背景技术Background technique
甲醛是室内空气中最主要的污染物之一,具有较大的毒性。目前,消除室内甲醛污染已成为环境治理领域的热点研究课题。在已有的甲醛脱除方法中,室温催化氧化法相对于其它方式(吸附法、吸收法、负离子氧化法、臭氧催化氧化法、生物过滤/植物净化法、低温等离子体法和光催化氧化法等)具有独特的优势,它能在常温常压下进行,甲醛脱除效率高,设备简单,寿命长等优点,是最具应用潜力的甲醛脱除技术。近年来,该技术在室内空气净化应用研究不断取得进展和突破,如中国发明专利CN200410047973.7、CN200410102837.3、CN200910215887.5、CN200910098634.4、CN200910047376.7、CN200610011663.9,CN200710121423.9、CN201210389227.0和CN201410015867.4,在专利CN200410047973.7中先制备金属氧化物载体,然后浸泡在贵金属组分的溶液后蒸发制得,但该催化剂有效成分贵金属的状态未标明,活性也较低。众所周知,要获得高且稳定的甲醛催化氧化活性,催化剂必须要有良好的分散性,较小的粒径和适当的价态。而大部分专利如CN200410102837.3、CN200910215887.5、CN200910098634.4、CN200910047376.7、CN200610011663.9和CN200710121423.9中所描述的催化剂制备方法所制备的样品中金属可能以氧化物的形式存在,且分散性差,这将会影响到活性的提高;而如果要得到0价的贵金属,还需要高温的H2还原过程,使工艺复杂化,成本也相应提高。专利CN201210389227.0报道了一种甲醛室温氧化催化剂的制备方法,该方法以多孔性无机氧化物为载体,以硼氢化纳为还原剂,可溶性金属氢氧化物为添加剂,通过浸渍-室温还原-沉积法与贵金属前驱体反应制得。该方法实现了催化剂的室温催化氧化,也表现出较高的催化活性。但以上公开专利中制备的催化剂从实用的角度考虑,大都是以普通多孔性无机物纳米颗粒(如二氧化钛、氧化铝、分子筛、氧化铈和氧化硅等)为载体制得,这些催化剂如应用到填充型净化设备中需要压片或进一步将其负载在其它大块型载体上才能使用,这会使工艺复杂化,且存在催化活性下降、气阻大和催化剂易脱落的问题。为克服上述缺陷,专利CN201410015867.4以静电纺丝法制备的TiO2为载体,以浸渍~室温还原~沉积法制备了负载型贵金属/TiO2复合催化剂,新制备的催化剂无需重新负载,且具有较高的催化活性和较小的空气阻力,但该催化剂由于是以无机TiO2纳米纤维基底,因此具有易脆性,且易脆性随纤维直径的减小而增大,这样会造成在使用过程中不断会被折断,原有的纤维结构逐步被破坏,使得气阻也逐渐增大。且贵金属负载时的后续工序中为除去残留氯离子(来自贵金属前驱体)而需要一个加热蒸发的过程,因此工艺仍较复杂。同时,静电纺丝制备TiO2纤维仍存在成本偏高、设备要求高、大规模化生产还存在一定困难等问题。Formaldehyde is one of the most important pollutants in indoor air and has great toxicity. At present, eliminating indoor formaldehyde pollution has become a hot research topic in the field of environmental governance. Among the existing formaldehyde removal methods, the room temperature catalytic oxidation method is better than other methods (adsorption method, absorption method, anion oxidation method, ozone catalytic oxidation method, biological filtration/plant purification method, low temperature plasma method and photocatalytic oxidation method, etc.) It has unique advantages, it can be carried out under normal temperature and pressure, high formaldehyde removal efficiency, simple equipment, long life and other advantages, it is the most potential formaldehyde removal technology. In recent years, this technology has made continuous progress and breakthroughs in the application research of indoor air purification, such as Chinese invention patents CN200410047973.7, CN200410102837.3, CN200910215887.5, CN200910098634.4, CN200910047376.7, CN200610011663.9, CN200710192, CN2007101927 .0 and CN201410015867.4. In the patent CN200410047973.7, the metal oxide carrier is prepared first, then soaked in the solution of the noble metal component and then evaporated. However, the state of the active component of the catalyst is not indicated, and the activity is also low. As we all know, in order to obtain high and stable formaldehyde catalytic oxidation activity, the catalyst must have good dispersion, small particle size and appropriate valence state. And most patents such as CN200410102837.3, CN200910215887.5, CN200910098634.4, CN200910047376.7, CN200610011663.9 and CN200710121423.9 in the catalyst preparation method described in the sample metal may exist in the form of oxides, and Poor dispersion will affect the improvement of activity; and if you want to obtain 0-valent noble metals, you need a high-temperature H2 reduction process, which complicates the process and increases the cost accordingly. Patent CN201210389227.0 reports a preparation method of formaldehyde room temperature oxidation catalyst, which uses porous inorganic oxide as carrier, sodium borohydride as reducing agent, soluble metal hydroxide as additive, through impregnation-room temperature reduction-deposition It is prepared by reacting with precious metal precursors. This method realizes the catalytic oxidation of the catalyst at room temperature and also exhibits high catalytic activity. However, from a practical point of view, the catalysts prepared in the above published patents are mostly made of ordinary porous inorganic nanoparticles (such as titanium dioxide, aluminum oxide, molecular sieves, cerium oxide and silicon oxide, etc.) as carriers. Filled purification equipment needs to be pressed into tablets or further loaded on other bulky carriers before it can be used, which will complicate the process, and there are problems such as reduced catalytic activity, large air resistance and easy fall off of the catalyst. In order to overcome the above defects, the patent CN201410015867.4 uses TiO 2 prepared by electrospinning as a carrier, and prepares a supported noble metal/TiO 2 composite catalyst by impregnation-room temperature reduction-deposition method. The newly prepared catalyst does not need to be re-loaded, and has High catalytic activity and small air resistance, but the catalyst is brittle because it is based on inorganic TiO2 nanofibers, and the brittleness increases with the decrease of fiber diameter, which will cause It will be broken continuously, and the original fiber structure will be gradually destroyed, so that the air resistance will gradually increase. Moreover, in the subsequent process of noble metal loading, a process of heating and evaporating is required to remove residual chloride ions (from the noble metal precursor), so the process is still relatively complicated. At the same time, there are still some problems in the preparation of TiO 2 fibers by electrospinning, such as high cost, high equipment requirements, and certain difficulties in large-scale production.
发明内容Contents of the invention
本发明所要解决的技术问题在于针对现有技术的不足而提供一种柔性Pt复合甲醛室温氧化催化剂及其制备方法,具体涉及一种Pt/TiO2/棉花纤维复合甲醛室温氧化催化剂及其制备方法。The technical problem to be solved by the present invention is to provide a flexible Pt composite formaldehyde room temperature oxidation catalyst and its preparation method in view of the deficiencies in the prior art, specifically a Pt/TiO 2 /cotton fiber composite formaldehyde room temperature oxidation catalyst and its preparation method .
为解决上述技术问题,本发明采用的技术方案如下:In order to solve the problems of the technologies described above, the technical scheme adopted in the present invention is as follows:
一种Pt/TiO2/棉花纤维复合甲醛室温氧化催化剂,包括棉花纤维载体、TiO2表面涂层和分散在TiO2涂层表面的Pt活性组分,所述的棉花纤维载体为脱脂棉花纤维,其本身就有分等级大孔-中孔结构,所述TiO2涂层为纳米二氧化钛涂层,所述的Pt以零价形式存在,粒径范围1~10nm。A Pt/ TiO2 /cotton fiber composite formaldehyde oxidation catalyst at room temperature, comprising cotton fiber carrier, TiO2 Surface coating and the Pt active component dispersed on the TiO2 coating surface, described cotton fiber carrier is degreased cotton fiber, It itself has a hierarchical macropore-medium pore structure, the TiO 2 coating is a nano-titanium dioxide coating, the Pt exists in a zero-valent form, and the particle size ranges from 1 to 10 nm.
上述方案中,所述铂负载量为0.05~2wt%,其最优的负载量在0.25~0.75wt%。In the above scheme, the platinum loading is 0.05-2wt%, and the optimal loading is 0.25-0.75wt%.
上述Pt/TiO2/棉花纤维复合甲醛室温氧化催化剂的制备方法,首先将钛醇盐在酸性水溶液中发生水解,搅拌后获得稳定的TiO2溶胶;然后通过浸渍法将纳米TiO2均匀地涂附于棉花纤维表面,经分离,干燥,得到TiO2/棉花纤维复合基底材料;然后以TiO2/棉花纤维为基底,以氯铂酸为前驱物,分别加入络合剂和还原剂,再通过浸渍-还原-沉积法将活性组分Pt负载于TiO2涂层表面,最后通过碱洗、水洗多次,除去表面的残留氯离子,得到Pt/TiO2/棉花纤维复合甲醛室温氧化催化剂。The preparation method of the above-mentioned Pt/ TiO2 /cotton fiber composite formaldehyde oxidation catalyst at room temperature, first hydrolyzes the titanium alkoxide in an acidic aqueous solution, and obtains a stable TiO2 sol after stirring; then uniformly coats the nano- TiO2 by the dipping method on the surface of cotton fiber, separated and dried to obtain TiO 2 /cotton fiber composite base material; - Reduction-deposition method loads the active component Pt on the surface of TiO 2 coating, and finally washes with alkali and water several times to remove residual chloride ions on the surface to obtain Pt/TiO 2 /cotton fiber composite formaldehyde oxidation catalyst at room temperature.
按上述方案,所述的Pt/TiO2/棉花纤维复合甲醛室温氧化催化剂的制备方法是将钛醇盐溶于无水乙醇中,加入乙酰丙酮,搅拌形成透明溶液,然后逐滴加到pH=2~3含有PVA的酸性水溶液中,搅拌4~8天获得稳定的溶胶,然后通过浸渍法将TiO2纳米粒子均匀地涂附于棉花纤维表面,经分离、干燥得到TiO2/棉花纤维复合基底材料,其中水,无水乙醇,乙酰丙酮和钛醇盐的摩尔比为=100:2~4:0.1~0.5:0.1~0.5;PVA在酸性水中的含量为0.01~0.1%;以氯铂酸为前驱物,加入络合剂和还原剂,通过浸渍~还原~沉积法将活性组分Pt负载于TiO2涂层表面,最后通过碱洗、水洗多次,除去表面的残留氯离子,干燥后得到Pt/TiO2/棉花纤维复合甲醛室温氧化催化剂。According to the above scheme, the preparation method of the Pt/TiO 2 /cotton fiber composite formaldehyde room temperature oxidation catalyst is to dissolve titanium alkoxide in absolute ethanol, add acetylacetone, stir to form a transparent solution, and then add dropwise to pH= 2-3 days in an acidic aqueous solution containing PVA, stir for 4-8 days to obtain a stable sol, then uniformly coat TiO2 nanoparticles on the surface of cotton fibers by dipping method, separate and dry to obtain a TiO2 /cotton fiber composite substrate Material, wherein the molar ratio of water, absolute ethanol, acetylacetone and titanium alkoxide is =100:2~4:0.1~0.5:0.1~0.5; the content of PVA in acidic water is 0.01~0.1%; As a precursor, complexing agent and reducing agent are added, the active component Pt is loaded on the surface of TiO2 coating by dipping-reduction-deposition method, and finally the residual chloride ions on the surface are removed by alkali washing and water washing for several times, and after drying A Pt/TiO 2 /cotton fiber composite formaldehyde oxidation catalyst at room temperature was obtained.
按上述方案,所述的钛醇盐为钛酸四异丙脂、钛酸四丁酯中的一种或二种的混合物;所述的酸性物质为硝酸,硫酸或二者的混合物;所述的络合剂为柠檬酸三钠或乙二胺四乙酸二钠(EDTA)或二者的混合物;所述的还原剂为硼氢化钾、硼氢化钠或二者的混合物。所述的碱洗为用NaOH,KOH和氨水中的任意一种水溶液或其中二种或三种物质的混合物水溶液洗涤。According to the above scheme, the titanium alkoxide is one or a mixture of tetraisopropyl titanate and tetrabutyl titanate; the acidic substance is nitric acid, sulfuric acid or a mixture of the two; the The complexing agent is trisodium citrate or disodium ethylenediaminetetraacetic acid (EDTA) or a mixture of the two; the reducing agent is potassium borohydride, sodium borohydride or a mixture of the two. The alkali washing is washing with any aqueous solution of NaOH, KOH and ammonia or a mixture of two or three of them.
所述的浸渍法为将棉花纤维浸泡在TiO2溶胶中,浸泡时间为5~10min,其中棉花和TiO2的质量比为1:2~3;所述的分离为滤网分离;干燥条件:先在50~70℃下,干燥3~10min,然后在110~120℃下,干燥20~40min,上述涂附过程可以重复上述过程1~2次,最后一次的干燥温度60~110℃,干燥时间4~12h。The impregnation method is to soak cotton fiber in TiO 2 sol, the soaking time is 5-10min, wherein the mass ratio of cotton and TiO 2 is 1:2-3; the separation is screen separation; drying conditions: First dry at 50-70°C for 3-10 minutes, then at 110-120°C for 20-40 minutes, the above coating process can be repeated 1-2 times, the last drying temperature is 60-110°C, dry Time 4 ~ 12h.
所述的浸渍~还原~沉积法为:将TiO2/棉花纤维复合材料分散于含氯铂酸和络合剂的混合溶液中浸泡5~10min,其中氯铂酸以Pt含量计为占TiO2/棉花纤维复合基底材料的0.05~2wt%,接着加入还原剂的碱性溶液(pH在8.0~10.0间),将贵金属还原成金属纳米粒子,其中氯铂酸,络合剂与还原剂的摩尔比为1:2:5~30,继续搅拌5~10min,接着将沉积有Pt的复合纤维与溶液分离,在60~110℃干燥4~24h,得到Pt/TiO2/棉花纤维复合甲醛室温氧化催化剂。The impregnation-reduction-deposition method is as follows: the TiO 2 /cotton fiber composite material is dispersed in a mixed solution containing chloroplatinic acid and a complexing agent and soaked for 5-10 minutes, wherein chloroplatinic acid accounts for 10% of the TiO 2 in terms of Pt content. / 0.05~2wt% of the cotton fiber composite base material, then add the alkaline solution of reducing agent (pH between 8.0~10.0), the precious metal is reduced into metal nanoparticles, wherein chloroplatinic acid, the mole of complexing agent and reducing agent The ratio is 1:2:5~30, continue stirring for 5~10min, then separate the composite fiber deposited with Pt from the solution, and dry at 60~110℃ for 4~24h to obtain Pt/TiO 2 /cotton fiber composite formaldehyde oxidation at room temperature catalyst.
本发明所提供的Pt/TiO2/棉花纤维复合甲醛室温氧化催化剂具有分等级中孔~大孔结构、轻质和柔性等特点,可避免传统催化剂应用于填充型净化设备中需要压片或进一步将其负载在其它大块型载体上才能使用而产生的气阻大和催化剂易脱落的问题,也可避免像无机纳米纤维在使用过程中存在易折断的问题。Pt与TiO2涂层及载体棉花纤维间结合牢固,活性组分单质Pt在TiO2涂层表面分散性好、粒径在1~10nm间,室温即可高效催化分解甲醛,贵金属用量小,适合于各类空气净化器中使用。The Pt/TiO 2 /cotton fiber composite formaldehyde oxidation catalyst at room temperature provided by the present invention has the characteristics of hierarchical meso-macropore structure, light weight and flexibility, and can avoid the need for tableting or further processing of traditional catalysts in filled purification equipment. The problem of large air resistance and easy falling off of the catalyst caused by loading it on other bulky carriers can also avoid the problem of easy breakage of inorganic nanofibers during use. The combination between Pt, TiO 2 coating and carrier cotton fiber is firm, the active component Pt has good dispersion on the surface of TiO 2 coating, the particle size is between 1 and 10nm, it can efficiently catalyze and decompose formaldehyde at room temperature, and the amount of precious metal is small, suitable for Used in various air purifiers.
与现有技术相比,本发明具有如下有益效果:Compared with the prior art, the present invention has the following beneficial effects:
(1)本发明的催化剂为有机-无机复合结构,Pt与TiO2涂层及载体棉花纤维间结合牢固,同时具有分等级中孔-大孔结构,活性组分Pt组分在载体中分散性好、粒径在1-10nm间并为0价,室温即可高效催化氧化甲醛,气阻小,且贵金属Pt用量小。(1) The catalyst of the present invention is an organic-inorganic composite structure, Pt and TiO 2 Coatings and carrier cotton fibers are firmly combined, and have a hierarchical mesopore-macropore structure, and the active component Pt component is dispersible in the carrier Good, the particle size is between 1-10nm and 0 valence, it can efficiently catalyze the oxidation of formaldehyde at room temperature, the air resistance is small, and the amount of precious metal Pt is small.
(2)催化剂产品具有柔性、质轻、绒团状和不易折断等特点,可直接应用于各种填充型净化设备中,可避免传统催化剂应用于填充型净化设备中需要压片或进一步将其负载在其它大块型载体上才能使用而产生的气阻大和催化剂易脱落的问题,也可避免像无机纳米纤维在使用过程中存在易折断的问题。(2) The catalyst product has the characteristics of flexibility, light weight, fluffy shape and not easy to break, and can be directly applied to various filled purification equipment, which can avoid the need for traditional catalysts to be used in filled purification equipment to be pressed into tablets or further processed. The problem of large air resistance and easy falling off of the catalyst caused by loading on other bulky carriers can also avoid the problem of easy breakage of inorganic nanofibers during use.
(3)由于残留氯离子(来自前驱体氯铂酸)对催化活性具有极大的影响,因此必须除去氯离子,本发明中采用碱洗和水洗的方法除去残留的氯离子,无需后续高温加热除氯过程节约了能耗。(3) Since the residual chloride ions (from the precursor chloroplatinic acid) have a great influence on the catalytic activity, the chloride ions must be removed. In the present invention, the method of alkali washing and water washing is used to remove the residual chloride ions without subsequent high-temperature heating The dechlorination process saves energy consumption.
(4)制备方法工艺简单,原材料来源广、成本低,重复性好,适合工业化生产。(4) The preparation method has simple process, wide sources of raw materials, low cost, good repeatability, and is suitable for industrialized production.
附图说明Description of drawings
图1为本发明实施例1所制备的催化剂样品的FESEM照片。Figure 1 is a FESEM photo of the catalyst sample prepared in Example 1 of the present invention.
图2为本发明实施例1所制备的催化剂样品的TEM(a)和高分辨TEM(b)照片。Fig. 2 is a TEM (a) and a high-resolution TEM (b) photo of the catalyst sample prepared in Example 1 of the present invention.
图3为本发明实施例1所制备的催化剂的XPS谱图。Fig. 3 is the XPS spectrogram of the catalyst prepared in Example 1 of the present invention.
图4为本发明实施例1的催化剂的甲醛室温氧化活性结果图,具体为甲醛浓度随反应时间变化图。Fig. 4 is a graph showing the results of formaldehyde oxidation activity at room temperature of the catalyst of Example 1 of the present invention, specifically a graph showing the variation of formaldehyde concentration with reaction time.
具体实施方式Detailed ways
以下结合本发明的具体实施例,对本发明的发明人内容做进一步作描述,但是本发明的保护范围并不限于这些实施例。凡是不背离本发明构思的改变或等同替代均包括在本发明的保护范围之内。The inventors of the present invention will be further described below in conjunction with specific embodiments of the present invention, but the protection scope of the present invention is not limited to these embodiments. All changes or equivalent substitutions that do not depart from the concept of the present invention are included in the protection scope of the present invention.
实施例1Example 1
(1)首先将钛酸丁酯溶于无水乙醇中,加入乙酰丙酮,搅拌形成透明溶液,然后逐滴加到含有0.01%的PVA的酸性(pH=2)水溶液中,搅拌6天获得稳定的TiO2溶胶,其中水,无水乙醇,乙酰丙酮和钛酸丁酯的摩尔比为=100:2:0.5:0.5。(1) First, dissolve butyl titanate in absolute ethanol, add acetylacetone, stir to form a transparent solution, then add dropwise to an acidic (pH=2) aqueous solution containing 0.01% PVA, and stir for 6 days to obtain a stable solution TiO 2 sol, wherein the molar ratio of water, absolute ethanol, acetylacetone and butyl titanate is =100:2:0.5:0.5.
(2)将脱脂棉浸泡在步骤(1)的TiO2溶胶中,浸泡时间为5min,其中脱脂棉和TiO2的质量比为1:2.0;经滤网分离后,先在60℃下干燥5min,再在115℃下干燥30min,再重复上述过程,但干燥温度为60℃,干燥时间为12h,得到TiO2/棉花纤维复合基底材料。(2) Soak the absorbent cotton in the TiO2sol of step (1), the soaking time is 5min, wherein the mass ratio of absorbent cotton and TiO2 is 1 :2.0; Dry at 115° C. for 30 minutes, and repeat the above process, but the drying temperature is 60° C., and the drying time is 12 hours to obtain a TiO 2 /cotton fiber composite base material.
(3)再将氯铂酸溶液中加入络合剂柠檬酸三钠,搅拌均匀,将步骤(2)中获得的TiO2/棉花纤维复合基底材料分散于上述混合溶液中浸泡5min,其中氯铂酸以铂计相对于TiO2/棉花纤维复合基底材料的质量为0.5wt%,再加入还原剂硼氢化钾的碱性溶液(pH值用0.5M的NaOH溶液调节为10左右),将氯铂酸还原成金属纳米粒子,其中氯铂酸,络合剂与还原剂的摩尔比为1:2:30,继续搅拌5min,接着将负载有铂的棉花纤维分离,再用0.1M的NaOH洗涤3遍,去离子水洗涤3遍,然后60℃干燥12h,得到Pt/TiO2/棉花纤维室温氧化催化剂。(3) Add complexing agent trisodium citrate to the chloroplatinic acid solution, stir evenly, and disperse the TiO2 /cotton fiber composite base material obtained in step (2) in the above-mentioned mixed solution and soak for 5min, wherein platinum chloride Acid is 0.5wt% in terms of platinum relative to the quality of TiO2 /cotton fiber composite base material, then add the alkaline solution of reducing agent potassium borohydride (the pH value is adjusted to about 10 with 0.5M NaOH solution), and the platinum chloride Acid reduction into metal nanoparticles, wherein the molar ratio of chloroplatinic acid, complexing agent and reducing agent is 1:2:30, continue to stir for 5min, then separate the cotton fibers loaded with platinum, and then wash with 0.1M NaOH for 3 and then washed three times with deionized water, and then dried at 60° C. for 12 hours to obtain a Pt/TiO 2 /cotton fiber room temperature oxidation catalyst.
上述制备的Pt/TiO2/棉花纤维的FESEM,TEM和XPS谱图分析分别见图1,图2和图3,图1中可见,所述的Pt/TiO2/棉花纤维在涂附TiO2及负载Pt前后纤维结构得到完好保持,其中TiO2粒径在1-10nm间,涂层均匀地负载在棉花纤维表面,贵金属Pt以零价单质形式存在(这由图3中的71.2eV和74.8eV两个特征峰可看出)粒径范围3~10nm,高度分散在TiO2涂层表面。The FESEM, TEM and XPS spectrogram analysis of the Pt/TiO 2 /cotton fibers prepared above are shown in Fig. 1, Fig. 2 and Fig. 3 respectively, and it can be seen in Fig. 1 that the Pt/TiO 2 /cotton fibers are coated with TiO 2 And before and after loading Pt, the fiber structure is well maintained, wherein the TiO 2 particle size is between 1-10nm, the coating is evenly loaded on the surface of the cotton fiber, and the noble metal Pt exists in the form of zero-valent simple substance (this is determined by the 71.2eV and 74.8 The two characteristic peaks of eV can be seen) the particle size ranges from 3 to 10nm, and is highly dispersed on the surface of the TiO 2 coating.
实施例2甲醛室温氧化催化剂的制备Preparation of embodiment 2 formaldehyde room temperature oxidation catalyst
(1)首先将钛酸丁酯溶于无水乙醇中,加入乙酰丙酮,搅拌形成透明溶液,然后逐滴加到含有0.05%的PVA的酸性(pH=2.5)水溶液中,搅拌8天获得稳定的TiO2溶胶,其中水,酸,无水乙醇,乙酰丙酮和钛酸丁酯的摩尔比为=100:4:0.5:0.5。(1) First, dissolve butyl titanate in absolute ethanol, add acetylacetone, stir to form a transparent solution, then add dropwise to an acidic (pH=2.5) aqueous solution containing 0.05% PVA, and stir for 8 days to obtain a stable solution TiO 2 sol, wherein the molar ratio of water, acid, absolute ethanol, acetylacetone and butyl titanate = 100:4:0.5:0.5.
(2)将脱脂棉浸泡在步骤(1)的TiO2溶胶中,浸泡时间为5min,其中棉花和TiO2的质量比为1:2.5,经滤网分离后,在60℃下干燥12h,得到TiO2/棉花纤维复合基底材料。(2) Soak the absorbent cotton in the TiO sol in step (1) for 5 minutes, wherein the mass ratio of cotton to TiO 2 is 1:2.5, and after being separated by a filter screen, dry it at 60°C for 12 hours to obtain TiO 2 / Cotton fiber composite base material.
(3)再将氯铂酸溶液中加入络合剂柠檬酸三钠,搅拌均匀,将步骤(2)中获得的TiO2/棉花纤维复合基底材料分散于上述混合溶液中浸泡5min,其中氯铂酸以铂计相对于TiO2/棉花纤维复合基底材料的质量为0.25wt%,再加入还原剂硼氢化钾的碱性溶液(pH值用0.5M的NaOH溶液调节为8左右),将氯铂酸还原成Pt纳米粒子,其中氯铂酸,络合剂与还原剂的摩尔比为1:2:15,继续搅拌5min,接着将负载有铂的棉花纤维分离,再用0.1M的KOH洗涤3遍,去离子水洗涤3遍,然后80℃干燥10h,得到Pt/TiO2/棉花纤维室温氧化催化剂。(3) Add complexing agent trisodium citrate to the chloroplatinic acid solution, stir evenly, and disperse the TiO2 /cotton fiber composite base material obtained in step (2) in the above-mentioned mixed solution and soak for 5min, wherein platinum chloride Acid is 0.25wt% in terms of platinum relative to the quality of TiO2 /cotton fiber composite base material, then add the alkaline solution of reducing agent potassium borohydride (the pH value is adjusted to about 8 with 0.5M NaOH solution), and the platinum chloride Acid reduction into Pt nanoparticles, wherein the molar ratio of chloroplatinic acid, complexing agent and reducing agent is 1:2:15, continue to stir for 5min, then separate the cotton fibers loaded with platinum, and then wash with 0.1M KOH for 3 and washed three times with deionized water, and then dried at 80°C for 10 hours to obtain a Pt/TiO 2 /cotton fiber room temperature oxidation catalyst.
实施例3甲醛室温氧化催化剂的制备Preparation of embodiment 3 formaldehyde room temperature oxidation catalyst
(1)首先将钛酸丁酯溶于无水乙醇中,加入乙酰丙酮,搅拌形成透明溶液,然后逐滴加到含有0.01%的PVA的酸性(pH=3)水溶液中,搅拌4天获得稳定的TiO2溶胶,其中水,无水乙醇,乙酰丙酮和钛酸丁酯的摩尔比为=100:2:0.1:0.1。(1) First, dissolve butyl titanate in absolute ethanol, add acetylacetone, stir to form a transparent solution, then add dropwise to an acidic (pH=3) aqueous solution containing 0.01% PVA, and stir for 4 days to obtain a stable solution TiO 2 sol, wherein the molar ratio of water, absolute ethanol, acetylacetone and butyl titanate = 100:2:0.1:0.1.
(2)将脱脂棉浸泡在TiO2溶胶中,浸泡时间为5min,其中棉花和TiO2的质量比为1:2,经滤网分离后,在80℃,干燥时间为10h,得到TiO2/棉花纤维复合基底材料。(2) Soak absorbent cotton in TiO 2 sol for 5 minutes, in which the mass ratio of cotton and TiO 2 is 1:2, after separation by filter screen, dry at 80°C for 10 hours to obtain TiO 2 /cotton Fiber composite base material.
(3)再将氯铂酸溶液中加入络合剂柠檬酸三钠,搅拌均匀,将步骤(2)中获得的TiO2/棉花纤维复合基底材料分散于上述混合溶液中浸泡5min,其中氯铂酸以铂计相对于TiO2/棉花纤维复合基底材料的质量为0.1wt%,再加入还原剂硼氢化钾的碱性溶液(pH值用0.5M的NaOH溶液调节为8左右),将氯铂酸还原成Pt纳米粒子,其中氯铂酸,络合剂与还原剂的摩尔比为1:2:5,继续搅拌5min,接着将负载有铂的棉花纤维分离,再用0.2M的NaOH洗涤3遍,去离子水洗涤3遍,然后60℃干燥12h,得到Pt/TiO2/棉花纤维室温氧化催化剂。(3) Add complexing agent trisodium citrate to the chloroplatinic acid solution, stir evenly, and disperse the TiO2 /cotton fiber composite base material obtained in step (2) in the above-mentioned mixed solution and soak for 5min, wherein platinum chloride Acid is 0.1wt% in terms of platinum relative to the quality of TiO2 /cotton fiber composite base material, then add the alkaline solution of reducing agent potassium borohydride (the pH value is adjusted to about 8 with 0.5M NaOH solution), and the platinum chloride Acid reduction into Pt nanoparticles, wherein the molar ratio of chloroplatinic acid, complexing agent and reducing agent is 1:2:5, continue to stir for 5min, then separate the cotton fibers loaded with platinum, and wash with 0.2M NaOH for 3 and then washed three times with deionized water, and then dried at 60° C. for 12 hours to obtain a Pt/TiO 2 /cotton fiber room temperature oxidation catalyst.
实施例4甲醛室温氧化催化剂的制备Preparation of embodiment 4 formaldehyde room temperature oxidation catalyst
(1)首先将钛酸丁酯溶于无水乙醇中,加入乙酰丙酮,搅拌形成透明溶液,然后逐滴加到含有0.01%的PVA的酸性(pH=2)水溶液中,搅拌6天获得稳定的TiO2溶胶,其中水,无水乙醇,乙酰丙酮和钛酸丁酯的摩尔比为=100:3:0.25:0.25。(1) First, dissolve butyl titanate in absolute ethanol, add acetylacetone, stir to form a transparent solution, then add dropwise to an acidic (pH=2) aqueous solution containing 0.01% PVA, and stir for 6 days to obtain a stable solution TiO 2 sol, wherein the molar ratio of water, absolute ethanol, acetylacetone and butyl titanate = 100:3:0.25:0.25.
(2)将脱脂棉浸泡在TiO2溶胶中,浸泡时间为10min,其中棉花和TiO2的质量比为1:3.0,经滤网分离后,先在60℃下干燥10min,再在60℃,干燥时间为12h,得到TiO2/棉花纤维复合基底材料。(2) Soak the absorbent cotton in TiO 2 sol for 10 minutes, wherein the mass ratio of cotton and TiO 2 is 1:3.0, after being separated by a filter, first dry at 60°C for 10 minutes, and then dry at 60°C The time is 12 hours, and the TiO 2 /cotton fiber composite base material is obtained.
(3)再将氯铂酸溶液中加入络合剂柠檬酸三钠,搅拌均匀,将步骤(2)中获得的TiO2/棉花纤维复合基底材料分散于上述混合溶液中浸泡10min,其中氯铂酸以铂计相对于TiO2/棉花纤维复合基底材料的质量为0.75wt%,再加入还原剂硼氢化钠的碱性溶液(pH值用0.5M的NaOH溶液调节为9左右),将氯铂酸还原成Pt纳米粒子,其中氯铂酸,络合剂与还原剂的摩尔比为1:2:15,继续搅拌5min,接着将负载有铂的棉花纤维分离,再用0.1M的氨水洗涤3遍,去离子水洗涤3遍,然后100℃干燥6h,得到Pt/TiO2/棉花纤维室温氧化催化剂。(3) Add the complexing agent trisodium citrate to the chloroplatinic acid solution, stir evenly, and disperse the TiO2 /cotton fiber composite base material obtained in step (2) in the above-mentioned mixed solution and soak for 10min, wherein the chloroplatinic acid Acid is 0.75wt% in terms of platinum relative to the quality of TiO2 /cotton fiber composite base material, then add the alkaline solution of reducing agent sodium borohydride (the pH value is adjusted to about 9 with 0.5M NaOH solution), and the platinum chloride Acid reduction into Pt nanoparticles, wherein the molar ratio of chloroplatinic acid, complexing agent and reducing agent is 1:2:15, continue to stir for 5 minutes, then separate the cotton fibers loaded with platinum, and then wash with 0.1M ammonia water for 3 and washed three times with deionized water, and then dried at 100° C. for 6 hours to obtain a Pt/TiO 2 /cotton fiber room temperature oxidation catalyst.
实施例5甲醛室温氧化催化剂的制备Preparation of embodiment 5 formaldehyde room temperature oxidation catalyst
(1)首先将钛酸四异丙酯溶于无水乙醇中,加入乙酰丙酮,搅拌形成透明溶液,然后逐滴加到含有0.1%的PVA的酸性(pH=2)水溶液中,搅拌6天获得稳定的TiO2溶胶,其中水,无水乙醇,乙酰丙酮和钛酸四异丙酯的摩尔比为=100:2:0.5:0.5。(1) First, dissolve tetraisopropyl titanate in absolute ethanol, add acetylacetone, stir to form a transparent solution, then add dropwise to an acidic (pH=2) aqueous solution containing 0.1% PVA, and stir for 6 days A stable TiO sol was obtained in which the molar ratio of water, absolute ethanol, acetylacetone and tetraisopropyl titanate was = 100:2:0.5:0.5.
(2)将脱脂棉浸泡在TiO2溶胶中,浸泡时间为5min,其中棉花和TiO2的质量比为1:2,经滤网分离后,先在60℃下干燥5min,再在100℃下干燥6h,得到TiO2/棉花纤维复合基底材料。(2) Soak absorbent cotton in TiO 2 sol for 5 minutes, in which the mass ratio of cotton and TiO 2 is 1:2. After being separated by a filter, first dry at 60°C for 5 minutes, and then dry at 100°C 6h, TiO 2 /cotton fiber composite base material was obtained.
(3)再将氯铂酸溶液中加入络合剂柠檬酸三钠,搅拌均匀,将步骤(2)中获得的TiO2/棉花纤维复合基底材料分散于上述混合溶液中浸泡5min,其中氯铂酸以铂计相对于TiO2/棉花纤维复合基底材料的质量为1.0wt%,再加入还原剂硼氢化钠的碱性溶液(pH值用0.5M的NaOH溶液调节为10左右),将氯铂酸还原成Pt纳米粒子,其中氯铂酸,络合剂与还原剂的摩尔比为1:2:30,继续搅拌5min,接着将负载有铂的棉花纤维分离,再用各自为0.1M的NaOH和KOH混合液洗涤3遍,去离子水洗涤3遍,然后60℃干燥12h,得到Pt/TiO2/棉花纤维室温氧化催化剂。(3) Add complexing agent trisodium citrate to the chloroplatinic acid solution, stir evenly, and disperse the TiO2 /cotton fiber composite base material obtained in step (2) in the above-mentioned mixed solution and soak for 5min, wherein platinum chloride Acid is 1.0wt% in terms of platinum relative to the quality of TiO2 /cotton fiber composite base material, then add the alkaline solution of reducing agent sodium borohydride (the pH value is adjusted to about 10 with 0.5M NaOH solution), and the platinum chloride Acid reduction into Pt nanoparticles, wherein the molar ratio of chloroplatinic acid, complexing agent and reducing agent is 1:2:30, continue to stir for 5min, then separate the cotton fibers loaded with platinum, and then use 0.1M NaOH Wash with KOH mixed solution for 3 times and deionized water for 3 times, then dry at 60° C. for 12 hours to obtain Pt/TiO 2 /cotton fiber room temperature oxidation catalyst.
实施例6甲醛室温氧化催化剂的制备The preparation of embodiment 6 formaldehyde room temperature oxidation catalyst
(1)首先将钛酸四异丙酯溶于无水乙醇中,加入乙酰丙酮,搅拌形成透明溶液,然后逐滴加到含有0.1%的PVA的酸性(pH=2.5)水溶液中,搅拌6天获得稳定的TiO2溶胶,其中水,无水乙醇,乙酰丙酮和钛酸四异丙酯的摩尔比为=100:2:0.25:0.25.(1) First dissolve tetraisopropyl titanate in absolute ethanol, add acetylacetone, stir to form a transparent solution, then add dropwise to an acidic (pH=2.5) aqueous solution containing 0.1% PVA, and stir for 6 days A stable TiO sol was obtained in which the molar ratio of water, absolute ethanol, acetylacetone and tetraisopropyl titanate was = 100:2:0.25:0.25.
(2)将脱脂棉浸泡在TiO2溶胶中,浸泡时间为8min,其中棉花和TiO2的质量比为1:2.5,经滤网分离后,先在60℃下干燥5min,再在120℃,干燥时间为4h,得到TiO2/棉花纤维复合基底材料。(2) Soak the absorbent cotton in TiO 2 sol for 8 minutes, and the mass ratio of cotton to TiO 2 is 1:2.5. After being separated by a filter, first dry it at 60°C for 5 minutes, and then dry it at 120°C. The time is 4 hours, and the TiO 2 /cotton fiber composite base material is obtained.
(3)再将氯铂酸溶液中加入络合剂EDTA,搅拌均匀,将步骤(2)中获得的TiO2/棉花纤维复合基底材料分散于上述混合溶液中浸泡8min,其中氯铂酸以铂计相对于TiO2/棉花纤维复合基底材料的质量为2.0wt%,再加入还原剂硼氢化钠的碱性溶液(pH值用0.5M的NaOH溶液调节为9左右),将氯铂酸还原成Pt纳米粒子,其中氯铂酸,络合剂与还原剂的摩尔比为1:2:25,继续搅拌5min,接着将负载有铂的棉花纤维分离,再用各自为0.05M的NaOH、KOH和氨水混合溶液洗涤3遍,去离子水洗涤3遍,然后110℃干燥4h,得到Pt/TiO2/棉花纤维室温氧化催化剂。(3) Add the complexing agent EDTA in the chloroplatinic acid solution again, stir evenly, the TiO2 /cotton fiber composite base material obtained in the step (2) is dispersed in the above-mentioned mixed solution and soaked for 8min, wherein the chloroplatinic acid is mixed with platinum Meter is 2.0wt% with respect to the quality of TiO2 /cotton fiber composite base material, then add the alkaline solution of reducing agent sodium borohydride (the pH value is adjusted to about 9 with the NaOH solution of 0.5M), the chloroplatinic acid is reduced into Pt nanoparticles, wherein the molar ratio of chloroplatinic acid, complexing agent and reducing agent is 1:2:25, continue to stir for 5min, then separate the cotton fibers loaded with platinum, and then use 0.05M NaOH, KOH and The mixed solution of ammonia and water was washed 3 times, and deionized water was washed 3 times, and then dried at 110°C for 4 hours to obtain a Pt/TiO 2 /cotton fiber room temperature oxidation catalyst.
实施例7甲醛室温氧化催化剂的制备Preparation of embodiment 7 formaldehyde room temperature oxidation catalyst
(1)首先将钛酸四异丙酯溶于无水乙醇中,加入乙酰丙酮,搅拌形成透明溶液,然后逐滴加到含有0.25%的PVA的酸性(pH=2)水溶液中,搅拌4天获得稳定的TiO2溶胶,其中水,无水乙醇,乙酰丙酮和钛酸四异丙酯的摩尔比为=100:2:0.1:0.1。(1) First, dissolve tetraisopropyl titanate in absolute ethanol, add acetylacetone, stir to form a transparent solution, then add dropwise to an acidic (pH=2) aqueous solution containing 0.25% PVA, and stir for 4 days A stable TiO sol was obtained in which the molar ratio of water, absolute ethanol, acetylacetone and tetraisopropyl titanate was = 100:2:0.1:0.1.
(2)将脱脂棉浸泡在TiO2溶胶中,浸泡时间为5min,其中棉花和TiO2的质量比为1:2.6,经滤网分离后,在60℃下干燥4min,再在115℃,干燥时间为30min,重复上述过程1次,最后在110℃下干燥4h,得到TiO2/棉花纤维复合基底材料。(2) Soak absorbent cotton in TiO 2 sol for 5 minutes, in which the mass ratio of cotton and TiO 2 is 1:2.6, after being separated by a filter, dry at 60°C for 4 minutes, and then at 115°C for a drying time Repeat the above process once for 30 minutes, and finally dry at 110°C for 4 hours to obtain a TiO 2 /cotton fiber composite base material.
(3)再将氯铂酸溶液中加入络合剂EDTA,搅拌均匀,将步骤(2)中获得的TiO2/棉花纤维复合基底材料分散于上述混合溶液中浸泡5min,其中氯铂酸以铂计相对于TiO2/棉花纤维复合基底材料的质量为0.25wt%,再加入还原剂硼氢化钠的碱性溶液(pH值用0.5M的NaOH溶液调节为10左右),将氯铂酸还原成Pt纳米粒子,其中氯铂酸,络合剂与还原剂的摩尔比为1:2:15,继续搅拌5min,接着将负载有铂的棉花纤维分离,再用0.1M的KOH洗涤3遍,去离子水洗涤3遍,然后60℃干燥12h,得到Pt/TiO2/棉花纤维室温氧化催化剂。(3) Add complexing agent EDTA in the chloroplatinic acid solution again, stir evenly, the TiO2 /cotton fiber composite base material obtained in the step (2) is dispersed in the above-mentioned mixed solution and soaked for 5min, wherein chloroplatinic acid is mixed with platinum Meter is 0.25wt% relative to the quality of TiO2 /cotton fiber composite base material, then add the alkaline solution of reducing agent sodium borohydride (the pH value is adjusted to about 10 with the NaOH solution of 0.5M), the chloroplatinic acid is reduced into Pt nanoparticles, wherein the molar ratio of chloroplatinic acid, complexing agent and reducing agent is 1:2:15, continue to stir for 5min, then separate the cotton fibers loaded with platinum, and then wash 3 times with 0.1M KOH to remove Washing with ion water for 3 times, and then drying at 60° C. for 12 hours to obtain a Pt/TiO 2 /cotton fiber room temperature oxidation catalyst.
为考察本发明制备的催化剂在室温下催化氧化降解甲醛效果,本发明人按以下方法对其室温降解甲醛性能进行测试。测试过程如下:取催化剂0.3g平铺于直径为14cm的表面皿表面,盖上玻璃盖,然后将该附着有催化剂的表面皿至于5.9L的有机玻璃反应器中,反应器内底部放置一个5W的风扇,再将一定量的浓甲醛溶液注入反应器内,打开风扇,至甲醛挥发直至浓度平衡,将玻璃盖移去,此时催化剂与甲醛开始接触反应,在此过程中通过多组分气体分析仪(INNOVA air Tech Instruments Model 1412)在线监测甲醛和产物二氧化碳的浓度变化。In order to investigate the catalytic oxidation degradation effect of the catalyst prepared by the present invention on the degradation of formaldehyde at room temperature, the inventors tested its performance on degradation of formaldehyde at room temperature according to the following method. The test process is as follows: Take 0.3g of the catalyst and spread it on the surface of a watch glass with a diameter of 14cm, cover the glass cover, and then place the watch glass with the catalyst attached in a 5.9L plexiglass reactor, and place a 5W glass reactor at the bottom of the reactor. Then inject a certain amount of concentrated formaldehyde solution into the reactor, turn on the fan, and remove the glass cover until the formaldehyde volatilizes until the concentration is balanced. At this time, the catalyst and formaldehyde start to contact and react. The analyzer (INNOVA air Tech Instruments Model 1412) monitored the concentration changes of formaldehyde and product carbon dioxide online.
实施例1~7中制备的催化剂的60min活性数据见表1。从表1可知,本发明的催化剂在比较低的Pt负载量的条件下,均具有良好的催化活性。The 60min activity data of the catalysts prepared in Examples 1-7 are shown in Table 1. It can be seen from Table 1 that the catalysts of the present invention have good catalytic activity under the condition of relatively low Pt loading.
表1Table 1
另为考察本发明催化剂的重复使用性能,特将实施例1的催化剂样品重复使用4次,观察其重复性能,结果见表2,由表2可看出:本发明的催化剂在多次的使用过程中,活性基本保持不变,说明本发明催化剂活性稳定。In addition, for investigating the reusability of the catalyst of the present invention, the catalyst sample of Example 1 is reused 4 times, and its reproducibility is observed. The results are shown in Table 2. As can be seen from Table 2: the catalyst of the present invention is used repeatedly. During the process, the activity remains basically unchanged, indicating that the activity of the catalyst of the present invention is stable.
表2Table 2
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