Carbon coating of anatase-type TiO2 and photoactivity

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TiO2纳米管内限域纳米Ru及其光催化降解罗丹明B的性能研究

TiO2纳米管内限域纳米Ru及其光催化降解罗丹明B的性能研究

TiO2纳米管内限域纳米Ru及其光催化降解罗丹明B的性能研究余翔;钟颖贤;杨旭;李新军【摘要】采用丙基三甲氧基硅烷(KH570)偶联剂对 TiO2纳米管外表面进行疏水改性,通过浸渍法再经氢气热还原法将 Ru 纳米颗粒原位选择性沉积在 TiO2纳米管内。

采用 TEM、HREM、EDS、HAADF-STEM和紫外可见吸收光谱仪分别对形貌和结构进行表征。

结果表明,内嵌于 TiO2纳米管的 Ru 纳米颗粒粒径约为2~3 nm,TiO2纳米管内负载 w =2% Ru 的光催化性能最好,其光降解罗丹明B 的效率大约是单一 TiO2纳米管的1.8倍。

%The exterior surfaces of the TiO2 nanotube (TNT)were modified by a silane coupling agent to make nano-Ru selectively deposit on the inner wall.The as prepared catalysts were characterized by transmission electron microscope (TEM),high-resolution transmission electron microscopy (HREM), energy dispersive spectrometer (EDS),high-angle annular dark field image (HAADF),scanning trans-mission electron microscopy (STEM)and UV-vis absorption spectra.The results confirm that nano-Ru particles in the range of 2 ~3 nm in diameter are entrapped in the TNTs.TNTs-confined 2% Ru exhibits the best photocatalytic performance,which photocatalytic efficient is 1 .8 times of pure TNTs.【期刊名称】《中山大学学报(自然科学版)》【年(卷),期】2016(055)002【总页数】4页(P85-88)【关键词】水热法;限域催化;TiO2 纳米管;贵金属【作者】余翔;钟颖贤;杨旭;李新军【作者单位】暨南大学生命科学与技术学院化学系,广东广州 510632; 中国科学院广州能源研究所中国科学院可再生能源重点实验室,广东广州 510640;暨南大学生命科学与技术学院化学系,广东广州 510632;中国科学院广州能源研究所中国科学院可再生能源重点实验室,广东广州 510640;中国科学院广州能源研究所中国科学院可再生能源重点实验室,广东广州 510640【正文语种】中文【中图分类】X703环境污染与能源危机是当今世界面临的重要问题,如何解决是摆在人类面前的迫切问题。

甘油磷酸钙浓度对钛合金MAO_涂层性能的影响

甘油磷酸钙浓度对钛合金MAO_涂层性能的影响

表面技术第53卷第9期甘油磷酸钙浓度对钛合金MAO涂层性能的影响肖水清,秦晋,王学禹,赵融芳,张荣发*(江西科技师范大学,南昌 330038)摘要:目的提高医用钛合金的生物活性。

方法在含葡萄糖酸钙(CaGlu2)、葡萄糖酸镁(MgGlu2)、植酸钠(Na12Phy)和磷酸(H3PO4)的基本溶液中,分别添加8、10、12 g/L甘油磷酸钙(Ca-GP),采用MAO 方法在Ti-6Al-4V表面制备3种涂层。

使用SEM、EDS、XRD、XPS和AFM检测涂层表面形貌、化学成分、物相结构、元素存在状态和表面粗糙度,并测试涂层的接触角、结合强度以及体外生物活性。

结果经过MAO处理后,钛合金表面可成功生长出多孔陶瓷涂层,Ca-GP参与了MAO涂层形成。

当Ca-GP的质量浓度为8 g/L时,涂层非常粗糙,Ca和Mg的原子数分数分别为7.56%和1.74%。

随着Ca-GP浓度的增加,微孔均匀性变好,表面微裂纹减少,且钙磷原子比(Ca/P)显著提高。

在含8、10 g/L的Ca-GP溶液中,制备的涂层以Ti、锐钛矿和金红石型TiO2组成为主;在12 g/L的Ca-GP溶液中生成的涂层,Ca/P原子比可达1.77,含有TiP2O7、Mg3(PO4)2和少量HA。

Ca-GP能显著增加涂层的粗糙度,且稍微增加涂层与基体之间的结合强度。

接触角测试结果表明,Ca-GP能明显改善涂层的亲水性。

结论随着Ca-GP浓度增加,涂层中钙含量增加,表明钙离子通过扩散进入MAO涂层中。

在含12 g/L Ca-GP溶液中制备的涂层,含TiP2O7、Mg3(PO4)2和HA,且Ca/P原子比与HA中的Ca/P原子比接近。

模拟体液中浸泡试验结果表明,添加12 g/L Ca-GP制备的MAO样品,表面形成了大量颗粒状HA,表现出优异的体外生物活性。

关键词:钛合金;微弧氧化;钙磷比;HA;生物活性中图分类号:TG174.4 文献标志码:A 文章编号:1001-3660(2024)09-0056-09DOI:10.16490/ki.issn.1001-3660.2024.09.006Effect of Calcium Glycerophosphate Concentration on Propertiesof MAO Coatings Developed on Titanium AlloysXIAO Shuiqing, QIN Jin, WANG Xueyu, ZHAO Rongfang, ZHANG Rongfa*(Jiangxi Science and Technology Normal University, Nanchang 330038, China)ABSTRACT: Titanium alloys have been widely used as implant materials due to their low density and elastic modulus, good biocompatibility and excellent corrosion resistance. However, they belong to bio-inert materials, which prevents the titanium implant from tightly bonding with the bone tissue. As a surface treatment method, micro-arc oxidation (MAO) can effectively improve the property of titanium alloys but may generate industrial wastewater. Therefore, selecting environmental friendly electrolytes to prepare high bioactive MAO coatings on the surface of titanium alloys will become the investigation focus. In this study, the environmentally friendly sodium phytate (Na12Phy) was used as the organic phosphorus-containing electrolyte. In收稿日期:2024-03-26;修订日期:2024-04-15Received:2024-03-26;Revised:2024-04-15基金项目:国家自然科学基金(52261017,52061013)Fund:National Natural Science Foundation of China (52261017, 52061013)引文格式:肖水清, 秦晋, 王学禹, 等. 甘油磷酸钙浓度对钛合金MAO涂层性能的影响[J]. 表面技术, 2024, 53(9): 56-64.XIAO Shuiqing, QIN Jin, WANG Xueyu, et al. Effect of Calcium Glycerophosphate Concentration on Properties of MAO Coatings Developed on Titanium Alloys[J]. Surface Technology, 2024, 53(9): 56-64.*通信作者(Corresponding author)第53卷第9期肖水清,等:甘油磷酸钙浓度对钛合金MAO涂层性能的影响·57·addition, calcium gluconate (CaGlu2), magnesium gluconate (MgGlu2) and calcium glycerophosphate (Ca-GP), commonly used in food and pharmaceutical industries, were separately selected as the calcium and magnesium sources in the coatings. Three anodic coatings were prepared by MAO treatment under constant voltage mode in a base solution containing 20.19 g/L CaGlu2,6.24 g/L MgGlu2, 5 g/L Na12Phy and 1.3 g/L phosphoric acid (H3PO4) added with 8, 10 and 12 g/L Ca-GP. Coating surfacemorphology, chemical composition, phase structure, elemental existing stage, and roughness were analyzed by scanning electron microscope (SEM), energy dispersive X-sight spectrophotometer (EDS), X-ray diffraction (XRD), X-ray photoelectron spectrophotometer (XPS) and Atomic Force Microscope (AFM). In addition, static contact angle, bond strength and in vitro bioactivity of three MAO coatings were also measured. After MAO treatment, ceramic coatings with porous characteristics were successfully developed on titanium alloys and Ca-GP took part in coating formation. When Ca-GP was 8 g/L, the developed coating was very rough with evident micro cracks and its amounts of Ca and Mg elements were separately 7.56at.% and1.74at.%. With the increasing Ca-GP concentration, the coating uniformity about surface micro pores became well with lessmicro cracks. The increasing Ca-GP concentration could improve the Ca content in MAO coatings, indicating that Ca ions entered the MAO coating by diffusion. Ca-GP concentration could significantly increase the calcium-phosphorus ratios (Ca/P) of MAO coatings and the values fabricated in the base solution with 8, 10 and 12 g/L Ca-GP were separately 0.98, 1.33 and1.77. The developed MAO coatings in the solution added with 8 and 10 g/L Ca-GP were mainly composed of Ti, rutile, andanatase-type TiO2. However, in the base solution added with 12 g/L Ca-GP, the fabricated MAO coating contained TiP2O7, Mg3(PO4)2 and a small amount of hydroxyapatite (HA). Ca-GP significantly improved the coating roughness but slightly increased the bonding strength between the substrate and coating. The results obtained by measuring contact angle indicated that Ca-GP could significantly improve the hydrophilicity of MAO coatings. According to phase structure and the similar Ca/P ratio to that of HA, the prepared coating in the solution containing 12 g/L Ca-GP exhibits excellent bioactivity. The results obtained through immersion experiments in simulated body fluids show that a large amount of granular HA is formed on the surface of MAO coating fabricated in the base solution added with 12 g/L Ca-GP, which further shows that the MAO coating achieves excellent in vitro bioactivity.KEY WORDS: titanium alloy; micro-arc oxidation; calcium-phosphorus ratio; HA; bioactivity钛合金因密度小、比强度高、弹性模量低以及优异的耐蚀性和生物相容性,是一种较常用的医用金属材料[1-2]。

Inactivated properties of activated carbon-supported TiO_2 nanoparticles for bacteria and kineti

Inactivated properties of activated carbon-supported TiO_2 nanoparticles for bacteria and kineti

Journal of Environmental Scienc es20(2008)1527–1533Inactivated properties of activated carbon-supported TiO2nanoparticles forbacter ia and kinetic studyLI Youji,MA Mingyuan,WANG Xiaohu,WANG XiaohuaCollege of Chemistry and Chem ical Engineering,Jishou University,Hunan416000,China.E-mail:bccly j@Received10December2007;revised16January2008;accepted19February2008Abstr a ctThe activated carbon-supported TiO2nanoparticles(TiO2/AC)were prepared by a properly controlled sol-gel method.The e ects of activated carbons(AC)support on inac tivated properties of TiO2nanoparticles were e valuated by photocatalytic inactivation experiments of Escher ichia coli.The key factors a ec ting the inactivation e ciency were investigated,including electric power of lamp, temperature,and pH values.The results show that the TiO2/AC composite s have high inactivation properties of E.coli in comparison with pure TiO2powder.The kinetics of photocata lytic inactivation of E.coli was found to follow a pseudo-rst order rate law for TiO2/AC composites,and kinetic behavior could be describe d in terms of a modi ed Langmuir-Hinshelwood model.The values of the adsorption equilibrium constants for the bacteria,K c,and for the rate constants,k r,were ce rtainly depended on TiO2content.At47 wt.%TiO2coatings with the highest rate constant,the K c and k r were1.17×108L/cfu and1.43×106cfu/(L min),respectively.The variety of parameters shows signi cant e ects on inactiva tion rate.The outer layer of bacteria decomposed rst resulting in inactivation of cell,a nd with further illum ination,the cells nearly decompose d.Key wor ds:inactivation;activated carbon-supported TiO2;sol-gel method;bacteriaIntroductionDisinfection of water by chlorine or ozone has been carried out for about one hundred years.However,some chlorine residuals in water are toxic to many aquatic organisms,and some byproducts of chlorination in water such as trihalomethane may be carcinogenic.T o avoid adding chemicals to the drinking water,disinfection by photocatalysis with titanium dioxide(T iO2)is generating considerable interest in recent years(Li et al.,1996). There are many publications reporting the application of photocatalysis toward water remediation with recent review articles summarizing the photocatalytic removal of organic,inorganic,and microbial pollutants(Salinaro et al.,1999;Ollis et al.,1991;Heller,1995;Ho mann et al.,1995,Mills and Hunte,1997;Blake et a l.,1999; Fujishima et al.,2000).When TiO2powder is suspended in water and irradiated with near ultraviolet(UV)light belowλ<385nm,electron hole pairs are generated within the metal oxide semiconductor and then are separated between the conductance band and valence band.The valence band hole has a very positive reduction potential and is capable of oxidizing water,or hydroxide ions,to form hydroxyl radicals in water(Mills and Hunte,1997). Hydroxyl radicals are known to be powerful for both the oxidation of organic substances and the inactivation of *yj@63bacteria and virus(Rincon and Pulgarin,2004).Mecha-nisms for the bactericidal action of TiO2photocatalysis have been proposed by a number of authors(Matsunaga et al.,1985;Christensen et al.,2003;Maness et al.,1999; Zheng et al.,2000;Sunada et al.,1998).The results from the above studies suggest that the cell membrane is the primary site of reactive photogenerated oxygen species attack.Oxidative attack of the cell membrane leads to lipid peroxidation.The combination of cell membrane damage and further oxidative attack of internal cellular components ultimately results in cell death.TiO2powder is commonly used in the laboratory in the form of a suspension.This method yields a high catalyst surface area to volume ratio for pollutant hydroxyl radical interaction; however,the catalyst must be removed by a posttreat-ment separation stage,which may not be cost e ective on a large scale.There is an e ective way to remove the need for posttreatment separation that the TiO2is loaded on a high surface area support,such as activated carbon,exfoliated graphite,and optical bers(Hammer and Kvande,2007;Lu et al.,1999;Matsunaga and Okochi, 1995).Meanwhile,this method is not associated with a decrease in surface area to volume ratio and mass transfer resulting in a reduction in the pollutant degradation rate. Matos and coworkers prepared carbon-coated TiO2with high photocatalytic activity and repeated-use property andf()y f qCorresponding author.E-mai l:.investigated in uence o di erent activated carbons A C on the photocatal tic degradation o a ueous organic1528LI Y ouji et al.Vol.20pollutants(Matos et al.,1998,1999,2001).But the studies about bacteria inactivation by T iO2/AC composites and the e ects of AC supports on inactivated properties of composites have not been reported.The main purpose of this article was to evaluate and compare photocatalytic inactivation of T iO2/AC composites and TiO2powder. Meanwhile,W e investigatedthat the e ects of A C supports on inactivated properties of composites from photocatalyt-ic kinetics.Finally,the inactivated mechanism of bacteria was explained in photocatalytic course in term of photo-catalytic characteristics.1Experimental1.1P reparat ion of TiO2/A C compositesCommercially available activated carbon grains from Tianjing,China,which were produced by the vapor ac-tivation of coconut shell,were serially treated and then used.Precursor solutions for TiO2/AC were prepared by the following method.T etrabutylorthotitanate and di-ethanoiamine were dissolved in ethanol.The solution was stirred vigorously for2h at20°C,followed by addition of a mixture of distilled water and ethanol.The resulted alkoxide solution was left at20°C for hydrolysis reaction to produce T iO2sol.Then,a desired amount of activated carbon grains was used as the substrates and was added into T iO2sol with a certain degree.After this,sol changes to gel;TiO2gel coated activated carbon was heat treated at250°C for2h in air and then heating temperature was increased gradually to the end temperature from300to 700°C for2h in a ow of high purity nitrogen using an electric oven.The amount of coated T iO2was adjusted by repeating the cycle from dipping to heat treatment.1.2C ulture of bacter ia and growth mediaEscherichia coli(E.coli,NCIMB8277)was grown under aerobic conditions at37°C overnight in50ml of Luria Bertani(LB)medium(pH7.0)containing tryptone 1%,yeast extract0.5%,and sodium chloride1%.Shaking was done to obtain the necessary oxygen transfer into the medium.The cells were centrifuged at8,000r/min for10 min,washed three times in sterilized Milli-Q water,and resuspended in sterilized water.1.3P hotocatalyt ic reactor operat ionSemiconductor composites or powder was suspended in sterilized water by sonication for5min.As shown in Fig.1,inactivated experiments were carried out in a cylindrical pyrex glass vessel on which there was a black light uorescent lamp to provide the irradiance source. Appropriate dilutions of E.coli suspensions were prepared in photocatalytic systems by E.coli being inoculated in sterilized water.A bacterial suspension without catalysts was irradiated as a control,and a dark reaction was also carried out.Circulation of reactant was provided with a magnetic stirrer.Samples were withdrawn at regularxT j6,,Fig.1Experimental apparatus for photocatalytic reaction.bu er(KH2PO4/NaOH).The resulting phosphate bu er solutions were maintained at approximately20mmol/L. Inactivation temperature was maintained at25,37,and 45°C by a temperature controller.1.4Det er minat ion of viable ba cteriaThe number of viable cells in the solution was deter-mined by plating samples after suitable dilutions on LB medium supplemented with20g/L agar and counting the colonies which appeared after24h of incubation at37°C. Many replicate plates were used and all experiments were repeated more than ve times to obtain a mean value applied in kinetics in terms of statistic principle.All the materials were autoclaved for30min to ensure sterility. 1.5Scanning electron m icroscopyBacteria were deposited on TiO2/AC composites or TiO2powder.The samples were subjected to the stan-dard procedure for sample preparation:after being xed with glutaraldehyde and osmium tetroxide,the samples were drained with ethanol/water in increasing concentra-tions of ethanol.The absolute ethanol was replaced by dimethoxymethane,and the samples underwent critical point drying with CO2.The photocatalysts were glued onto stages and metallized with gold.The samples were microscoped and photographed with a scanning electron microscope(JSM-5600LV,JEOL,Japan).2Results and discussion2.1Cha ract er ization of TiO2/ACThe content of TiO2in composite samples per doped cycle,BET surface area,and total pore volume,including the original A C,are summarized in Table1,together with heat-treatment temperature(HTT)and doped cycle times. Nano-TiO2particles have high surface area to increase surface area of hybridization catalyst by doped surface of AC and at the same time,to decrease surface area by blocking the pore entrances on the surface of AC substrate.For1-doped cycle TiO2/AC,because the former e ect on surface area is stronger than the latter e ect,its surface area is larger than the original AC and increased with increasing heat-treatment temperature.However,for T O y y3y,f yintervals and each e periment was repeated at least twice. he pH was ad usted to7or8using a phosphatei2/AC catal st with2-doped c cles or-doped c cles its sur ace area was decreased markedl and was increasedNo.12Inacti vated properties of activated carbon-supported TiO 2nanoparticles for bacteria and kinetic study1529Table 1Characteristic of TiO 2/AC co mposites and original activated carbon (AC)supportsSample HTT (°C)TiO 2content Doped cycle Surface area T otal poreCrystallite Escherichia coli surviv al (wt.%)(times)(m 2/g)volumn (cm 3/g)phase rate after 100min (%)AC–0–4350.08768Amorphou 92TA1-300300314400.08547Anatase 60TA1-400400414480.08469Anatase 57TA1-500500514560.08231A+R 45TA1-600600914620.08075Ru tile 38TA1-7007001014780.07968Ru tile 32TA2-5005001823730.074874A+R 27TA3-5005004732790.06458A+R 23TA4-5005006342710.05364A+R30HTT:heat-treatment temperature;A+R:anatase and rutile.gradually with increasing heat-treatment temperature,but complete recovery of surface area was not attained.The decrease of surface area is reasonably supposed to be the fact that the e ect of nanometer TiO 2particles on enhancingsurface area were fewer than that of its blocking.The total pore volume of original AC is 0.08768cm 3/g.The total pore volume of TiO 2/AC is smaller than that of original AC and decreases with increasing TiO 2content,which could indicate that T iO 2particles had performance of blocking the pore entrances.Therefore,the change tendency of surface area is the same as that of total pore volume with increasing doped cycle times for catalysts at heat-treatment of 500°C as shown in T able 1.Meanwhile,the ratio of anatase to rutile and TiO 2crystallite phase on TiO 2/AC samples at heat-treatment temperature of 500°C were invariable with changes of T iO 2content.2.2P hotocatalyt ic inactivat ion of E.coliThe time course of viable E.coli cells when cell suspensions (107cfu/ml)were irradiated with powder or composites (2g/L)under lamp light after saturation of adsorption in dark was determined in Fig.2.By the control experiments,the percentage of viable cell counts was observed to be >95%in the absence of photocatalysts.In contrast,the number of viable cells decreased gradually for powder or composites in illumination.After 250min illumination,only 60%–70%of E.coli wereinactivatedF T f f y y L f T O y y ×f using T iO 2powder;however,99.99%of E.coli wereinactivated using TiO 2/AC composites.It is obviously found that the TiO 2/A C composites were more e ective for E.coli inactivation in comparison with powder.The AC e ect on inactivated enhancement as observed in photocatalytic course was mainly due to its high surface area,which shows great adsorbing energy to bacteria,as well as organic molecules more than TiO 2powder.In addition,it is experimentally shown that the carbon in active carbon reduces TiO 2to form more Ti 3+ions (Liu et al.,2003).By acting as active center,the T i 3+can trap photogenerated electrons in the conduction band and prevent the recombination of electron-hole pairs;hence,there are more photogenerated holes in composites.The hole in the valence band received an electron from CoA as the donor to form dimeric CoA.Dimerization of CoA inhibited the respiration and caused the death of the cells (Matsunaga et al.,1988).2CoA –SH +2h +vb →CoA –S –S –CoA +2H +(1)Meanwhile,it can be observed from Fig.2that T iO 2content a ects inactivated properties of composites.The relation between rate of E.coli inactivation and T iO 2content follows the sequence:47%>18%>63%>5%.The survival rate of the E.coli inactivated by the pure T iO 2was nearly 77%after 250min.However,the TiO 2/AC that contained 47%T iO 2has reached almost 100%of the removal of E.coli for 175min.2.3Phot ocat alytic inactivation kinet ics of E.coli byTiO 2/A C com posites The inactivated curves of E.coli by TiO 2/A C are well tted by a mono-exponential curve,suggesting that a pseudo-rst order homogeneous reaction model can be tak-en into consideration for describing the kinetic behavior.However,in photocatalytic inactivation reaction system,the reactant in solution absorbs light and then lowers its intensity,which results in the decrease of photocatalytic activity.So the initial concentration of E.coli has a funda-mental e ect on the degradation rate,i.e.,the kinetic rate constant decreases with the concentration (da Silva and Faria,2003).In other words,from a practical standpoint,at the same illumination time,the relative amount of E.f f T x y T O f f ig.2ime co urse o changes i n the surviv al rate o E.coli caused b photocat al sis wi th 2g/o i 2/AC catal st or without catal sts.E.coli content is 1107c u/ml.coli inactivated is less or the more high content o bacteria solutions.he inactivated e periments b i 2/AC o E.coli ollow the pseudo-rst order kinetics with respect to1530LI Y ouji et al.Vol.20 E.coli concentration(C)in the bulk solution:dCdt=k app C=r(2)Integration of that equation will lead to the expectedrelation:ln(C0C)=k app t(3)where,k app is the apparent pseudo-rst order rate constant and is a ected by E.coli concentration,C0is the initial concentration in the bulk solution after dark adsorption, and t is the reaction time,with the same restriction of C =C0at t=0.Generally,the photocatalytic degradation is assumed to occur on the basis of adsorption,so it can be speculated that the inactivation reaction between the surface-adsorbed substrates and the photogenerated oxidants is predominant, although other pathways may exist(Tunesi and Anderson, 1993).We reasonably postulate that photocatalytic inac-tivation of E.coli on the T iO2supported on porous AC follows a modi ed Langmuir-Hinshelwood model,where the oxidationof intermediates competes with that of E.coli intact cells.Then,the reaction rate can be written as:r=dCdt=k2θHO.θEC t(4)where,k2is a second-order surface rate constant,θHO is the fractional site coverage by HO radicals,andθE C is the fraction of sites covered by E.coli cell(EC)at any time t.Owing to the fact that water is the solvent(i.e.,H2O and OH are in large excess)and the oxygen partial pressure remains the same in a given experiment,the fractional site coverage by HO radicals is also constant,and Eq.(3)can be arranged as:r=dCdt=k rθEC t(5)where,k r is rate constant.k r=k2θHO.includes the second-order rate constant.On the other hand,the fractional site coverage by the E.coli cells is given byθEC=K C C1+K C C+PiK i[I i](6)where,K C and K i are adsorption equilibrium constants, and I refers to the various intermediate products of E. coli decomposition.If it is assumed that the adsorption coe cients for all intermediates present in the reacting mixture are e ectively equal,the following assumption can be made as:K C C+XiK i[I i]=K C C0(7)where,C0is the initial concentration of E.coli.Now, substitution of Eq.(6)into Eq.(5)results on the expression:=×K+K=()The relationship between k app and C0can be expressed asa linear equation:1k app=1k r K C+C0k r(9)The values of k app can be obtained directly from theregression analysis of the linear curve in Eq.(2)(a plot ofln(C0/C)versus t)for all the experiments with di erentinitial bulk concentrations of E.coli.In Fig.3,a plot of1/k app versus C0for di erent T iO2contents of TiO2/A C isshown.The values of K C and k r were obtained by linearregression of the points calculated by Eq.(8).Fig.4showsdependence of k r and K C determined in this way on theTiO2content of TiO2/A C.By comparing the dependenceof the k r on the T iO2content with that of K C given in Fig.4,rate constant rst increases with increasing content ofTiO2,but then decreases;however,absorption equilibriumconstant decrease with increasing content of TiO2.It can beobserved that the rate of E.coli inactivation for TiO2/ACcatalysts is mostly determined by TiO2particles.This maybe caused by the fact that E.coli cells have to be adsorbedinto A C layer and then migrated to the surface of T iO2par-Fig.3Relation between1/k app and C0.F R()fq(K)f f f T Oyr k r C C1C C0k app C8ig.4ate constant k r o E.coli inactivated reaction and theadsorption e uilib rium constant C o E.coli as a unction o the i2content in composite catal st.No.12Inacti vated properties of activated carbon-supported TiO 2nanoparticles for bacteria and kinetic study 1531ticles.The rate of T iO 2/AC catalysts inactivation depends on the content of TiO 2,k r being the lower with the smaller TiO 2content.But absorption strength of substrates is an important factor e ecting photoactivity of catalysts.V ery high adsorption equilibrium constant for 5%TiO 2content of catalyst showed a lowered degradation rate presumably due to low TiO 2content and retardation of easy di usion of the adsorbed E.coli by high absorption strength.The highest rate constant (1.43×106cfu/(L min))was ob-served for the sample,which contained 47%TiO 2with adsorption equilibrium constants of 1.17×108L/cfu.Rate constant appears to increase gradually at a region of TiO 2content below 47%,which is reasonably supposed to be due to increasedamount of T iO 2particles because of the occurrence of photocatalytic inactivation on TiO 2particles.After passing a maximum,rate constant decreases with increasing TiO 2content,which may be due to decreasing amount of adsorbed E.coli drastically decreased (low K C )by reduced surface area.It is obvious that a decrease of the amount of adsorbed substrate resulted in the decrease of the inactivation rate.The inactivation of E.coli through hybrid catalysis process by using TiO 2/AC catalysts is mainly determined by TiO 2particles,but adsorption of E.coli cells into AC layer appears to be also important.This may be due to the photon generated by excitation of TiO 2species can easily contact with E.coli and so the process of their recombination could be avoided,giving high yield of photocatalytic activity.In Fig.3,it can be observed that rate constant k app for 5%TiO 2catalysts with high surface area is higher than that for 63%TiO 2catalysts.However,rate constant k r shows inverse result for both.It can be explained by the fact that degradation of E.coli occurs on TiO 2particles.2.4E ects of electr ic power,temperat ur e,and pH on E.coli inactiva tion To investigate the relation between inactivation rate constant and these parameters including electric power and lamp,temperature,and pH values,a series of experiments was conducted using TiO 2/AC with 47%T iO 2as catalysts.Light intensity is a major factor in photocatalytic reactions because electron-hole pairs are produced by light energy (Ku and Jung,2001).The relation between electric power of the uorescent lamp and its light intensity ts direct ratio when the positions of uorescent lamp and reactor are invariable in Fig.1,so the electric power of the uorescent lamp also in uences photodegradation of bacteria during photocatalytic process.T able 2shows that the rate of inactivation increased with increasing electric power of the lamp.For example,the inactivation constant at 400W was faster than that at 300and 200W.This was because higher electric power provides higher ow of photons,which isavailable not only to directly attack bacteria but also to induce generation of oxidative species on the T iO 2surface that subsequently attack bacteria,increasing considerably the bacterial inactivation rate.In addition,the selfdefense and autorepair mechanisms of bacteria are insu cient to protect cells at high electric power.From T able 2,it can be observed that although most of photoreactions are not sensitive to the small variation in the temperature and very few cases have shown an Arrhenius dependence (Herrman et al.,1993,Eqling and Lin,2001),the modi cations in the initial temperature in these ranges a ect the photocatalytic inactivation of E.coli to a signi cant extent.As the temperature was increased from 25to 45°C,the rate constant of E.coli inactivationwas 1.28×106and 1.63×106cfu/(L min),respectively.This implies that the e ect of temperature on E.coli inactivation in photocatalytic TiO 2disinfection is mainly owing to the change in microorganism susceptibility.The relation between temperature and bacteria inactivation is consistent with description by T ang et a l.(2004).The pH is an important factor in in uencing the pho-tocatalytic process.It was clearly observed that pH 7is an advantage for the photocatalytic inactivation of E.coli (Table 2).The weak acid or alkali is not available for E.coli inactivation,it is owing to the fact that the amount of hydroxy absorption and hydroxy produce on TiO 2is in uenced by pH in solution (Chen et al.,2001).So pH value a ects photocatalytic inactivation process of E.coli because high hydroxy content and plentiful E.coli cells that are absorbed on TiO 2/AC are available for the photocatalytic inactivation.2.5Inactivated m echanism of bacteriaT o elucidate the mechanism for photocatalytic inacti-vation of bacteria cells on T iO 2/AC,the morphology of bacteria cells on TiO 2/AC composites was characterized using SEM with di erent illumination times as indicated in Fig.5.Before illumination,the surfaces of the cells ap-peared grainy,smooth,furrowed,crumbled,or dilapidated (Fig.5a).Even after illumination for 1.0h,no obvious morphological changes were recognized,even though the cells had already lost their viability (Fig.5b).However,the outermost layer that was clearly observed in Fig.5a disappeared after 1.0h of illumination.In contrast,the outermost layer of the cells on TiO 2/AC before illumi-nation remained intact.Therefore,the disappearance of the outermost layer results from the composites photo-catalysis.Furthermore,the observation re ects the change in concentration of the cell wall components and also demonstrates that cells on illuminated T iO 2/AC are decom-posed from the outside of the cell.Along with illumination time,bacteria cells lose the smooth and tight surface.AsT able 2E ects of parameters change on reaction co ns tant k rKinetic constantElectric power of lamp a (W)Temperature b (°C)pH c 200300400253745678×6(f (L ))363636333°;W ;W 3°k r 10c u/min 1.4 1.11.871.281.4 1. 1.2 1.4 1.9aAt 7C and pH 7b at 200and pH 7cat 200and 7 C.1532LI Y ouji et al.Vol.20Fig.5SEM ph otographs of bacteria on TiO2/AC in course of ph otocatalytic inactivation before inactivation(a),inactivation for1.0h(b),and inactiv ation for2.0h(c).shown in Fig.5c,the outer layer of the spherical-shape cells disappeared completely and the inner membrane dissolved after2.0h of illumination,indicating the damage of bacteria cells and starting of decomposition of dead cells.3ConclusionsThe use of A C adsorbents as a support for TiO2is e ec-tive in getting high inactivated rates of bacteria in water phase.These merits are summarized as follows:(1)the adsorbent supports make a high concentration environment of bacteria around the loaded TiO2by adsorption,and then the rate of photocatalytic inactivation is improved;(2)the bacteria are inactivated on the photocatalyst surfaces and then further decomposed.High inactivation e ciency of composite is available to prevent the repair of cells.The amount of T iO2in catalysts may play a signi cant role on the photoe ciency of the hybrid catalysts.The E.coli inactivation process well ts a pseudo-rst order kinetic equation.The photocatalytic inactivation processes can be explained in terms of a modi ed Langmuir-Hinshelwood model for the surface reaction between the bacteria and the oxidizingagent.The values of K C and k r were certainly dependent on the TiO2coatings.At47wt.%T iO2coatings with the highest rate constant,K C and k r was 1.17×108L/cfu and1.43×106cfu/(L min),respectively.The electric power of lamp,pH values,and temperature show signi cant e ects on inactivation rate of E.coli.The scanning electron microscopy measurements of bacteria cells on illuminated T iO2/AC showed that the outer layer decomposed rst resulting in inactivation of cell,and with further illumination,the cells nearly decomposed.These results suggest that the inactivated reaction is initiated by a partial decomposition of the outer wall,followed by dissolving of inner member,and then it resulted in cell death.Acknowledgment sThis work was supported by the Educational and Tech-nological Department of Hunan Province(No.08B063), the Natural Science Foundationof Science and T echnology Department of Hunan Government(No.2007GK3060)D F f U y(N SDXKYZZ6)ReferencesBlake D M,Maness P C,Huang Z,Wolfrum E J,Huang J,Jacoby W A,1999.Application of the photocatalytic 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甲烷干重整研究进展

甲烷干重整研究进展

万方数据万方数据万方数据万方数据万方数据万方数据万方数据万方数据万方数据甲烷干重整研究进展作者:赵健, 周伟, 汪吉辉, 马建新, ZHAO Jian, ZHOU Wei, WA NG Ji-hui, MA Jian-xin作者单位:赵健,汪吉辉,ZHAO Jian,WA NG Ji-hui(华东理工大学资源与环境工程学院,上海200237;同济大学新能源汽车工程中心,上海201804), 周伟,马建新,ZHOU Wei,MA Jian-xin(同济大学新能源汽车工程中心,上海201804;同济大学汽车学院,上海201804)刊名:天然气化工英文刊名:Natural Gas Chemical Industry年,卷(期):2011,36(6)1.程金民;黄伟;左志军碳化终温对碳化钼的制备及甲烷二氧化碳重整催化性能的影响[期刊论文]-高等学校化学学报2010(01)2.Hanif A Study on the structure and formation mechanism of molybdenum carbides[外文期刊] 2002(03)3.Nagaoka K;Takanabe K;Aika K I Influence of the reduction temperature on catalytic activity of Co/TiO2 (anatase-type) for high pressure dry reforming of methane[外文期刊] 2003(01)4.Ghorbanzadeh A M;Lotfalipour R;Rezaei S Carbon dioxide reforming of methane at near room temperature in low energy pulsed plasma 20095.Zhang J;H Wang;A K Dalai Development of stable bimetallic catalysts for carbon dioxide reforming of methane [外文期刊] 2007(02)6.史克英;商永臣天然气二氧化碳转化制合成气的研究:Ⅸ.反应机理 1998(01)7.陈文艳环境友好条件下甲烷等离子体重整制氢的研究[学位论文] 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Preparation and characterization of TiO2 photocatalysts supported on various rigid supports

Preparation and characterization of TiO2 photocatalysts supported on various rigid supports
P.O. Box I 115, 41080, Sevilla, Spain b (IRA au CNRS Photocatalyse, Catalyse et Environment, Ecole Centrale de Lyon, B.P. 163, 69131, Ecully Cedex, France ’ DPpartement de Chimie Physique, Universiti Ibnou Zohr, B.P./S 28, Agadir, Morocco Received 2 February 1995; revised 25 May 1995; accepted 25 May 1995
Abstract In the present study Ti02 has been supported on several rigid substrates. Deposition on glass and quartz was carried out by a dip coating procedure and the deposition on stainless steel by an electrophoretic deposition process. The resulting materials have been characterized by XPS, SEM/EDX, XRD and UV-vis absorption spectroscopy. The materials were then tested for the photocatalytic degradation of malic acid. For this reaction, the sample supported on quartz showed the highest catalytic activity. The photocatalytic activity pattern as a function of the nature of the support (fused silica, glass, stainless steel) followed the decreasing order: TiO,/quartz > TiO,/steel = TiOJ glass B photolysis. This decline in activity has been correlated with the presence of cationic impurities (Si“‘ , Na+, Cr3+ , Fe3 + ) in the layer as a consequence of the necessary thermal treatments to improve the cohesion of the titania layer and its adhesion onto the support.

Pigment-颜料精讲

Pigment-颜料精讲
Anatase
Rutile Rutile
Ti+4 O-2
a
c
d
b Tetragonal Cells b
Refractive Index = 2.56 Density = 3.90 a = 0.951 nm b = 0.379 nm c = 0.296 nm d = 0.459 nm
d
Refractive Index = 2.71 Density = 4.17
PIGMENTS 颜料
• Pigment/Color Technology 颜料/颜色 技术 • Effect Pigments 特效颜料 • Colored Pigments 有色颜料
Pigment


Function in Coating 在涂料中的功能 Type of Pigment 颜料种类
Whiteness 白度 Chemical Resistance
耐化学性
It has a neutral pH, a good resistance to alcali solutions 良好的耐碱性
TiO2 分类
Typical Pigment
crystal morphology 晶体形态
Rutile 金红石型
Micronized TiO2

微化TiO2
Introduced into automotive in the 1980’s
与90年代引特点 Particle size---30-50 nm versus 200+ nm
纳米级

Transparent 透明性 Creates a unique effect in metallic colors

具有光增强芬顿活性的有序介孔FeTiO2的制备

Chinese Journal of Catalysis 40 (2019) 631–637催化学报 2019年 第40卷 第5期 | a v a i l ab l e a t w w w.sc i e n c ed i re c t.c o mj o u r n a l h o m e p a g e : w w w.e l s e v i e r.c o m /l o c a t e /c h n j cArticle (Special Issue on Environmental and Energy Catalysis for Sustainable Development)Ordered mesoporous Fe/TiO 2 with light enhanced photo-Fenton activityZhenmin Xu †, Ru Zheng †, Yao Chen, Jian Zhu, Zhenfeng Bian *Key Laboratory of Resource Chemistry, Ministry of Education, Shanghai Key Laboratory of Rare Earth Functional Materials, Shanghai Normal University, Shanghai 200234, ChinaA R T I C L E I N F OA B S T R A C TArticle history:Received 30 December 2018 Accepted 19 January 2019 Published 5 May 2019Ordered mesoporous Fe/TiO 2 was prepared by an evaporation-induced self-assembly method. The iron ions were in situ embedded in the pore wall of the TiO 2 framework. The catalyst has excellent light-assisted Fenton catalytic performance under UV and visible light irradiation. X-ray diffraction and transmission electron microscopy results showed that the TiO 2 samples have an ordered two-dimensional hexagonal pore structure and an anatase phase structure with high crystallinity. The ordered pore structure of the TiO 2 photocatalyst with a large specific surface area is beneficial to mass transfer and light harvesting. Furthermore, iron ions can be controlled by embedding them into the TiO 2 framework to prevent iron ion loss and inactivation. After five cycles, the reaction rate of the ordered mesoporous Fe/TiO 2 remained unchanged, indicating that the material has stable performance and broad application prospects for the purification of environmental pollutants.© 2019, Dalian Institute of Chemical Physics, Chinese Academy of Sciences.Published by Elsevier B.V. All rights reserved.Keywords:Ordered mesoporous TiO 2 Iron doping Photo-Fenton Photocatalysis1. IntroductionThe traditional Fenton reaction is an advanced oxidation technology for wastewater treatment [1,2]. It involves the mix-ture of hydrogen peroxide (H 2O 2) and ferrous iron (Fe 2+) in acidic solution to produce hydroxyl radicals (•OH) for the at-tack of organic pollutants [3,4]. However, the classical Fenton reaction has two obvious shortcomings: low activity under neutral or alkaline conditions and secondary pollution caused by iron sludge. To overcome these shortcomings, various Fen-ton-like reactions have been developed [5–7]. Heterogeneous Fenton-like reactions under neutral conditions have also been studied extensively [3,8–11]. The key of the heterogeneousFenton-like reaction is to develop an efficient heterogeneous Fenton-like catalyst to overcome the challenges of iron leaching and low catalytic activity [12]. Porous materials such as zeolite, clay, metal oxide, mesoporous silica, porous carbon, graphene, graphene oxide, and carbon nanotubes have a large surface area [13–19]. These can be used as a good supporter for iron species and are usually used to increase the surface area and the dispersion of active sites [20].TiO 2 semiconductor materials are promising candidate ma-terials because of their high photocatalytic activity, non-toxicity, good stability, and low cost [21–26]. Recently, Fe 2O 3 modified on the surface of TiO 2 showed enhanced visible light photocatalytic activity [27]. Some efforts have been fo-* Corresponding author. Tel: +86-21-64323520; Fax: +86-21-64322272; E-mail: bianzhenfeng@ † These two authors made equal contributions to this work.This work was supported by the National Natural Science Foundation of China (21876114, 21761142011, 51572174), Shanghai Government (17SG44), International Joint Laboratory on Resource Chemistry (IJLRC), and Ministry of Education of China (PCSIRT_IRT_16R49). Research is also supported by The Program for Professor of Special Appointment (Eastern Scholar) at Shanghai Institutions of Higher Learning and Shuguang Re-search Program of Shanghai Education Committee.DOI: S1872-2067(19)63309-7 | /science/journal/18722067 | Chin. J. Catal., Vol. 40, No. 5, May 2019632Zhenmin Xu et al. / Chinese Journal of Catalysis 40 (2019) 631–637cused on the heterogeneous catalytic oxidation processes of Fe/Fe2O3-loaded TiO2nanoparticles or nanowires [28,29]. Deng et al. [30] prepared a TiO2/Fe2TiO5/Fe2O3tri-ple-heterojunction structure with excellent visible-light re-sponsive Fenton reaction. This work demonstrates that the porous structure of the TiO2is beneficial to the performance and stability of the catalyst.Ordered mesoporous TiO2 has a large specific surface area and a controllable pore structure, which is very beneficial to mass transfer and light harvesting. However, ordered mesopo-rous TiO2 surface loaded with iron ions as a photo-Fenton cat-alyst has not been reported to date. Herein, we report the syn-thesis of highly active mesoporous titania photocatalyst by embedding iron ions in the ordered framework. Titanium pre-cursors, surfactants, and iron ions were self-assembled by a one-step method. By homogenously embedding iron ions into the TiO2framework, the pore structure and specific surface area of TiO2can be controlled, and the photocatalytic activity and light absorption of TiO2 can be improved significantly.2. Experimental2.1. Preparation of ordered mesoporous Fe/TiO2Our synthesis method is based on the preparation reported by Li’s group [31]. In a typical synthesis, transparent sols were prepared by mixing 1.0 g P123 (Sigma-Aldrich), 1.7 g TiCl4 (Aladdin, AR), 3.0 g Ti(OBu)4(Aladdin, AR), and a certain amount of Fe(NO3)3·9H2O with 20.0 mL absolute ethanol (Richjoint Chemical). The mixture was stirred vigorously at least for 30 min and transferred to a Petri dish. The ethanol was evaporated at 25 °C for 24 h with a relative humidity. After aging at 40 °C for 24 h and 100 °C for 24 h, the gels were finally calcined at 350 °C for 4 h in air using a heating rate of 0.5 °C/min with the Fe:Ti molar ratios 0.1%, 0.5%, 1.0%, and 1.5% and the as-synthesized mesoporous materials were denoted as FT-0.1, FT-0.5, FT-1.0, and FT-1.5, respectively. The ratio of Fe:Ti of the FT materials were tested by ICP, and the details are listed in Table S1 (in the Supporting Information) .2.2. Preparation of Fe/TiO2-ImThe ordered mesoporous TiO2was dispersed in Fe(NO3)3 solution, and the suspension was held for 24 h until the sus-pension had dried. The sample was then calcined at 350 °C for 4 h in conditioned air. These samples were denoted as FT-X-Im.2.3. Preparation of Fe/TiO2-SGSolution A was formed by dripping 10 mL Ti(OBu)4 into 35 mL ethanol. Solution B was obtained by adding 4 mL glacial acetic acid, 10 mL distilled water, a certain amount of Fe(NO3)3·9H2O, and 35 mL ethanol. Then, solution A was slowly dripped into solution B and heated for 18 h at 40 °C to obtain the gel. The gel was transferred to an oven at 80 °C and aged for24 h. The as-synthesized samples were calcined at 350 °C for 4h. These samples were denoted as FT-X-SG. 2.4. CharacterizationThe crystal structure was recorded by X-ray diffraction (XRD, Rigaku Dmax-3C, Cu-Kα), and the morphology was ob-served by transmission electron microscopy (TEM, JEOL-2010F, 200 kV). The UV-Vis diffuse reflectance spectra (DRS) were obtained on a UV-Vis spectrophotometer (UV-Vis DRS, Shimadzu UV-2450). The Brunauer-Emmett-Teller (BET) method was used to calculate the specific surface area (S BET), and the Barrett-Joyner-Halenda (BJH) model was used to cal-culate pore volume (V P) and pore diameter (D P). Surface elec-tronic states were determined by X-ray photoelectron spec-troscopy (XPS, PHI 5000 Versaprobe II). The shift of the binding energy due to relative surface charging was corrected using the C 1s level at 284.8 eV as an internal standard. The Fe-loadings were determined on an inductively coupled plasma optical emission spectrometer (ICP-OES, Varian VISTAMPX).2.5. Photo-Fenton activity testThe photocatalyst (100 mg) was added into 50 mL of RhB (10 ppm), and 100 μL of H2O2 was added to the mixture and ultrasonically dispersed for 30 min. The photo-Fenton reaction under UV or visible light irradiation was initiated by a xenon lamp with a filter (λ< 400 nm or >420 nm). After dark ad-sorption for 30 min, the lamp was turned on upon adsorption equilibrium. A volume of 2 mL of reaction solution was taken each time, and the liquid membrane was filtered. The absorb-ance of the solution was measured by a UV spectrophotometer (UV 7502/PC) at the characteristic wavelength, and the reac-tion rate was calculated by (1 − C/C0), where C is the test con-centration and C0 is the initial concentration [32].3. Results and discussionTo determine the structure of the materials, the XRD pat-terns, TEM images, XPS results, and N2 adsorption-desorption isotherms of the samples were analyzed. The wide-angle XRD and low-angle XRD patterns of representative samples are shown in Fig. 1, respectively. As shown in Fig. 1(a), seven high-intensity peaks could be observed at 2θ= 25.2°–76.1°, corresponding to (101), (004), (200), (105), (204), (220), and (215) of anatase (JCPDS No. 21-1272), respectively [33]. No characteristic diffraction peaks of iron compounds were ob-served in the TiO2 samples with different iron ion loadings be-cause of the good dispersion of the iron ions. The XRD diffrac-tion peak did not change with increase of iron ion content, in-dicating that the crystallinity of the samples did not change.The typical small-angle XRD patterns of the mesoporous TiO2 with different iron ion loadings are shown in Fig. 1(b). The small-angle XRD patterns demonstrated that the samples dis-played a representative diffraction peak, suggesting a highly ordered mesoporous structure [34]. With increase of iron ion content, the small angle diffraction intensity decreases and the diffraction peak shifts to a large angle, indicating that the or-dered mesoporous structure of the samples remains and that the pore size of the samples decreases gradually. The resultsZhenmin Xu et al. / Chinese Journal of Catalysis 40 (2019) 631–637 633show that the self-assembly process of TiO 2 is affected by the increase of iron ion content, which results in local collapse of the mesoporous structure. The effect of temperature on FT-1.5 was tested by low-angle XRD (Fig. S1, see the Supporting In-formation). It is important to note that the highly ordered mesoporous structure can be maintained at 350 °C. The peak intensity of the prepared samples decreased gradually with increase of calcination temperature.The structures of the samples were further confirmed by TEM. Fig. 2(a)–(b) shows the TEM images of FT-1.0 and FT-1.5, respectively. Both of these exhibit a 2D hexagonal mesoporous structure with average diameter of 5.0–7.0 nm and average thickness of pore walls of 3.0–4.0 nm. Fig. 2a exhibits well-arranged pores, which confirms the ordered mesoporous structure [31]. The ordered pore structure of FT-1.5 has dam-age at some edges, which is in agreement with the small-angle XRD result. No iron compounds or aggregations were observed inside the pore channels. This result might indicate that iron ions are embedded in pore wall. The EDX analysis (Fig. 2f) re-vealed the presence of Fe, which was homogeneously dispersed in the whole TiO 2 framework.The XPS spectra of different elements in FT-1.5 are shown in Fig. 3. The full-scanned XPS spectrum indicates that the FT-1.5 is composed mainly of the three elements of Ti, O, and Fe (Fig. 3a) [30,31]. The Fe 2p XPS spectra are shown in Fig. 3b. Thepeaks at 711.8 and 725.6 eV are assigned to Fe 3+ 2p 3/2 and Fe 3+ 2p 1/2, respectively. The peaks at 708.9 and 722.7 eV are as-signed to Fe 2+ 2p 3/2 and Fe 2+ 2p 1/2, respectively. This result suggested that the Fe cations in the FT-1.5 have mixed valence (Fe 2+, Fe 3+).Fig. 4(a) shows the N 2 adsorption-desorption isotherms of the mesoporous TiO 2 with different iron ion loadings. At rela-tively high pressure (0.4–0.8), the curves exhibit small hystere-sis loops and type IV isotherms, which are typical of mesopo-rous solids with uniform pore size (Fig. 4(b)). The pore size distribution curves calculated by the BJH method for the mes-oporous composite exhibit narrow peaks centered at about 5nm, which confirms the ordered mesoporous structure [35,36].Fig. 1. (a) Wide-angle XRD patterns and (b) small-angle XRD patterns of TiO 2with different iron ions doping.Fig. 2. HRTEM images of (a) FT-1.0 and (b) FT-1.5; (c–e) The corre-sponding EDX elemental mapping of (b).Fig. 3. (a) Full scanned XPS spectrum and (b) Fe 2p XPS spectra of FT-1.5.634 Zhenmin Xu et al. / Chinese Journal of Catalysis 40 (2019) 631–637This result is consistent with the XRD and TEM results. The catalysts possessed high surface areas (>120 m 2/g,) and large pore volumes (> 0.2 cm 3/g). With increase of iron ion loading, the pore size of the samples becomes larger. The specific BET surface area also decreases, which indicates that some pore structures have been destroyed (Table 1).The UV-Vis diffuse reflectance spectra (DRS) of the samples are shown in Fig. 5. The initial absorption wavelength of TiO 2 is 385 nm, which is consistent with the intrinsic band gap absorp-tion of anatase-type TiO 2. When doped with iron ions, the light harvesting ability of TiO 2 is improved and the adsorption range is extended to the visible light region.The band gap energy of the FT-X can be confirmed by the plot in Fig. 5(b) [37]. The bandgap values of TiO 2 and the FT-0.1, FT-0.5, FT-1.0, and FT-1.5 nanocomposites are 3.20,2.92, 2.90, 2.82, and 2.80 eV, respectively. Therefore, it can be concluded that the light response of FT-X can be changed from ultraviolet to visible light by controlling the content of iron ions. Briefly, the optical properties of FT-X can be tuned by adjusting the molar ratio of iron ion to titanium source.The visible light-Fenton-like catalytic activities of TiO 2 and Fe/TiO 2 samples were evaluated via RhB degradation (Fig. 6). The degradation efficiency of FT-X was higher than that of bare TiO 2 under visible light irradiation. The conversion of RhB con-tinuously increases to nearly 90% after 80 min when the Fe 2O 3 content is 1.5%.To understand the reaction mechanism further, we investi-gated the performance of the light-assisted Fenton catalytic activity under different conditions. As shown in Fig. 7(a), FT-1.5 showed no activity when there is no light and H 2O 2 in the reac-tion. In the absence of H 2O 2, the activity of FT-1.5 for RhB re-moval under visible light is very low, which is attributable to the visible light photocatalytic activity of iron-doped TiO 2. The FT-1.5 sample also showed weak activity in the absence of light, mainly due to the Fenton process. However, under the condi-tions of visible light and H 2O 2, the catalytic reaction rate of the sample increased by nearly 7 times. To evaluate the photocata-lytic activity of FT-1.5 under different conditions further,theFig. 4. (a) N 2 sorption isotherms and (b) pore-size distribution curves of the TiO 2 with different iron ions doping.Table 1BET properties of TiO 2 with different iron ions doping. Sample D p (nm) P v (m 3/g) S BET (m 2/g) FT-0.1 6.1 0.23 191.1 FT-0.5 5.1 0.21 165.2 FT-1.0 5.0 0.16 136.9 FT-1.5 3.70.11113.4Fig. 5. (a) The UV-Vis diffuse reflectance spectra (DRS) of TiO 2 with different iron ions doping; (b) The plot of transformed Kubelka-Munk function versus the energy of light.Zhenmin Xu et al. / Chinese Journal of Catalysis 40 (2019) 631–637 635photo-Fenton catalytic degradation of RhB under UV light irra-diation was also studied (Fig. 7(b)). The degradation rate under the UV light-Fenton process was 9.5 times that under the UV light photocatalytic condition, but about 130 times that the under the Fenton condition.The photo-Fenton ability of FT-1.5 to RhB at different con-centrations was also studied. As shown in Fig. S2, RhB can be completely degraded within 45 min when the concentration is 5 ppm. When the concentration was increased to 10 ppm, 80% of RhB was eliminated. Even at a concentration of 20 ppm, about 50% of RhB was degraded. This indicates that FT-1.5 hasa very good degradation efficiency.The photo-Fenton reaction is significantly influenced by the pH of the solution. Therefore, the effect of pH value was ex-plored further in the range from 3 to 9 (Fig. 8). We found that the FT-1.5 still has excellent activity for the degradation of RhB, even under alkaline conditions. When the pH value is 9.0, more than 80% of RhB can be removed within 80 min. The perfor-mance is slightly lower than that at pH 6.0 and 3.0. This means that FT-1.5 has excellent performance in a wide range of pH value.To investigate the effects of different structures of TiO 2 on photo-Fenton activity, the performances of FT-1.5-SG (prepara-tion by sol-gel) and FT-1.5-Im (preparation by impregnation) were also investigated. As seen in Fig. S3, about 75% and 85% removal efficiencies were achieved within 80 min in the pres-ence of FT-1.5-SG and FT-1.5-Im, respectively. This result demonstrated that the ordered mesoporous structure is more advantageous than the disordered mesoporous structure for photo-Fenton reaction.The stability and reusability of FT-1.5 were evaluated by recycling tests (Fig. 9). As is apparent from the figure, almost no loss of catalytic activity was observed after five consecutive cycles of catalytic reactions. Under visible light irradiation, the performance of each cycle exceeded 90%. Furthermore,theFig. 6. Photo-Fenton activity of the TiO 2 with different iron ions doping.Fig. 7. Photo-Fenton activity of the FT-1.5 in degradation of RhB under(a) visible light and (b) UV irradiation.Fig. 8. Photo-Fenton activity of the FT-1.5 in degradation of RhB underdifferent pH.Fig. 9. Recycling test of photo-Fenton activity of FT-1.5.636 Zhenmin Xu et al. / Chinese Journal of Catalysis 40 (2019) 631–637structure of FT-1.5 was also unchanged after 5 cycles, as shown in the TEM image of Fig. S4. The results show that FT-1.5 has good stability in the process of photo-Fenton reaction.The above experimental results proved that the photocatal-ysis of TiO 2 and Fenton of iron ions are synergistic in the pho-to-Fenton process. A schematic of the detailed mechanism is shown in Fig. 10. Under visible light irradiation, the energy band of TiO 2 is narrowed due to doping of iron ions, which can be irradiated by visible light to generate electrons, thus pro-moting the transformation of Fe 3+ to Fe 2+ in the Fenton process [38]. Under ultraviolet light, this process is more rapid. Thus, the reaction rate is accelerated greatly. 4. ConclusionsIn summary, ordered mesoporous Fe/TiO 2 was prepared by a solvent evaporation self-assembly method. TEM, XRD, and BET measurements showed that the samples doped by iron ions had an ordered pore structure with high crystallinity of anatase and a large specific surface area. There are several reasons for the stable and high photo-Fenton performance of the samples. One is that the photocatalysis accelerates the con-version process between Fe 3+ and Fe 2+ under both UV and visi-ble light irradiation. The other is that porous TiO 2 has a large specific surface area, which is conducive to the exposure of active sites. The third is that the ordered pore structure is con-ducive to the retention of iron ions during the photo-Fenton process. This work provides a new pathway for designing andfabricating high-performance catalysts for environmental puri-fication.AcknowledgmentsThis work was supported by the National Natural Science Foundation of China (21876114, 21761142011, 51572174), Shanghai Government (17SG44), International Joint Laboratory on Resource Chemistry (IJLRC), and Ministry of Education of China (PCSIRT_IRT_16R49). Research is also supported by The Program for Professor of Special Appointment (Eastern Schol-ar) at Shanghai Institutions of Higher Learning and Shuguang Research Program of Shanghai Education Committee. References[1] Z. Xu, C. Huang, L. Wang, X. Pan, L. Qin, X. Guo, G. Zhang, Ind. Eng. Chem. Res., 2015, 54, 4593–4602.[2] M. A. De León, M. Sergio, J. Bussi, G. Ortiz de la Plata, A. E. Cassano, O. M. Alfano, Ind. Eng. Chem. Res., 2015, 54, 1228–1235.[3] A. W. Vermilyea, B. M. Voelker, Environ. Sci. Technol., 2009, 43, 6927–6933.[4] R. F. Hems, J. S. Hsieh, M. A. Slodki, S. Zhou, J. P. D. Abbatt, Environ. Sci. Technol. Lett., 2017, 4, 439–443.[5] X. S. Nguyen, G. Zhang, X. Yang, ACS Appl. Mater. Interfaces , 2017, 9, 8900–8909.[6] D. Yin, L. Zhang, X. Zhao, H. Chen, Q. Zhai, Chin. J. Catal., 2015, 36, 2203–2210.[7] X. Geng, W. Li, F. Xiao, D. Wang, L. Yang, Catal. Sci. Technol., 2017, 7, 658–667.[8] T. Soltani, B. K. Lee, Photochem. Photobiol. Sci., 2017, 16, 86–95. [9] X. Zhao, C. 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C, 2007, 111,18965–18969.具有光增强芬顿活性的有序介孔Fe/TiO2的制备许振民, 郑茹, 陈瑶, 朱建, 卞振锋*上海师范大学, 资源化学教育部重点实验室, 稀土功能材料上海市重点实验室, 上海200234摘要: Fenton反应能够无选择性地降解有机物, 甚至能够处理一些不能被生物降解的污染物, 其原理为过氧化氢(H2O2)和亚铁离子(Fe2+)在酸性溶液中生成具有强氧化性的羟基自由基(•OH), 后者将有机物氧化分解. 因此, Fenton反应在处理环境问题中占有重要地位. 将光催化与Fenton反应结合, 相比单独的Fenton反应可提高氧化矿化性能, 大大加快反应速率, 减少H2O2使用量, 降低成本, 拓宽反应pH范围, 其协同作用主要体现在两方面: (1)光催化产生的电子加速Fe3+转变成Fe2+, 促进Fenton反应进行; (2)Fenton反应中的H2O2与光生电子反应降低了电子-空穴的复合率, 从而提高光催化降解效率. 由于协同作用的存在, 污染物的降解效率大大增加.到目前为止, Fenton反应中催化剂的载体多为惰性多孔材料, 如沸石、粘土、金属氧化物、介孔二氧化硅、多孔碳和sp2型石墨(石墨烯、氧化石墨烯、碳纳米管等)等具有较大比表面积的材料. 通常, 增加载体的表面积有利于活性位点的分散, 但是大比表面积的载体材料会削弱铁催化剂组分之间的相互作用, 导致催化剂稳定性差, 循环利用几次后会增加铁浸出量. 因此, 寻求大比表面积和高稳定性的光催化材料依然是巨大的挑战.本文首次通过蒸发诱导自组装法成功制备了Fe离子修饰的有序介孔TiO2(FT-X), 并通过XRD、BET、TEM、XPS和UV-Vis等分析手段对催化剂的结构进行了表征, 同时以光芬顿降解罗丹明B反应考察了pH、污染物浓度及载体(TiO2)结构对催化性能的影响. 结果表明, 由于Fe离子修饰减小了TiO2的禁带宽度, FT复合材料具有更宽的可见光响应距离和更强的可见光吸收, 在光芬顿反应过程中可以迅速转移电子, 避免电子-空穴对的重组, 同时加速了Fe3+和Fe2+的转化, 显著提高了催化剂的催化性能. 另外, 将Fe离子原位锚定在有序介孔TiO2的孔壁上, 使FT具有规整的孔道结构和高的比表面积. 与不规则多孔材料相比, 一方面, 该结构有利于活性位点的暴露, 另一方面, 有序的孔道更有利于光吸收和溶质传输. 同时, Fe 离子与载体之间具有较强的相互作用, 可以有效地抑制反应过程中Fe离子的流失, FT-1.5样品(Fe:Ti摩尔比为1.5%)在经过5次循环测试后依然保持较高的催化活性.关键词: 有序介孔TiO2; 铁离子掺杂; 光芬顿; 光催化收稿日期: 2018-12-30. 接受日期: 2019-01-19. 出版日期: 2019-05-05.*通讯联系人. 电话: (021)64323520; 传真: (021)64322272; 电子信箱: bianzhenfeng@†共同第一作者.基金来源: 国家自然科学基金(21876114, 21761142011, 51572174); 上海市曙光学者(17SG44); 资源化学国际合作联合实验室(IJLRC); 环境功能材料教育部创新团队 (PCSIRT_IRT_16R49); 上海市东方学者人才计划.本文的电子版全文由Elsevier出版社在ScienceDirect上出版(/science/journal/18722067).。

Self-Clean%20Materials

Application of Titanium Dioxide Photocatalysis to Create Self-Cleaning Building Materials

Roland Benedix1 Frank Dehn2

Jana Quaas, Marko Orgass3

SUMMARY To realize self-cleaning material surfaces there are two principal ways: the de-velopment of super-hydrophobic or super-hydrophilic materials. By transferring the microstructure of selected plant surfaces to practical materials like tiles and facade paints, super-hydrophobic surfaces were obtained (Lotus effect). Super-hydrophilic materials were developed by coating glass, ceramic tiles or plastics with the semiconducting photocatalyst titanium dioxide (TiO2). If TiO2 is illumi-

nated by light, grease, dirt and organic contaminants are decomposed and can easily be swept away by water (rain). Subject of our further research is a detailed study of the interaction between TiO2 and traditional building materials like con-

Pd-TiO2

DOI: 10.1016/S1872-5813(21)60171-8Effects of TiO 2 in Pd-TiO 2/C for glycerol oxidation in a direct alkaline fuel cellViviane Santos Pereira *,Júlio Nandenha ,Andrezza Ramos ,Almir Oliveira Neto(Instituto de Pesquisas Energéticas e Nucleares-IPEN-CNEN/SPCentro de Células a Combustível e Hidrogênio-CECCO ,Cidade Universitária , São Paulo-SP 05508-000, Brasil )Abstract: The Pd-TiO 2 electrocatalysts were synthesized via sodium borohydride reduction and characterized by X-ray diffraction (XRD), transmission electron microscopy (TEM), cyclic voltammetry, chronoamperometry and attenuated total reflectance-Fourier transform infrared (ATR-FTIR). The X-ray diffraction experiments of the Pd-TiO 2 showed peaks associated with Pd face-centered cubic (fcc) structure and peaks characteristics of TiO 2 (anatase phase) with a tetragonal structure. The TEM images showed that the Pd and TiO 2 nanoparticles were well distributed in the carbon support showing some clustered regions with nanoparticle sizes between 7 and 8 nm. Cyclic voltammograms showed an increase in current density values after the glycerol adsorption process. Experiments in alkaline direct glycerol fuel cells at 60 °C showed a higher power density for Pd-TiO 2/C (70∶30) in comparison to the commercial Pd/C electrocatalyst indicating that the use of the TiO 2 co-catalyst with Pd nanoparticles had a beneficial behavior. This effect can be attributed to the electronic effect or to the bifunctional mechanism. Molecules with high-value added glyceraldehyde, hydroxypyruvate and formate were identified as electrochemical reaction products of glycerol on all prepared electrocatalysts.Key words: glycerol oxidation ;Pd-TiO 2 electrocatalysts ;in-situ ATR-FTIR ;cyclic voltammetry ;alkaline fuel cell CLC number: O646 Document code: ADirect alcohol fuel cells (DAFCs) have a high energy density and are easy to handle when compared to PEMFC cells that use hydrogen (H 2) as fuel. In this context, cells (DAFCs) are considered potential alternative energy sources with the possibility of application in portable equipment and electronic devices, in addition to the possible production ofproducts with high added value [1,2].Glycerol fuel applied to an Alkaline Direct Glycerol Fuel Cell (ADGFC) is very attractive because it has a high energy density with a theoretical value close to 6.4 kW·h/L, it is not toxic, and is a non-flammable liquid and of low cost. It presents advantages regarding its application and use in a direct alcohol fuel cell due to the reduction of environmental impacts and the possibility of conversion into high-value added products [3]. The main challenge of this fuel for commercialization in ADFC lies in the kinetics of the glycerol oxidation reaction, that is, the breaking theC−C bonds and completing the oxidation to CO 2[4,5].Pt and Pd nanoparticles are commonly used as primary electrocatalysts in the anode of one ADGFC due to Pt-based electrocatalysts has a chemical stability and high catalytic activity, but it is considered a rare material in the nature and of high cost, in addition to suffering CO poisoning. The decrease in the activities of electrocatalysts during the oxidation reaction is evidenced by the formation of intense adsorbedintermediates on its surface [6]. Electrocatalysts based on Pd nanoparticles in alkaline medium for alcohol oxidation have been shown good results, these electrocatalysts also showed resistance to poisoning by intermediates adsorbed (CO) on the Pd surface.However, their contribution becomes limiting and dependent on factors such as support material,morphology and distribution [7,8].However, the performance of Pd increase alsowhen combined with other metals such as Ru [9], Ni [10],Au [11], Ag [12], In [13] and Co [14]in the form of alloys,deposits or anchors. In this context, new studies with materials for the synthesis of cheaper and more efficient electrocatalysts that help to improve reaction kinetics in a direct glycerol fuel cell have been developed.The combination of Pd with titanium dioxide (TiO 2) was studied in this work to investigate the catalytic activity and the possible production of products with high added value in the oxidation ofReceived :2021-09-16;Revised :2021-10-26*Corresponding author. E-mail: *****************************.br.The project was supported by the CAPES, FAPESP (2017/11937-4) and CNPq (302709/2020-7).本文的英文电子版由 Elsevier 出版社在 ScienceDirect 上出版 (/science/journal/18725813)第 50 卷 第 4 期燃 料 化 学 学 报Vol. 50 No. 42022 年 4 月Journal of Fuel Chemistry and TechnologyApr. 2022glycerol fuel. Titanium dioxide is attractive to be used in the composition of an electrocatalyst because it has resistance to corrosion and tolerance to intermediates formed in the reaction, such as carbon monoxide (CO). TiO2 can be used as a doping material on carbon support or as a co-catalyst[15−18]. Silva et al.[16] synthesized Pd/TiO2-C electrocatalysts for ethanol oxidation in an alkaline medium and showed good results due to the formation of OH species from TiO2, facilitating the oxidation of ethanol fuel, and also observed the change in the d band of Pd in this material due to the strong interaction between metal and support.Han et al.[17] prepared the TiO2-Au/C electrocatalyst for glycerol oxidation in an alkaline medium, and they observed an improvement in the catalytic activity as well as a change in the glycerol reaction pathway due to TiO2-Au interfaces formed during the preparation, attributing the increase of catalytic performance to TiO2 by facilitating oxidation on the Au surface. Souza et al.[18] investigated the combination Pd-TiO2/C (50∶50) for methane activation in an acidic medium, observing the formation of high added value products such as methanol. They attributed the improvement in catalytic activity and stability of the materials to the presence of TiO2. The presence of TiO2 also favors the adsorption of some intermediates for the methane oxidation reaction on the Pd surface, thus increasing the catalytic performance of the prepared electrocatalysts.In this work we present a study that aims to contribute to the understanding of the use of Pd-TiO2/C electrocatalysts with different atomic compositions (50∶50, 70∶30 and 90∶10) supported with Carbon Vulcan XC72® used in the oxidation of glycerol fuel.1 Synthesis, characterization and experiments1.1 Preparation of electrocatalystsPd/C, TiO2/C and Pd-TiO2/C (50∶50, 70∶30 and 90∶10) electrocatalysts were prepared by the sodium borohydride reduction method[18,19]. The metal salt Pd(NO3)2-2H2O (Aldrich) and (TiO2-(Aldrich) were used as metallic precursors, (NaBH4-(Aldrich) as a reducing agent and Carbon Vulcan XC72® (Cabot, Corp. USA) was used as support[18]. Initially, the ions metallic were dissolved in a mixture of water with 2-propanol (50:50 volume ratio), and the Carbon Vulcan XC72® support was added in the solution. The resulting mixture was submitted to an ultrasonic probe sonicator for 10 min for homogenization. After this step, (NaBH4:metal molar ratio equal to 5∶1 was added in one step under magnetic stirring for 1 h at room temperature to reduction of metallic salts. Finally, the resulting mixtures were filtered, and the solids (electrocatalysts) washed with ultrapure water and dried at 70 °C for 2 h.1.2 Electrocatalysts characterization1.2.1 Energy-dispersive X-ray spectroscopy (EDX)The energy-dispersive X-ray spectroscopy analyzes were performed in an equipment containing a scanning electron microscope (SEM), with a 20 keV electron beam, model Philips XL30 equipped with an EDAX microanalyzer, model DX-4 was used for analysis. Samples were prepared with a small amount of powdered electrocatalyst over a sticky paint on the detection support. The data collected correspond to an average of four random points in each sample to obtain the real atomic compositions[20].1.2.2 X-ray diffraction (XRD)X-ray diffraction analyses were performed in a conventional diffractometer, (Rigaku, model Miniflex II) with a Cu Kα radiation source (λ = 0.15406 nm). The diffractograms were obtained in the range scanning angle 2θ from 20° to 90° with a step size of 0.05° and scan time of 2 s per step [18]. To carry out these experiments, a small amount of electrocatalyst powder was compacted in a glass support with the aid of silicone grease, which was introduced into the diffractometer[21].1.2.3 Transmission electron microscopy (TEM)Transmission electron microscopy analyses were performed to estimate morphology and nanoparticles distribution of the electrocatalysts on the carbon support, using JEOL transmission electron microscopy (JEM-2100) operated at 200 kV[20,21]. The samples were prepared from the suspension of the electrocatalyst in isopropyl alcohol, undergoing homogenization in an ultrasound system. Subsequently, an aliquot of the sample was placed on a copper grid of 0.3 cm diameter containing a carbon film. Mean nanoparticle sizes were digitally measured by counting about 150 nanoparticles in different regions of each sample to construct nanoparticle distribution histogram and calculate mean nanoparticle size.1.2.4 Cyclic voltammetry (CV) and chronoamperometry (CA)Cyclic voltammetry and chronoamperometry measurements were performed at room temperature using a potentiostat/galvanostat (Autolab PGSTAT 302N, Metrohm). These studies were carried out using working electrodes (geometric area of 0.0707 cm2)第 4 期Viviane Santos Pereira et al.:Effects of TiO2 in Pd-TiO2/C for glycerol oxidation in a direct alkaline fuel cell 475prepared by the ultra-thin porous coating technique, the reference electrode was an Ag/AgCl (3.0 mol/L KCl) and the counter electrode was a Pt plate. The electrochemical measurements were performed in the presence of 1.0 mol/L KOH or 1.0 mol/L glycerol in 1.0 mol/L of KOH solutions saturated with N2. The cyclic voltammetry experiments were done at a scan rate of 10 mV/s for the potential range from −0.85 to 0.2 V versus Ag/AgCl[22]. The chronoamperometry analyses were carried out keeping the same setup of cyclic voltammetry using 1.0 mol/L glycerol in 1.0 mol/L KOH solution at −0.35 V versus Ag/AgCl for 1800 s[22].1.2.5 Attenuated total reflection-Fourier transform infrared (ATR-FTIR)The ATR-FT-IR measurements were performed on a Nicolet® 6700 FT-IR spectrometer equipped with an MCT detector cooled with liquid N2, ATR accessory (MIRacle with a ZnSe Crystal Plate Pike®) installed is coupled to the spectrometer, to identify the products formed during the electrochemical oxidation of glycerol in alkaline medium in different potentials.1.2.6 Alkaline direct glycerol fuel cell testAlkaline Direct Glycerol Fuel Cell Tests were carried out using Pd/C, TiO2 and Pd-TiO2/C electrocatalysts as anodes and Pt/C electrocatalysts as cathodes in a single fuel cell with an area of 5 cm−2. For Alkaline direct glycerol fuel cell studies it was used the carbon-cloth treated with Teflon and with the presence of Carbon Vulcan XC72® as a gas diffusion layer, and a Nafion® 117 membrane as electrolyte. The electrodes (anode and cathode) were hot pressed on both sides of a Nafion® 117 membrane at 125 °C for 10 min under a pressure of 225 kgf/cm2[23]. The prepared electrodes contain Pd 1 mg/cm2 at the anode and Pt 1 mg/cm2 at the cathode. The temperature was set to 60 °C for the fuel cell and 85 °C for the oxygen humidifier. 2 mol/L glycerol in 2 mol/L KOH aqueous solution was delivered at 1 mL/min, and the oxygen flow was regulated to 150 mL/min[5]. Polarization curves were obtained using a potentiostat/galvanostat (Autolab, model PGSTAT 302 N).2 Results and discussionThe results of the nominal atomic ratios and atomic ratios obtained by EDX for the synthesized Pd-TiO2/C (50∶50, 70∶30 and 90∶10) electrocatalysts are presented in Table 1.For Pd-TiO2/C binary electrocatalysts synthesized with different atomic proportions, the EDX analyses revealed that the atomic ratios (Pd:TiO2) obtained were similar to the nominal atomic ratios (Table 1), therefore, these results indicated that the sodium borohydride reduction method is efficient for the production of the proposed electrocatalysts.Table 1 Nominal atomic ratios and atomic ratios obtained by EDX of the Pd-TiO2/C (50∶50, 70∶30 and 90∶10) electrocatalysts synthesized by the sodium borohydridereduction methodElectrocatalystNominal atomic ratios(%)(Pd:TiO2)Atomic ratios EDX(%)(Pd:TiO2)Pd-TiO2/C50:5045:55Pd-TiO2/C70:3068:33Pd-TiO2/C90:1089:11The X-ray diffractograms of the as-synthesized electrocatalysts are shown in the Figure 1. All diffractograms, showed the presence of a peak centered at about 2θ ≈ 24° associated with the (004) plane of the carbon support. The Pd/C and Pd-TiO2/C electrocatalysts also presented four peaks at about 2θ ≈ 40°, 47°, 68°and 82° associated, respectively, to the (111), (200), (220) and (311) planes of face-centered cubic (fcc) structure of Pd or Pd alloys (JCPDF#89-4897)[20,24−26]. Pd-TiO2/C and TiO2 showed peaks at approximately 2θ≈ 25°, 37°, 38°, 39°, 48°, 54°, 69° and 70°, associated with (101), (103), (004), (112), (200), (105), (116) and (220) crystalline planes of the tetragonal structure (JCPDF#2-387)[20,24], which were characteristics of titanium oxide (TiO2-anatase phase) as already evidenced by Silva et al. and De Souza et al.[16,18].2030405060708090#Pd-TiO2/C (90:10)Pd-TiO2/C (70:30)Pd-TiO2/C (50:50)Pd (311)Pd (220)Pd (200)C (004)2θ /(°)Pd (111)Pd/CTiO2/C########=TiO2 Intensity/(a.u.)Figure 1 X-ray diffractograms of the Pd/C, TiO2/C, Pd-TiO2/C (50∶50, 70∶30 and 90∶10) electrocatalysts synthesized by the sodium borohydride reduction methodThe mean crystallite sizes of the studied electrocatalysts were from 2.0 to 4.3 nm. As seen in Figure 1, the results did not show peak detachment for smaller or larger angles, indicating that there was no476 燃 料 化 学 学 报第 50 卷formation of metallic alloys in the composition of the synthesized electrocatalysts. The micrographs obtainedby transmission electron microscopy analysis and its histograms are shown in Figure 2.0246810121416511162126323742Nanoparticles size /nmPd-TiO 2/C (50:50)d medium =(7.0±2.10) nm24681012481216202428d medium =(7.0±1.5) nm Nanoparticles size /nmPd-TiO 2/C (70:30)56789101151015202530Nanoparticles size /nmPd-TiO 2/C (90:10)d medium =(8.0±1.0) nm24681012145101520253035d medium =(7.2±1.7) nmPd/CF r e q u e n c y /%F r e q u e n c y /%F r e q u e n c y /%F r e q u e n c y /%20 nm 20 nm 20 nm 20 nm(a)2468101214161805101520253035d medium =(8.04±2.24) nmNanoparticles size /nmTiO 2/CNanoparticles size /nmF r e q u e n c y /%20 nm (b)(c)(d)(e)Figure 2 Micrographs and the size distribution of nanoparticles obtained by transmission electron microscopy: (a) Pd/C, (b) TiO 2/C,(c) Pd-TiO 2/C (50∶50), (d) Pd-TiO 2/C (70∶30), (e) Pd-TiO 2/C (90∶10)第 4 期Viviane Santos Pereira et al.:Effects of TiO 2 in Pd-TiO 2/C for glycerol oxidation in a direct alkaline fuel cell477The Pd/C and TiO 2/C electrocatalysts had mean nanoparticle sizes of 7.2 and 8.0 nm and standard deviations of 1.7 and 2.2 nm. The Pd-TiO 2/C (50∶50),Pd-TiO 2/C (70∶30) and Pd-TiO 2/C (90∶10) binary electrocatalysts, presented mean nanoparticle sizes of 7.0, 7.0 and 8.0 nm, respectively, with standard deviations of 2.1, 1.5 and 1.0 nm. All micrographs obtained showed some agglomeration regions of the nanoparticles on the carbon support.All electrocatalysts studied by electrochemical measurements were normalized by milligram of palladium (Pd) considering that the adsorption/desorption process of the studied fuels is directly related to the palladium (Pd) sites at room temperature.The cyclic voltammograms were made in the absence of glycerol (Figure 3). The cyclic voltammograms of Pd/C, Pd-TiO 2/C (50∶50, 70∶30 and 90∶10) exhibited a well-defined hydrogen adsorption/desorption region at (−0.85 to −0.5 V), (Figure 3). In these experiments a shift of the peak position to more negative potentials at about −0.7 V in the adsorption/desorption region (anodic scanning) of hydrogen for Pd-TiO 2/C (50∶50) can also be observed when compared to the Pd/C, Pd-TiO 2/C (70∶30) and Pd-TiO 2/C (90∶10) electrocatalysts,indicating a possible electronic modification of palladium atoms by the neighboring titanium dioxideatoms. Han et al.[15]prepared the TiO 2-Ni composition for glycerol oxidation. Cyclic voltammetry studies showed the presence of hydroxyl formation peaks on the material surface, originating from TiO 2 electron orbitals.−8−6−4−202468E /(V vs Ag/AgCl)j /(m A ·c m −2)Figure 3 Cyclic voltammograms of Pd/C, TiO 2/C, Pd-TiO 2/C(50∶50, 70∶30 and 90∶10) electrocatalysts in a 1 mol/L KOH solution at room temperature at a scan rate of 10 mV/sIn Figure 3, an increase in the current values in the electric double layer at about −0.5 to 0.0 V was observed in the Pd-TiO 2/C (50∶50) and Pd-TiO 2/C (70∶30) binary electrocatalysts in comparison withPd/C, indicating the formation of Pd oxides in the anodic scan, possibly due to a greater amount ofadsorbed oxygen species (OH ads )[23]. Grdén et al.[27]reported that the choice of material composition for the formation of an electrocatalyst can lead to an increase in adsorbed oxygen species on its surface, playing a decisive role in the hydrogen adsorption/desorption process.mA /cm 2mA /cm 2mA /cm 2In Figure 4, the onset of glycerol oxidation was observed at more negative potentials (−0.4 V) for Pd-TiO 2/C (70∶30) with a higher current value with oxidation peak at 14.91 when compared to Pd-TiO 2/C (50∶50) and Pd-TiO 2/C (90∶10) binary electrocatalysts, which had oxidation onset at less negative potentials at −0.36 V with oxidation peaks at 9.37 and 4.88 , respectively. The Pd/C and TiO 2/C electrocatalysts started the glycerol oxidation at about −0.2 V with oxidation peaks at around 1.08 and0.55 respectively (Figure 4). Geraldes et al.[5]investigated the electrochemical oxidation of glycerol in alkaline electrolyte using the PdAu/C, PdSn/C and PdAuSn/C electrocatalysts, and obtained good results,in which its performance wasattributed to thebifunctional mechanism, where Au and Sn provide OH -species favoring the oxidation of intermediates adsorbed on the Pd surface.03691215E /(V vs Ag/AgCl)j /(m A ·c m −2)Figure 4 Cyclic voltammograms of glycerol electro-oxidationon Pd/C, TiO 2, Pd-TiO 2/C (50∶50, 70∶30 and 90∶10)electrocatalysts using 1.0 mol/L glycerol in 1.0 mol/L KOH electrolyte at room temperature with a scan rate of 10 mV/sOttoni et al.[23]studied the Pd/C, Pd/ITO and Pd/C-ITO combinations in the oxidation of glycerol in an alkaline medium and highlighted the Pd/C-ITO material that presented the best electrocatalytic performance in relation to the Pd/C that obtained inferior performance. The authors associated the best results with the bifunctional mechanism and electronic478燃 料 化 学 学 报第 50 卷The current values obtained for Pd-TiO2/C (50∶50) and Pd-TiO2/C (70∶30) electrocatalysts were highest being almost twice higher than those of standard Pd/C and TiO2/C (Figure 5). For the Pd-TiO2/C (70∶30) electrocatalyst there is a slight decay over time compared to Pd-TiO2/C (50∶50). This behavior might be associated with the presence of adsorbed intermediates on the surface of this electrocatalyst in the glycerol oxidation process, as already observed in the literature[14,28]. However, the Pd-Current density /(mA·cm−2)Figure 6 Polarization (A-(I)) curves and power density (A-(II)) in a 5 cm2 alkaline direct glycerol fuel cell (ADGFC) at 60 °C, using Pd/C, TiO2/C and Pd-TiO2/C electrocatalysts with different atomic proportions fed with 2.0 mol/L glycerol in a 2.0 mol/L KOH solution and oxygen flux was set to150 mL min at 85 °CThe Pd-TiO2/C (70∶30) combination obtained the best maximum power density activity and open-circuit voltage value, confirming the performance observed in the cyclic voltammetry and chronoamperometryexperiments (Figure 4 and Figure 5), probably due to the higher formation of oxygenated species for the oxidation of CO ads on the Pd surface[23]. Lower values of maximum power density and open-circuit voltage were observed for Pd/C, TiO2/C when compared to PdTiO2/C (50∶50, 70∶30 and 90∶10), possibly due to resistivities of its electrodes that can hinder glycerol diffusion through the catalytic layer. Han et al.[17] studied the Au-TiO2 combination and reported that the improvement of the catalytic system might be associated with the role of TiO2 in facilitating the glycerol oxidation on the gold surface. This response was also observed in this work.The ART-FTIR spectra of Pd/C, TiO2/C, Pd-TiO2/C (50∶50, 70∶30 and 90∶10) are shown in Figure 7 and the interpretation of the absorption bands for each molecule formed from the partial glycerol electro-oxidation reaction was based on the comparison between standard FT-IR by considering the authors Winiwarter et al.[29] and the works of Gomes et al.[30] and Zalineeva et al.[31].V0.00 Wave number /cm−1Wave number /cm−1Wave number /cm−1Wave number /cm−10.190.290.390.490.590.690.110.210.310.410.510.61V0.00 0.000.140.440.540.74V0.240.640.340.000.120.220.320.62V0.420.52 Wave number /cm−10.000.100.200.300.400.500.60V0.70Figure 7 FT-IR spectra obtained from products collected at different potentials in increments of 100 mV in alkaline direct glycerol fuel cell (ADGFC) experiments using Pd/C, TiO2/C, Pd-TiO2/C (50∶50, 70∶30 and 90∶10) electrocatalystsThe Pd/C electrocatalyst showed efficiency in the glycerol oxidation, and led to the formation of the formate located at 1225 cm−1 present in all potentials and was more intense at 0.69 V. The presence of the hydroxypyruvate band in 1355 cm−1 was observed at all potentials and was more intense at 0.59 and 0.69 V480 燃 料 化 学 学 报第 50 卷respectively[30]. The mesoxalate that would occur from the hidroxypyruvate oxidation was not observed in the samples obtained (in the glycerol oxidation using Pd/C, TiO2/C or the Pd-TiO2/C (50∶50, 70∶30 and 90∶10) binary. Thus, the intermediate molecules of the partial glycerol electro-oxidation reaction were formed and consumed simultaneously.Glycerate was observed at 1377 cm−1 at all potentials, and this was less intense at 0.19 and 0.29 V at Pd/C. The carbonate and carboxylate were located at 1405 and 1575 cm−1 respectively and were more intense from 0.59 to 0.69 V[30,31]. The intensities of the bands corresponding to the glycerol electro-oxidation products of the TiO2/C electrocatalyst are significantly lower than those related to the glycerol electro-oxidation reaction in Pd/C electrocatalysts and those with higher proportions of Pd such as Pd-TiO2/C (with 50%, 70% and 90 % of Pd).In the FT-IR spectra of all electrocatalysts, no peaks close to 2050 cm−1 were observed, this fact can be attributed to the stretching vibration of CO species linearly bound to the surface of the electrocatalyst. However, implying that the reaction in these electrocatalysts does not include the CO formation as an intermediate[32,33]. Confirming that there is no total oxidation in the potential range observed for these electrocatalysts. According to the electrochemical results obtained, the PdTiO2/C (50∶50) and PdTiO2/C (70∶30) electrocatalysts were more promising than Pd/C, TiO2/C and Pd-TiO2 (90∶10). In the PdTiO2/C electrocatalyst (50∶50) the bands of the reaction products formed were more evident from 0.30 V. Moreover, in the PdTiO2/C (70∶30) electrocatalyst the bands that tended to increase together with the value of potential were observed.Table 2 shows the products formed with the different electrocatalysts studied. According to the electrochemical results obtained, the Pd-TiO2 (50∶50) and Pd-TiO2 (70∶30) electrocatalysts were more promising than Pd/C, TiO2/C and Pd-TiO2 (90∶10), with respect to the rate of reaction. However, for the Pd-TiO2 (50∶50) electrocatalyst, the bands of the reaction products formed were more evident from −0.30 V, while for the Pd-TiO2 (70∶30) electrocatalyst, varying intensities along the potentials were observed.Table 2 Molecules formation in the partial electro-oxidation reaction of glycerol at different potentials usingcombined Pd/C and TiO2/C electrocatalystsPd TiO250%70%90% Formate0.0→0.69 (0.59↑)0.21 → 0.510.34 → 0.74(0.52↓)0.0 to 0.70 Hydroxypyruvate0.0→0.69 (0.59↑)0.21 → 0.510.34 → 0.74 (0.34↓)(0.52↓)0.0 to 0.70 Glycerate0.0→0.69 (0.59↑ and 0.69↑)0.21 → 0.510.34 → 0.74 (0.34↓ and 0.44↓)0.0 → 0.62 (0.52↓)0.0 to 0.70 Carbonate0.0→0.69 (0.59↑ and 0.69↑)0.21 → 0.510.34 → 0.74 (0.34↓ and 0.44↓)0.0 → 0.62 (0.52↓)0.0 to 0.70 Carboxylate0.0→0.69 (0.59↑ and 0.69↑)N.O.0.54 → 0.74 (0.74↑)(0.62↑)N.O. Symbol used: → : increase to; ↓: less intense; ↑: more intense; N.O.: not observed3 ConclusionsThe sodium borohydride reduction method was an efficient process to produce Pd/C, TiO2/C and Pd-TiO2/C electrocatalysts for glycerol oxidation because atomic ratios EDX (%) result showed that the amount of Pd and TiO2 in the synthesized electrocatalysts is close to those nominal atomic ratios (%), as expected. All Pd-TiO2/C electrocatalysts were promising for the glycerol oxidation in comparison with Pd/C and TiO2/C. Pd-TiO2/C obtained showed the presence of segregated face-centered cubic (fcc) structure Pd-rich and that also showed peaks associated with the tetragonal structure characteristics of titanium oxide (TiO2-anatase phase). The ATR-FTIR results showed the complexity of glycerol oxidation with the formation of different oxidation products. The electrochemical measurements and the experiments in a single DFAFC showed that Pd-TiO2/C (50∶50), Pd-TiO2/C (70∶30) and Pd-TiO2/C (90∶10) exhibited superior performance for glycerol electrochemical oxidation than Pd/C electrocatalyst. The highest catalytic activity of Pd-TiO2/C (70∶30) electrocatalyst could be attributed to the synergy between the constituents of the electrocatalyst (metallic Pd and TiO2). Further work still need to be done in order to investigate the electrocatalyst surface and to elucidate the mechanism of glycerol electrochemical oxidation using these electrocatalysts, as well as to understand the electronic effect that TiO2 causes in Pd atomic structure.第 4 期Viviane Santos Pereira et al.:Effects of TiO2 in Pd-TiO2/C for glycerol oxidation in a direct alkaline fuel cell 481ReferencesONG C B, KAMARUDIN K S, BASRI S. Direct liquid fuel cells: A review [J ]. Int J Hydrogen Energy ,2017,42(15):10142−10457.[1]ANTOLINI E, GONZALEZ R E. 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Promotional effect of auxiliary metals Bi on Pt, Pd, and Ag on Au, for glycerolelectrolysis [J ]. Int J Hydrogen. Energy ,2020,45(47):25658−25671.[7]NANDENHA J, FONTES H E, PIASENTIN M R, FONSECA C F, NETO O A. Direct oxidation of methane at low temperature using Pt/C, Pd/C,Pt/C-ATO and Pd/C-ATO electrocatalysts prepared by sodium borohydride reduction process [J ]. J Fuel Chem Technol ,2018,46(9):1137−1145.[8]DASH S, MUNICHANDRAIAH N. Nanoflowers of PdRu on PEDOT for electrooxidation of glycerol and its analysis [J ]. Electrochim Acta ,2015,180:339−352.[9]HOUACHE E S M, SHUBAIR A, SANDOVAL G M, SAFARI R, BOTTON A G, JASEN V P, GONZÁLEZ A E, BARANOVA A E. Influenceof Pd and Au on electrochemical valorization of glycerol over Ni-rich surfaces [J ]. J Catal ,2021,396:1−13.[10]VILLA A, DIMITRATOS N THAW-C E C, HAMMOND C, PRATI L, HUTCHING J G. Glycerol oxidation using old-containing catalysts [J ].Acc Chem Res.,2015,48:1403−1412.[11]BENIPAL N, QI J, LIU Q, LI W. Carbon nanotube supported PdAg nanoparticles for electrocatalytic oxidation of glycerol in anion Exchangemembrane fuel cells [J ]. Appl Catal ,2017,210:121−130.[12]NANDENHA J, RAMOS C E D, DA SILVA G S, DE SOUZA R F B, FONTES H E, OTTONI C A, NETO A O. Borohydride reduction methodfor PdIn/C electrocatalysts synthesis towards glycerol electrooxidation under alkaline condition [J ]. Eletroanalysis ,2021,33(4):1115−1120.[13]ROSTAMI H, OMRANI A, ROSTAMI A A. On the role of electrodeposited nanostrutured Pd-Co alloy on Au for the electrocatalytic oxidation ofglycerol in alcaline media [J ]. Int J Hydrogen Energy ,2015,40(30):9444−9451.[14]HAN J, KIM Y, KIM W H, JACKSON K H D, LEE D, CHANG H, CHAE J-H, LEE Y-K, KIM J H. Effect of atomic-layer-deposited TiO 2 oncarbono-supported Ni catalysts for electrocatalytic glycerol oxidation in alkaline media [J ]. Electrochem Commun ,2017,83:46−50.[15]SILVA M C J, BUZZO S G, DE SOUZA B F R, SPINACÉ V E, NETO O A, ASSUMPÇÃO T M H M. 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Structure and chemical composition of a supported Pt-Ru electrocatalysts for methanoloxidation [J ]. J Catal ,1995,154(1):98−106.[21]ANTONIASSI M R, SILVA M C J, NETO O A, SPINACÉ V E. Synthesis of Pt+SnO 2/C electrocatalysts containing Pt nanoparticles withpreferential (100) orientation for direct ethanol fuel cell [J ]. Appl Catal ,2017,218:91−100.[22]OTTONI A C, DE SOUZA R R, DA SILVA S G, SPINACÉ V E, DE SOUZA B F R, NETO O A. Performance of Pd electrocatalyst supported ona physical mixture Indium tin oxide-carbon for glycerol electro-oxidation in alkaline media [J ]. Electroanalysis ,2017,29:960−964.[23]NETO O A, NANDENHA J, DE SOUZA B F R, BUZZO S G, SILVA M C J, SPINACÉ V E, ASSUMPÇÃO T M H M. Anodic oxidation offormic acid on PdAuIr/C-Sb 2O 5. SnO 2 electrocatalysts prepared by borohydride reduction [J ]. J Fuel Chem Technol ,2014,42(7):851−857.[24]GERALDES N A, SILVA F D, SILVA M C J, SOUZA B F R, SPINACÉ V E, NETO O A, LINARDI M, SANTOS C M. 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Towards an atomistic understanding of electrocatalytic partial hydrocarbon oxidation:propene on palladium [J ]. Energy Environ Sci ,2019,12(3):1055−1067.[29] 482燃 料 化 学 学 报第 50 卷。

电化学阻抗谱简介 (EIS)

曹楚南、张鉴清著,《电化学阻抗谱导论》,2002年
如何测量得到EIS?
• 装置简图
Lock-in amplifier (EG&G, M5210).
• 相应的操作软件
Potentiostat (EG&G, M273)
EIS测量结果的表达形式
• Y = G()X G()为阻抗或者导纳,总称阻纳。它是一个随频率变化的矢 量,用变量为f或其角频率为的复变函数表示,可记为: G() = G’() +jG’’() 若G为阻抗,则有Z() = Z’() +jZ’’() 相位角=arctg(-Z’’/Z’)
电极系统
角频率为
正弦波信号Y
Y = G()X
电位或者电流
G()为阻抗或者导纳
在一系列下测得的一组这种频响函数值就是电极系统的EIS,即G()~
曹楚南、张鉴清著,《电化学阻抗谱导论》,2002年
EIS测量有哪些特点?
• 以小幅值的正弦波对称的围绕稳定电位极化,不会引起 严重的瞬间浓度变化及表面变化。
弥散效应:固体电极的电双层电容的频响特性与“纯电容

并不一致,而有或大或小的偏离的现象。
ZQ
1 Y0
(
j ) n
0< n <1
曹楚南、张鉴清著,《电化学阻抗谱导论》,2002年
在染料敏化电池 (DSC)中的应用
• 用于电导测定 • 过程研究 • 电池稳定性测试 • 电场分布及表面态能量分布 • ……
• Type transformation in CuInSe2 and CuInS2 solar cells is an important issue with far reaching consequences.
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Carbon coating of anatase-type TiO 2and photoactivityTomoki Tsumura,*a Naoko Kojitani,a Ikuichiro Izumi,b Norio Iwashita,c Masahiro Toyoda d and Michio Inagaki eaGroup 2,NARD Institute Co.Ltd.,2-6-1Nishinagasu,Amagasaki 660-0805,Japan.E-mail:tsumura@nard.co.jp;Fax:181-6-6482-8502;Tel:181-6-6482-7012bNara National College of Technology,Yata,Yamatokoriyama 639-1080,Japan cNational Institute of Advanced Industrical Science &Technology (AIST),Kansai Center,Midorigaoka,Ikeda,563-8577,Japan dFukui National College of Technology,Geshi,Sabae,916-8507,Japan eAichi Institute of Technology,Yakusa,Toyota,470-0392,Japan Received 22nd February 2002,Accepted 4th March 2002First published as an Advance Article on the web 3rd April 2002Carbon coating of photocatalytic anatase-type TiO 2powders was successfully carried out by heating apowder mixture of poly(vinyl alcohol)and TiO 2under N 2gas flow at temperatures above 700u C.All particles of TiO 2were covered by a carbon layer and looked black.For methylene blue (MB)in aqueous solution,carbon-coated anatase powders thus prepared showed marked adsorption and decomposition under UV irradiation and were confirmed to keep almost the same photoactivity as that without any carbon coating.Carbon coating of anatase-type TiO 2was found to give different merits for photoactive performance;suppression of phase transformation from anatase to rutile at high temperatures,quick adsorption of MB into the carbon layer,decomposition of adsorbed MB by TiO 2and prevention of the interaction of TiO 2with binder resin.Repeated cycles of adsorption and decomposition of methylene blue in aqueous solution were experimentally confirmed.1.IntroductionEnvironmental pollution by NO x in air and various organic compounds in water has caused various serious problems for human health.The decomposition of these pollutants using TiO 2photocatalysts has been one of the most promising methods for dealing with the problem,1–9and now these photocatalysts have started to be utilized as filters,built into purification systems for air and water,and also as paints and coatings for walls,building blocks,tiles,window glasses,tents,etc .10–14For some practical applications,the particles of photo-catalyst TiO 2were either mounted on adsorbents,such as activated carbons and zeolites,or fixed on a substrate by using a binder.In the former case,the pollutant molecules could be adsorbed onto adsorbents,but they were not readily decomposed by the TiO 2photocatalyst mainly because of the slow diffusion speed of the pollutants on the adsorbent sur-face to the TiO 2particles.Consequently,the adsorbent was saturated with pollutants during long-term use and so only photocatalytic decomposition of the pollutants by the TiO 2particles themselves was observed.In the latter case,organic polymer binders were not suitable,because the binder was decomposed by the photocatalytic reaction on the TiO 2particles,as well as the pollutants.Therefore either ceramics or fluorinated resins had to be used as binders,which led to increased costs.In the present work,TiO 2particles were coated with a carbon layer in order to give adsorption ability to the catalyst particles,to transfer the adsorbates to the surface of the TiO 2and also to prevent direct contact of the TiO 2with the binder polymer.The carbon-coated anatase-type TiO 2,in practice,could keep almost the same photocatalytic activity as that without the carbon coating,in addition to the adsorption ability of the carbon layers,and could prevent the decomposi-tion of the polymer binder. 2.Experimental2.1Sample preparationCarbon coating of the TiO 2powders was achieved by following the same procedure as that reported in a previous paper;15powder mixtures of TiO 2with a carbon precursor polymer in different ratios were heated in a flow of nitrogen at different temperatures of 700to 1100u C for 1h.In the present work,a commercially available TiO 2powder with an anatase-type structure (ST-01,Ishihara-Sangyo Co.Ltd)was selected as the starting material,of which the average size of primary particles was determined to be 7nm by means of X-ray diffraction (XRD),and that of aggregated secondary particles was about 60nm by SEM.As a carbon precursor polymer,poly(vinyl alcohol)(PVA,Nippon Synthetic Chem.Ind.Co.Ltd)with an average degree of polymerization of 2000and particle size under 850m m was used.The TiO 2–PVA mixtures with 5,10,30and 50mass%PVA were prepared.The heating rate to the programmed temperature was 10u C min 21and flow rate of nitrogen was 100mL min 21.After heat treatment the powders were cooled down to room temperature in a flow of nitrogen.The preparation conditions,mixing ratio of PVA and heating temperature and time,are listed in Table 1,together with the sample code used in the present paper.For each sample the X-ray diffraction (XRD)pattern was measured with Ni-filtered CuK a radiation and a scanning speed of 2u min 21,and carbon content was determined from the weight loss of the sample heated at 500u C for 1h in air.For some samples,the BET surface area was measured by nitrogen adsorption at 77K.2.2Adsorption and photocatalytic decomposition of methylene blueMethylene blue (MB,C 16H 18N 3S,reagent grade)was dis-solved in purified water to a concentration of 2.9461025andDOI:10.1039/b201942fJ.Mater.Chem.,2002,12,1391–13961391This journal is #The Royal Society of Chemistry 2002P u b l i s h e d o n 03 A p r i l 2002. D o w n l o a d e d b y S h a n g h a i I n s t i t u t e o f T e c h n o l o g y o n 22/04/2014 02:25:42.View Article Online / Journal Homepage / Table of Contents for this issue1.4761024mol L 21.Powder samples of 0.021g were dis-persed into 40mL of2.9461025mol L 21MB solution thus pre-pared in a glass bottle with a screw cap.The bottle was stirred either in the dark or under UV rays of about 1mW cm 22from a black light (10W)in a box.The blue color of the solution faded gradually with time due to the adsorption and decomposition of MB.The speed of color fading was followed by sampling 3mL aliquots of the solution at appropriate intervals and measuring the optical absorbance at a wavelength of 650nm,which was attributed to MB.From the experiments in the dark,the adsorption of MB into the samples could be followed.In the experiments under UV irradiation,the color fading was due to both adsorption and decomposition of MB by the sample powders.In the present work,therefore,sample powders saturated with MB were prepared and transferred into 40mL of MB solution with 2.9461025mol L 21with stirring under UV irradiation.The saturated samples were prepared by dispersing in a ten-times concentrated MB solution (2.9461024mol L 21)with stirring in the dark.After no change in optical absorbance of the solution was detected,though MB still remained in the solution,the samples were isolated by centrifuging,and then washed with water.There was little extraction of MB from the samples thus treated during washing with water and so these samples were considered to be saturated or nearly saturated by MB.The decomposition of MB using these saturated samples was followed by measuring the optical absorbance of the solution as a function of UV irradiation time.The value of pH of the MB solution was kept around 6–7during the photocatalytic reaction with different samples.In order to measure the cyclic performance of adsorption and photocatalytic decomposition of MB,sample powders prepared from the mixture with 50mass%PVA at 900u C (SP50-900)were mounted on a slide glass using a styrene–butadiene base latex binder;the slurry of SP50-900powders with a latex emulsion (Nipol LX430,Nippon Zeon Co.,Ltd)in a mass ratio of 80:20was spread on a slide glass and then dried at 150u C for 10min.Two slide glasses holding 0.034and 0.015g of SP50-900were prepared.The former was immersed in 40mL of 2.9461025mol L 21MB solution and the latter in 40mL of 1.4761024mol L 21MB solution with stirring under UV irradiation.When the optical absorbance at 650nm of the solution became almost zero,the slide glass was taken out from the solution and again immersed in new MB solution with the same concentration under UV irradiation with checking the change in optical absorbance with time.2.3Interaction with acrylic resinThe interaction between photocatalytic TiO 2particles and binder was studied by using a combination of the sample powders prepared from the mixture with 50mass%PVA at 700u C (SP50-700)and an acrylic resin (A-166,Dainihon-Ink Chem.Ind.Co.Ltd).The acrylic resin was diluted with propan-2-ol to a concentration of 20mass%.Into the solution the sample powders SP50-700were mixed in a mass ratio of acrylic resin to carbon-coated TiO 2of 80:20by using a mixer with 15000rpm for 15min.The mixed solution was spread on a slide glass and dried at 120u C for 5min.The film thus obtained was exposed to UV rays with about 1mW cm 22from a black light (10W)in a box.Weight loss with UV irradiation time was measured at appropriate intervals.Two acrylic resin films containing no photocatalysts and those without carbon coating (i.e.,ST-01)were also examined.3.Results and discussion3.1Structure and morphology of carbon-coated TiO 2The samples obtained after heating with PVA above 700u C looked black,though the original ST-01remained white after heating.Therefore,the particles of TiO 2were covered with carbon which was produced by the carbonization of PVA.The carbon coating of solid particles has been reported on various ceramics,including graphite,and metals.15–20SEM micro-graphs of samples,ST-01,ST-01-700,SP95-700and SP50-700,are shown in Fig.1.In the original ST-01,aggregated secondary particles with a size of around 60nm are observed (Fig.1a),though the size of primary particles is supposed to be one tenth that of secondary particles.After 700u C heating,i.e.,in ST-01-700,most of the particles are sintered with each other,becoming larger than 1000nm,though a small amount of small particles still remain (Fig.1b).For SP95-700and SP50-700,however,the particle size observed under SEM is kept almost the same as the original ST-01,around 60nm,even though they have been heated at 700u C,as shown in Fig.1c and 1d,respectively.In Table 1,the carbon content (the carbon residue after the carbonization of PVA)in each sample is listed.It decreases with decreasing mixing ratio of PVA and therefore,it may be controlled by changing the PVA mixing ratio.The carbon content in the sample also decreases with increasing heating temperature;16mass%after heating at 700u C and 9mass%at 1100u C for a PVA mixing ratio of 50mass%.The values of BET surface area of some samples are shown in Table 1.The original ST-01has a rather high surface area of about 300m 2g 21,but after heating up to 700u C the surface area becomes one tenth of the original value,30m 2g 21,because of sintering of the particles.The surface area of carbon-coated TiO 2samples also decreased to below 130m 2g 21after heating at 700u C,because of slight sintering and crystal growth of the TiO 2particles.If the surface area of TiO 2particles coated by carbon after 700u C heating is the same as those heated without the carbon layer (ST-01-700),the surface area for carbon layers is rather high,about 500–600m 2g 21.However,it was not possible to measure the surface area for carbon and TiO 2separately.In Fig.2a,XRD patterns of the samples heated with 50mass%PVA at different temperatures (the samples SP50-700to SP50-1100)are shown.The anatase-type structure is kept even after heating at 1100u C,though small amounts ofTable 1The samples prepared in the present work Sample code Catalyst/carbon precursor Heating temperature and time Mixing ratio of PVA (mass%)Carbon content (mass%)BET surface area/m 2g 21ST-01——00300ST-01-700—700u C,1h 0030SP50-700ST-01/PVA 700u C,1h 5016130SP70-700ST-01/PVA 700u C,1h 309120SP90-700ST-01/PVA 700u C,1h 10560SP95-700ST-01/PVA 700u C,1h 5240SP50-800ST-01/PVA 800u C,1h 5014SP50-900ST-01/PVA 900u C,1h 5010170SP50-1000ST-01/PVA 1000u C,1h 5012SP50-1100ST-01/PVA1100u C,1h5091392J.Mater.Chem.,2002,12,1391–1396P u b l i s h e d o n 03 A p r i l 2002. D o w n l o a d e d b y S h a n g h a i I n s t i t u t e o f T e c h n o l o g y o n 22/04/2014 02:25:42.the unknown phase marked by filled circles in the figure and also a rutile-type structure marked by open circles appear above 900u C.As shown in Fig.2b,on the other hand,the original ST-01without carbon coating has an anatase-type structure,but it is partly transformed to a rutile-type structure even at 700u C.In the present work,the identification of the unknown phase appearing in Fig.2a could not be performed mainly because of its formation in only small amounts.However,it was proved to be a Ti 4O 7phase,which is reasonably supposed to be formed by the reduction of TiO 2by coated carbon,by using fine par-ticles synthesized through the hydrolysis of titanium alkoxides and has almost the same photocatalytic activity as anatase.21The crystallinity of the sample ST-01is improved by heating to 700u C,as indicated by sharpening of all the diffraction lines,typically by a separation of 103,004and 112diffraction peaks at around 38u in 2h .The improvement in crystallinity is not so pronounced in the carbon-coated samples SP50-700and SP50-800;broad diffraction lines are seen,with no separation among the three diffraction peaks mentioned above.This XRD measurement agreed with the SEM observation and surface area measurement,which showed sintering of the TiO 2par-ticles on heating.Above 900u C,the diffraction lines for the anatase-type structure are sharpened and the separation of these three diffraction peaks becomes clear,but at the same time a rutile phase appears (Fig.2a).The PVA mixing ratio has an influence on structural change in anatase,as shown in Fig.2c.With decreasing PVA mixing ratio,i.e.,with consequent decreasing carbon content in the resultant samples,the crystallinity of the anatase-type struc-ture is improved.In the samples with 10and 5mass%PVA (SP90-700and SP95-700),a rutile-type structure is formed,butFig.1SEM micrographs of the samples ST-01(a),ST01-700(b),SP95-700(c)and SP50-700(d).Fig.2XRD patterns of the samples heated to different temperatures.a)The samples heated at different temperatures,$:unknown phase,#:rutile phase,b)the original ST-01and ST-01-700(ST-01heated at 700u C),c)the samples produced from different mixing ratios of TiO 2and PVA.J.Mater.Chem.,2002,12,1391–13961393P u b l i s h e d o n 03 A p r i l 2002. D o w n l o a d e d b y S h a n g h a i I n s t i t u t e o f T e c h n o l o g y o n 22/04/2014 02:25:42.other samples with 30and 50mass%PVA are a single anatase phase.In the XRD patterns for all carbon-coated samples (Fig.2a and c),the diffraction peaks of carbon were not observed because of the low carbon content and also low crystallinity as so-called amorphous carbon.For ST-01,the particles observed under SEM are supposed to be aggregates of small crystals whose size may be com-parable with the average crystallite size of 7nm determined by XRD.The particles of the original sample ST-01were sintered during heating and became much larger,as seen in ST-01-700(Fig.1b).During heating the growth of crystals occurred at the same time,which was shown by the sharpening of the diffraction lines (Fig.2).In the carbon-coated samples,how-ever,not only sintering of the aggregated particles but also crystal growth in each particle were depressed,the apparent size of carbon-coated samples being not so much different from the original ST-01and all diffraction lines being broadened as the original showed.The reduction in sintering and crystal growth may be responsible for the suppression of the phase transformation from anatase to rutile at high temperatures.The same effect of suppression of the transformation to rutile was observed on the anatase powders which were coated by carbon from a different precursor.22However,the detailed mechanism for the suppression of phase transformation from anatase to rutile by carbon coating requires more experimental results to be understood.3.2Adsorption and photocatalytic activities of carbon-coated anataseIn Fig.3a,color fading of the MB solution in the dark,which is due to the adsorption of MB into the sample particles,wasshown on the samples with different carbon contents heated at 700u C (ST-01-700and SP50-700to SP95-700),together with the original ST-01.The original ST-01and ST-01-700adsorb MB very slowly,and about 39%of MB is absorbed after plete color fading of MB of the solution with these samples took more than 120h.However,carbon-coated samples show marked adsorption of MB.Samples SP50-700and SP70-700,which have high carbon contents,adsorb all the MB in the solution within 10min.The color fading curves for samples SP90-700and SP95-700with low carbon contents seems to occur in two steps,very quick fading in the beginning and then a slow one;in the first step color fades down to about 3and 26%,respectively,and then the complete adsorption of the rest of the MB in the solution takes about 15and 25h,respectively.These results clearly show two types of adsorption of MB into carbon-coated TiO 2particles;rapid and slow adsorption.The former is the adsorption of MB into the micropores of the coated carbon layer which is supposed to have a high surface area (Table 1),similar to that of activated carbons.The latter is observed on the particles of ST-01and ST-01-700;ST-01and ST-01-700adsorbed slowly onto their aggregated particles,which looked blue at the end of adsorption.From the present results in Fig.3a,the speed of color fading can be concluded to be much faster for the former than for the latter.It was experimentally shown that the high crystallinity of the anatase phase on photocatalytic decomposition of MB and ipconazole (a kind of fungicide)is an important factor for a high decomposition speed,23–25even though the surface area decreases markedly.Partial transformation to rutile was shown to reduce the photocatalytic activity of TiO 2catalysts through the determination of the optical band gap.25The improvement in the crystallinity of anatase was reported to be advantageous for MB decomposition,and the decrease in specific surface area due to the grain growth and also phase transformation to rutile by heating were also reported to be unfavorable for MB decomposition.23In the sample ST-01-700,these three factors,improvement in crystallinity,decrease in surface area and phase transformation to rutile,occurred at the same time.This might be the reason why ST-01and ST-01-700showed similar behavior for MB decomposition,as shown in Fig.3a.Color fading of the MB solution under UV irradiation in the presence of the present samples is shown in Fig.3b.Color fading curves for SP50-700and SP70-700are not differentiated from those in the dark,indicating that apparent color fading is governed by the adsorption of MB into these particles.On SP95-700,however,fading is accelerated by UV irradiation;in the dark MB color fades to about 26%after 10min and then to 2%after 25h (Fig.3a),but under UV irradiation it becomes zero after only 1hour.A similar but a little less accelerated effect is observed for SP90-700.For ST-01and ST-01-700,on the other hand,color fading is much faster than that without UV irradiation,but it is still slower than that observed on carbon-coated samples.It has to be mentioned that the particles of ST-01and ST-01-700are never colored during UV irradiation.These results indicate that photocatalytic decomposition of MB certainly occurs on TiO 2particles,even on those coated by carbon,and that MB adsorption and decomposition were performed on carbon-coated particles,the former looking faster than the latter.In Fig 3c,the fading behavior of the MB-saturated samples under UV irradiation are shown.For the original ST-01,fading speed is rather slow in the beginning,probably because the decomposition of adsorbed MB is the main photocatalytic reaction,and then fading occurs rapidly due to the decom-position of MB in the solution,but it needs about 5h for the complete decomposition.For MB-saturated ST-01-700,fading speed is also slower in comparison with that for non MB-saturated ST-01-700.The results for ST-01andST-01-700Fig.3Color fading of the MB solution in the presence of photo-catalysts with time.a)In the dark.b)Under UV irradiation.c)Under UV irradiation with MB-saturated photocatalysts.#:ST-01,$:ST-01-700,':SP50-700,(:SP70-700,%:SP90-700,and e :SP95-7001394J.Mater.Chem.,2002,12,1391–1396P u b l i s h e d o n 03 A p r i l 2002. D o w n l o a d e d b y S h a n g h a i I n s t i t u t e o f T e c h n o l o g y o n 22/04/2014 02:25:42.reveal that adsorbed MB is reasonably supposed to be decomposed before MB in the solution.On carbon-coated samples,the same sequence of photocatalytic decomposition of MB could be assumed;SP95-700and SP90-700which have small carbon contents and small adsorption capacities show rapid fading of the MB solution,faster than the original ST-01, but SP70-700and SP50-700fade the color much more slowly than ST-01.The low apparent photoactivity for SP70-700and SP50-700with high carbon contents seems to be caused by two factors.First,in SP50-700and SP70-700,a relatively large amount of MB is adsorbed into the carbon layers very quickly, but it is supposed to take time for the adsorbed MB in the carbon layers to diffuse to the surface of the TiO2particles. Secondly,UV irradiation is supposed to become weaker during passing through the coated carbon layer.In Fig.4,color-fading behaviors of the carbon-coated samples with different heating temperature are compared with the original ST-01.With increasing heating temperature up to900u C,the fading speed becomes faster,probably because of the improvement of crystallinity of the anatase-type structure,and above900u C the color fading speed decreases, which is supposed to be mainly because of the partial trans-formation of anatase to rutile in the TiO2aggregates.For SP50-1000and SP50-1100,with increasing rutile(Fig.2a),the color fading speed tends to be reduced.In the present work,color fading was principally followed by a decrease in absorbance at650nm wavelength.It is worth mentioning that the same absorbance decrease was observed at wavelengths around250–300nm.The present experimental results clearly show that colorfading of the MB solution is due to the adsorption and decomposition of MB,and the MB adsorbed in the carbon layer is decomposed by UV irradiation of the TiO2particles. The suppression of the phase transformation from anatase to rutile by carbon gives certain advantages for the present carbon-coated catalysts.3.3Cycle of adsorption and photocatalytic decomposition of MB To confirm that a cycle of adsorption and photocatalytic decomposition is possible on the present carbon-coated anatase-type TiO2,the sample SP50-900was selected,because it has the highest speed of apparent photocatalytic decom-position among the present samples.The color fading with cycling is shown in Figs.5a and b.The result in Fig.5a,where the concentration of MB is2.94 61025mol L21,proves clearly that cyclic usage of carbon-coated anatase-type TiO2is possible and no detectable reduction in photocatalytic activity is observed.Even in higher concentration MB solution(1.4761024mol L21)in Fig.5b,the same cycling performance is confirmed.The fading rate appears to decrease with cycling in Fig.5a,which seems to be due to adsorbed MB and its decomposition products remaining in the carbon layers and also at the side in contact with the slide glass,where the UV rays could not reach.This is reasonably supposed to be related to the experimental procedure in Fig.5a,transferring the catalysts before reaching complete fading.In Fig.5b,therefore,UV irradiation was continued even after complete fading.A long irradiation time even after the solution faded to zero absorbance(period shown by arrows in Fig.5b)seems to give faster fading speeds at the beginning of the following cycle,suggesting that the complete decomposition of MB adsorbed into the carbon layers is performed during this irradiation period.3.4Interaction with acrylic resinIn Fig.6,weight loss under UV irradiation with time is compared among three acrylic resinfilms,thefilm without any photocatalysts,that containing the original ST-01and that containing carbon-coated sample SP50-700.Thefilm contain-ing ST-01decreases its weight quite rapidly and reaches39% loss after870h,which is mainly due to the photocatalytic decomposition of the resin by TiO2,as pointed out by many authors.However,thefilm containing SP50-700shows only 5%loss even after870h irradiation,which is almost the same as the acrylic resinfilm without any photocatalyst,whichis Fig.4Color fading of the MB solution under UV irradiation in thepresence of MB-saturated photocatalysts heated to different tempera-tures.0:SP50-700,y:SP50-800,<:SP50-900,.:SP50-1000,and(:SP50-1100,#:ST-01Fig.5Color fading of the MB solution under UV irradiation in thepresence of the sample SP50-900with cycling to use fresh MB solution.Arrows represent the transfer of the SP50-900sample into fresh MBsolution.a)2.9461025mol L21MB solution,b)1.4761024mol L21MBsolution.Fig.6Weight loss of photocatalysts dispersed in acrylic resin underUV irradiation.#:acrylic resin with ST-01':acrylic resin with SP50-700,%:acrylic resin without photocatalysts.J.Mater.Chem.,2002,12,1391–13961395 Publishedon3April22.DownloadedbyShanghaiInstituteofTechnologyon22/4/2142:25:42.reasonably supposed to be due to the evaporation of the organic solvent remaining from film casting.The present result reveals that carbon coating on TiO 2particles works effectively to prevent the interaction with binder resins.4.ConclusionPhotocatalyst anatase-type TiO 2particles were coated with a carbon layer by mixing TiO 2particles with PVA and then heating above 700u C under N 2gas flow.The presence of carbon layers on coated TiO 2particles was found to give various advantages to the photocatalytic TiO 2particles;suppression of the phase transformation of anatase to rutile structure by preventing the sintering and crystal growth in TiO 2particles,quick adsorption of MB to transfer it to the surface of TiO 2where it undergoes decomposition under UV irradiation,and also prevention of the interaction between TiO 2and binder polymer which decomposes the polymer under UV irradiation.The cycle of adsorption 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