硫修饰的多孔Co3O4活化过一硫酸盐降解亚甲基蓝

以Na₂S₂O₃为硫源，采用改进的草酸盐-热解法制备了一系列硫修饰的Co₃O₄多孔催化剂[S_x@Co₃O₄,x=0.25、0.50、0.75、1,x为硫的修饰量，以Co(NO₃)₂·6H₂O的物质的量为基准，下同]。以亚甲基蓝(MB)为降解模型，考察了不同催化剂活化过一硫酸盐(PMS)的性能。探讨了催化剂用量、PMS浓度、反应温度、常见阴离子种类在S_x@Co₃O₄-PMS体系下对MB降解率的影响，并评价了催化剂的循环稳定性。结果表明，随着硫修饰量的增加，Co₃O₄的催化性能逐渐升高，S₁@Co₃O₄表现出最佳的催化性能。硫元素以SO₄^2–     

CoFe2O4@MS活化过一硫酸盐处理6-硝氧体废水的研究

采用溶胶-凝胶法制备了催化剂CoFe₂O₄@MS,对以其活化过一硫酸盐（PMS）处理重要染料中间体废水 6-硝氧体废水进行了研究。采用扫描电子显微镜（SEM）、X 射线衍射仪（XRD）和傅立叶变换红外吸收光谱仪（FTIR）对催化剂进行表征。系统研究了 PMS投量、催化剂投量、初始 pH 和反应温度对 CoFe₂O₄@MS/PMS 体系处理 6-硝氧体废水的影响。结果表明：CoFe₂O₄@MS/PMS 催化体系对 6-硝氧体废水 COD 降解效果显著;6-硝氧体废水 COD 降解率随 PMS 投量先增加后减少,随催化剂投量和温度的增加而增加;6-硝氧体废水 COD 降解在强酸性条件下效果最好,在强碱性条件下效果大幅降低。在实际废水处理时,选择 PMS投量 12 g/L、催化剂投量 0.5 g/L,在常温（25 ℃）下无需调 pH,反应 60 min 内对 6-硝氧体废水的 COD 降解率可达 99.84%。实验结果可为非均相过渡金属催化剂活化PMS 处理萘磺...     

超细Co3O4粉体的制备及其应用

综述了超细Co3O4粉体的制备方法和特点,简要介绍了超细Co3O4粉体在催化剂、电极、陶瓷等领域的应用现状.     

ZIF-67衍生Co3O4/g-C3N4复合材料光催化降解盐酸四环素废水的研究

将ZIF-67与g-C₃N₄按一定质量比复合制备Co₃O₄/g-C₃N₄复合光催化材料,并以此来提高Co₃O₄的光催化性能。利用XRD、SEM和FT-IR对复合材料结构、性能和元素分布进行表征。结果表明,当盐酸四环素(TC-HCl)质量浓度为3 mg/L、质量分数为3%的Co₃O₄/g-C₃N₄投加量为15 mg且pH为中性时,催化剂光催化性能最佳,90 min降解盐酸四环素效率达到了91.1%。3%Co₃O₄/g-C₃N₄复合光催化剂重复使用5次后,其降解率仍可达到88.5%,表明该材料具有一定的光催化稳定性和重复利用性。体系自由基捕获实验证明,产生了·O^-₂、h⁺、·OH...     

颗粒Co3O4-g-C3N4吸附剂的制备及其对甲基橙的吸附性能研究

本文采用简单的一步热聚合法制备了钴掺杂碳基材料Co₃O₄-g-C₃N₄,并对其作为吸附剂的性能进行研究。所制备的材料通过XRD、XPS、BET对晶体结构、形貌、价态分布、比表面积以及孔径分布进行表征分析,实验以甲基橙为目标污染物进行吸附,其最大平衡吸附容量为118.83mg/g。Co₃O₄-g-C₃N₄吸附剂对甲基橙溶液吸附的动力学符合准二级动力学模型,吸附等温线符合Langmuir等温线。     

Co3O4/HY选择性催化苯甲醇氧化合成苯甲醛的研究

以HY分子筛为载体,采用水热法合成了系列Co₃O₄/HY复合分子筛催化剂,通过XRD、SEM、EDS、FT-IR、BET等手段对Co₃O₄/HY进行表征,并对Co₃O₄/HY分子筛催化氧气液相氧化苯甲醇合成苯甲醛的性能进行研究。结果表明,Co₃O₄的引入未破坏分子筛的骨架结构,且Co₃O₄在HY晶体表面形成片层蜂窝状多孔结构,可有效增加催化剂样品的介孔孔容和外表面积,增加催化活性。但Co₃O₄负载过量易出现堆叠现象,使得介孔孔容和外表面积降低,不利于氧化反应进行。以1.0-Co₃O₄/HY为催化剂,在适宜的反应条件下苯甲醇的转化率和苯甲醛的选择性分别达到73.2%和95.8%;催化剂重复使用5次,依然表现出较好的催化活性。     

CuFe2O4/硅藻土复合材料活化过一硫酸盐降解酸性橙7

通过柠檬酸辅助溶胶凝胶法制备了一种磁性复合材料CuFe2O4/硅藻土（CFD）。通过SEM、XRD、FTIR、XPS表征分析了材料的微观形貌结构和元素价态，并探讨了不同氧化体系、CFD质量浓度、PMS质量浓度、溶液初始pH、反应温度、阴离子种类等对CFD体系降解酸性橙7（AO7）的影响。结果表明，CFD上的球状颗粒CuFe2O4能够分散地负载在硅藻土上，减少了纯CuFe2O4的团聚，且CFD复合材料上的表面羟基及Fe3+/Fe2+、Cu2+/Cu+之间的价态循环参与了PMS的活化。在CFD质量浓度为0.5 g/L、PMS质量浓度为0.3 g/L，AO7质量浓度为50 mg/L，反应温度为30 ℃的最佳条件下，60 min时的AO7降解率为96.88%，CFD+PMS体系降解AO7过程符合准一级动力学模型，且相比于纯CuFe2O4+PMS体系，对AO7的降解速率常数提升了1.98倍。单因素影响试验结果表明，CFD+PMS体系的pH适用范围广（5~11），具有较低的活化能（Ea=31.77 kJ/mol）。猝灭试验表明，降解过程的主要活性物质为1O2和?O2-，同时也有SO4-?、?OH产生。     

一步法制备Co3O4及其电化学性能研究

以六水合硝酸钴为钴源、二甲基咪唑为有机配体,通过室温共沉淀法合成前驱体模板ZIF-67,而后再高温煅烧形成目标产物Co₃O₄材料。利用X-射线衍射与扫描电镜对目标产物进行表征,而后选用蓝电电池测试系统测试其倍率与循环性能。测试表明,在100mA/g电流密度条件下,Co₃O₄电极的首次充电容量和放电容量分别可有2069.2mAh/g和2928.3mAh/g,首次库伦效率有70.66%,循环使用寿命长,但容量维持率低,经100圈测试后容量保持率仅有35%;而在倍率测试中发现即使经过50次充放电,电流密度从2000mA/g回到100mA/g时,Co₃O₄电极的放电容量依然可以保持有1482mA/g,并且表现出良好的循环稳定性,说明Co₃O₄即使经过高倍率充放电,其结构依然可以保持稳定,具有较为不错的倍率性能。     

还原氧化石墨烯膜负载Co3O4活化过硫酸氢钾降解罗丹明B

以RGO(还原氧化石墨烯膜)为载体,采用水热法制备RGO/Co₃O₄高效复合催化剂。通过XRD(X射线衍射仪)、SEM(扫描电子显微镜)和XPS(X射线光电子能谱仪)等手段对复合催化剂的结构、形貌和化学组成等进行表征,并以RhB(罗丹明B)为降解物评价复合催化剂活化PMS(过硫酸氢钾)的反应活性。另外,考察了PMS质量浓度、RhB初始质量浓度、pH值及温度对催化剂活化PMS降解RhB的影响。结果表明：在PMS质量浓度为100 mg/L、RhB初始质量浓度为10 mg/L、pH值为7、温度为25℃时反应18 min对RhB降解率为98%。自由基捕获实验结合ESR(电子顺磁共振)结果表明体系中同时存在SO₄^-·和HO·2种活性自由基。循环实验结果显示催化剂经过5次循环使用后对RhB的降解率仍保持90%以上,显示优异的循环稳定性。     

Mn改性Co3O4催化剂及其低温CO氧化反应研究

利用锰掺杂对Co₃O₄基催化剂进行改性,合成了具有不同Mn掺杂量的Mn_aCo_bO_x催化剂,考察了Mn掺杂量对催化剂结构以及表面物种对CO氧化反应的影响。结果表明,随着Mn掺杂量的增加,Mn_aCo_bO_x催化剂的催化活性显著增加,其变化趋势呈现为“火山型”曲线。Mn₁Co₅O_x催化剂表现出最佳的催化活性,80℃实现CO完全氧化。Mn掺杂提高了催化剂表面Co³⁺含量,有利于CO的吸附和活化过程。同时,Mn掺杂也增强了催化剂的氧迁移能力,有利于CO氧化过程中CO₂的解吸过程和随后表面氧空位的再生过程。     

加热时间对Co_3O_4颗粒光催化性能的影响

以Co(NO_3)_2·6H_2O和CO(NH_2)_2为原料,十六烷基三甲基溴化铵为活性剂,采用水热-热分解法在不同加热时间(2 h、3 h、4 h、5 h)条件下制备纯相尖晶石结构的Co_3O_4颗粒。利用X射线衍射和电子扫描电镜研究Co_3O_4颗粒的结构和形貌,并以甲基橙为模拟废水,研究加热时间对Co_3O_4颗粒光催化性能的影响。结果表明,加热时间对Co_3O_4颗粒形貌影响很大,并直接影响其光催化性能。加热时间5 h制备的Co_3O_4结构疏松多孔,光催化性能最好,光照20 min,甲基橙降解率达95%。     

可见光增强g-C_3N_4/Co_3O_4胶体催化剂的催化产氢性能

通过水热法制备了具有可见光增产氢高性能的g-C_3N_4/Co_3O_4胶体催化剂,采用XRD、TEM、SEM和EDS等分析样品的组成和形貌结构。催化产氢结果表明,光照条件下g-C_3N_4/Co_3O_4胶体催化剂具有极高的催化产氢活性,TOF值高达58.2 min~(-1),通过拟合温度动力学曲线,得到了催化反应的活化能为15.73 kJ·mol~(-1)。对样品进行UV-vis和PL测试发现,g-C_3N_4/Co_3O_4胶体催化剂具有极高的光能利用率和电子-空穴分离率,并进一步阐述了光能促进催化产氢的作用机理。     

Microwave-assisted rapid fabrication of Co3O4 nanorods and application to the degradation of phenol

A novel microwave-assisted hydrothermal route for preparation of Co₃O₄ nanorods had been developed. The process contained two steps: first, nanorods of cobalt hydroxide carbonate were obtained from a mixed solution of 50 ml of 0.6 M Co(NO₃)₂·6H₂O and 2.4 g of urea under 500 W microwave irradiated for 3 min. Then, the cobalt hydroxide carbonate nanorods were calcined at 400 °C to fabricate pure cobaltic oxide (Co₃O₄) nanorods. Both nanorods were characterized by X-ray diffraction (XRD), scanning electron microscopy (SEM), thermogravimetry (TG), infrared (IR) and temperature-programmed reduction (TPR). The catalytic activity towards the degradation of phenol over Co₃O₄ nanorods was further studied under continuous bubbling of air through the liquid phase. The results showed that phenol was degraded into harmless products (CO₂ and malonic acid). The mechanism of phenol degradation was also discussed.     

Potassium-doped Co3O4 catalyst for direct decomposition of N2O

Direct decomposition of nitrous oxide (N₂O) on K-doped Co₃O₄ catalysts was examined. The K-doped Co₃O₄ catalyst showed a high activity even in the presence of water. In the durability test of the K-doped Co₃O₄ catalyst, the activity was maintained at least for 12 h. It was found that the activity of the K-doped Co₃O₄ catalyst strongly depended on the amount of K in the catalyst. In order to reveal the role of the K component on the catalytic activity, the catalyst was characterized by XRD, XPS, TPR and TPD. The results suggested that regeneration of the Co²⁺ species from the Co³⁺ species formed by oxidation of Co²⁺ with the oxygen atoms formed by N₂O decomposition was promoted by the addition of K to the Co₃O₄ catalyst.     

Combined CO/CH4 oxidation tests over Pd/Co3O4 monolithic catalyst: Effects of high reaction temperature and SO2 exposure on the deactivation process

CO and CH₄ combined oxidation tests were performed over a Pd (70 g/ft³)/Co₃O₄ monolithic catalyst in conditions of GHSV = 100,000 h⁻¹ and feed composition close to that of emission from bi-fuel vehicles. The effect of SO₂ (5 ppm) on CO and CH₄ oxidation activity under lean condition (λ = 2) was investigated. The presence of sulphur strongly deactivated the catalyst towards methane oxidation, while the poisoning effect was less drastic in the oxidation of CO. Saturation of the Pd/Co₃O₄ catalytic sites via chemisorbed SO₃ and/or sulphates occurred upon exposure to SO₂. A treatment of regeneration to remove sulphate species was attempted by performing a heating/cooling cycle up to 900 °C in oxidizing atmosphere. Decomposition of PdO and Co₃O₄ phases at high temperature, above 750 °C, was observed. Moreover, sintering of Pd⁰ and PdO particles along with of CoO crystallites takes place.     

氧化石墨烯负载纳米Fe3O4类芬顿处理制药废水

采用改进Hummer法制备了氧化石墨烯(GO)负载纳米Fe₃O₄磁性催化剂(Fe₃O₄/GO),对其进行了X射线衍射仪、扫描电子显微镜和能量-色散光谱表征,并将其应用于多相类芬顿处理高浓化学原料药生产废水。结果表明,Fe₃O₄颗粒成功负载在GO表面,且没有出现明显的团聚现象。当废水的pH为3,双氧水(H₂O₂的质量分数30%)投加量10 mL/L,催化剂投加量2 g/L,反应120 min后COD去除率达78%,UV254去除率高达81%。三维荧光光(3D-EEM)分析可知,芳香类和富里酸类物质在催化降解过程中得到有效去除。     

Catalytic decomposition of N2O over CeO2 promoted Co3O4 spinel catalyst

A series of CeO₂ promoted cobalt spinel catalysts were prepared by the co-precipitation method and tested for the decomposition of nitrous oxide (N₂O). Addition of CeO₂ to Co₃O₄ led to an improvement in the catalytic activity for N₂O decomposition. The catalyst was most active when the molar ratio of Ce/Co was around 0.05. Complete N₂O conversion could be attained over the CoCe0.05 catalyst below 400 °C even in the presence of O₂, H₂O or NO. Methods of XRD, FE-SEM, BET, XPS, H₂-TPR and O₂-TPD were used to characterize these catalysts. The analytical results indicated that the addition of CeO₂ could increase the surface area of Co₃O₄, and then improve the reduction of Co³⁺ to Co²⁺ by facilitating the desorption of adsorbed oxygen species, which is the rate-determining step of the N₂O decomposition over cobalt spinel catalyst. We conclude that these effects, caused by the addition of CeO₂, are responsible for the enhancement of catalytic activity of Co₃O₄.     

Characterization and tests of planar Co3O4 model catalysts prepared by chemical vapor deposition

The chemical vapor deposition method was used to deposit thin films of cobalt oxide starting with cobalt (II) acetylacetonate and oxygen. The deposition process was investigated and the obtained films were identified as a cubic spinel-type polycrystalline Co₃O₄ with a crystallite size of 30–40 nm. The coating was carbon-free and the surface oxygen concentration was measured to be 66 at.% with AES analysis. Smooth and highly uniform thin films were deposited on planar stainless steel substrates and subjected to TPR and catalysis tests that show positive correlation. The apparent activation energy of Co₃O₄ reduction to CoO was measured to be (33±5) kJ/mol. The catalytic activity of Co₃O₄ was investigated toward the conversion of both propane and ethanol to carbon dioxide. Though the catalytic action was registered at the same temperature, the deactivation process was seen to be different. The catalytic conversion of ethanol induces a fast deactivation process, which was linked to its high ability to reduce Co₃O₄.     

动物骨源羟磷灰石负载Co3O4用于N2O催化分解

通过焙烧猪骨和鸡骨获得羟磷灰石(nHAP)载体,并采用浸渍法制备Co3O4/nHAP催化剂。采用XRD、N2物理吸附-脱附、FT-IR和H2-TPR等对催化剂进行表征,在连续流动微反装置上考察催化剂催化分解N2O的性能。结果表明,相比于鸡骨源Co3O4/nHAP催化剂,以猪骨源HAP为载体的催化剂因其较大的比表面积以及较小的Co3O4粒径尺寸,提供了更多的活性位点。特别是猪骨源Co3O4/nHAP催化剂中适量的K、Na等元素促进了Co^3+到Co^2+的还原,削弱了Co-O键,使催化剂的催化活性显著提高。     

Co3O4 based catalysts for NO oxidation and NOx reduction in fast SCR process

Reaction activities of several developed catalysts for NO oxidation and NO_x (NO + NO₂) reduction have been determined in a fixed bed differential reactor. Among all the catalysts tested, Co₃O₄ based catalysts are the most active ones for both NO oxidation and NO_x reduction reactions even at high space velocity (SV) and low temperature in the fast selective catalytic reduction (SCR) process. Over Co₃O₄ catalyst, the effects of calcination temperatures, SO₂ concentration, optimum SV for 50% conversion of NO to NO₂ were determined. Also, Co₃O₄ based catalysts (Co₃O₄-WO₃) exhibit significantly higher conversion than all the developed DeNO_x catalysts (supported/unsupported) having maximum conversion of NO_x even at lower temperature and higher SV since the mixed oxide Co-W nanocomposite is formed. In case of the fast SCR, N₂O formation over Co₃O₄-WO₃ catalyst is far less than that over the other catalysts but the standard SCR produces high concentration of N₂O over all the catalysts. The effect of SO₂ concentration on NO_x reduction is found to be almost negligible may be due to the presence of WO₃ that resists SO₂ oxidation.