Removal of toluene from air streams by cobalt-copper bimetallic catalysts supported on sepiolite

Abstract

Oxidative removal of toluene using copper and cobalt bimetallic catalysts with varying molar ratios supported on sepiolite was investigated. The catalysts prepared by a deposition precipitation method and were characterized using X-ray diffraction, nitrogen adsorption-desorption, field emission scanning electron microscopy, H₂-temperature-programmed reduction, transmission electron microscope, and inductive coupled plasma atomic emission spectroscopy. The species supported on sepiolite are Co₃O₄, CuO, and CuCo₂O₄. The activities of the tested catalysts increased in the order 0Co-4Cu/Sep <1Co-3Cu/Sep <4Co-0Cu/Sep <1Co-1Cu/Sep <3Co-1Cu/Sep. The latter exhibiting 90% toluene oxidative degradation at 288?°C within 15?h, having high selectivity towards CO₂, and being stable at 300?°C up to 15?h. In conclusion, this study showed that sepiolite has excellent properties as a support.     

氧化亚铁硫杆菌浸出废旧锂离子电池的工艺条件

考察了接种量、振荡条件、浸出液以及电池原料对氧化亚铁硫杆菌浸出废旧锂离子电池的影响.研究结果表明,浸出10 d,钴浸出率达到48.5%,之后,浸出率不再增加;当接种量在2.5%—12.5%之间时,钴浸出率在第10天都为47.6%,接种量对浸出率无影响;振荡过程中控制温度为35℃时,钴浸出率最佳,并随着振荡速率的升高而增加;浸出液中加入硫磺对浸出影响不大,初始pH值在1.5—2.5范围内,都适合钴酸锂的浸出,而初始亚铁离子浓度在45 g.L-1条件下浸出效果最好;选择固液比为3%最佳,并且钴酸锂粉末的粒度大小对浸出率无影响.     

酸浸出法回收冶金污泥中的有价金属

采用二次酸浸出的方法回收镍钴湿法冶金工业污泥中的有价金属。先采用水和硫酸作为浸出剂浸出Mg和Na,最佳工艺条件为浸出液的pH 7.5、浸出时间5 min、浸出剂体积与干污泥质量的比(ω)为10 mL/g。再采用硫酸作为浸出剂、焦亚硫酸钠作为还原剂进行二次酸浸,在硫酸与污泥质量比为1.3、焦亚硫酸钠与污泥质量比为0.3、ω为5 mL/g、浸出温度85℃、浸出时间20 min的最佳工艺条件下,Co、Ni、Cu、Mn和Zn的浸出率分别达92.45%、93.48%、89.52%、97.78%和94.79%。经XRD表征,浸出后污泥中未见原污泥中的矿物相,说明原污泥中的矿物几乎全部被溶解。     

碱熔法回收废催化剂中的钴、钼和铝

采用碱熔法从废钴钼催化剂中回收钴、钼和铝。该方法的工艺过程为 :将废催化剂与纯碱按质量比 1∶1 8混合 ,在焙烧温度 90 0℃条件下 ,焙烧 2h ;用 2倍于熔块的沸水浸取30min ;用稀硫酸调浸取液 pH至 6 ,浸取液中的铝形成氢氧化铝被回收 ;然后除盐并回收钼酸钠 ;使酸浸黑渣中的钴形成氢氧化钴并脱水氧化成为氧化钴。用该工艺回收铝、钼和钴 ,其回收率可达 95 %以上 ,回收产品的纯度可达 97%以上。     

不同酸碱度土壤阳离子交换量的测定研究

为了能够快速准确测定不同酸碱度土壤中的阳离子交换量,弥补现行标准方法的不足,对三氯化六氨合钴浸提-分光光度法中的土壤称样量、pH、浸提时间、浸提温度和离心时间等条件进行了优化。优化后的方法检出限为0.43 cmol^+/kg,测定下限为1.72 cmol^+/kg,方法实验室内精密度为0.2%~1.8%,适用于大批量土壤样品中阳离子交换量的测定。     

Concentration of some heavy metals in organically grown primitive,old and modern wheat genotypes: Implications for human health

The concentration of six HMs (Cd, Cr, Co, Pb, Hg and Ni) was analysed in 321 organically grown winter and spring wheat genotypes from six genotype groups, i.e. selections, old landraces, primitive wheat, spelt, old cultivars and cultivars. Also the potential risk of individual toxic HM to human health was estimated by using the Hazard Quotient (HQ). Significantly the lowest grain concentration of Cd was found in primitive wheat as compared to all other investigated genotype groups. Intake of HM by consumption of whole wheat grain was not found to pose a health risk to human for any of the investigated genotype groups. The bio-concentration factor of Cd for the different genotype groups indicated a lower ability to accumulate Cd for primitive wheat as compared to other genotype groups. The primitive wheat was found the most promising and might be of interest in future wheat breeding programs to develop wheat genotypes with low HMs concentration in the grain.     

苯甲酸生产残液中锰、钴和镍的提取及分离

探讨了苯甲酸生产残液中锰、钴和镍的提取及分离方法。首先采用酸溶液提取残液中的金属元素;然后通过氨水沉淀法分离锰;最后使用p507萃取剂分离钴和镍。实验结果表明:当苯甲酸生产残液中锰、钴和镍的质量分数分别为0.085 0%,0.307 1%,0.015 5%时,在硫酸浓度为2.0 mol/L、过氧化氢溶液质量分数为25%的条件下,锰、钴和镍的提取率分别为88.59%,87.77%,86.50%;当氨水浓度为2 mol/L时,锰的沉淀率达94.24%;在平衡水相p H为4、p507萃取剂皂化率为60%、油相中p507萃取剂的体积分数为15%的条件下,钴萃取率达87.53%,镍萃取率仅为8.46%,钴镍分离系数为68.70。     

5-氯-2-(吡啶偶氮)-1,3-二氨基苯分光光度法测定水质钴

采用5-氯-2-(吡啶偶氮)-1,3-二氨基苯分光光度法测定水质钴。对分析方法的样品前处理、样品保存、样品分析条件、干扰消除、检出限及测定范围、实际样品测定进行了深入研究和技术改进。水样经消解后测定的方法检出限为0.009 mg/L,经富集后测定的方法检出限为4×10-4mg/L,干扰消除实验的回收率为96%~101%,地表水、地下水、生活污水及工业废水等4种类型水样的加标回收率为92%~103%。     

金属络合剂在烟气同时脱硫脱硝中的应用

液相络合法是烟气同时脱硫脱硝中广泛应用的方法之一。液相络合法常用的金属络合剂有亚铁络合剂和钴络合剂等。重点介绍了亚铁氨羧络合剂、含-SH的亚铁络合剂和六氨合钴络合剂、乙二胺合钴络合剂等同时脱硫脱硝的基本过程及常用吸收液的再生方法,指出了金属络合剂在烟气同时脱硫脱硝中应用时存在的问题及今后的发展方向。     

用废锂电池制备Co3O4

将废锂电池正极用酸溶解,再分别采用分步沉淀法和吸附沉淀法去除废锂电池液中的Fe^3＋,Al^3＋,Ca^2＋,Mg^2＋,抽滤后得到含CoSO。的滤液;用NaHCO3作沉淀剂,对CoSO4滤液进行沉淀反应,将得到的沉淀物过滤、洗涤、干燥后得CoCO4粉末;将CoCO4粉末进行煅烧后得Co3O4粉末。实验得出的制备CoCO4粉末的最佳工艺条件：反应温度50℃,用NaHCO,作沉淀剂;制备Co3O4粉末的最佳工艺条件：煅烧温度600℃,煅烧时间大于4h。在该条件下得到的Co3O4粉末符合锂电池生产的要求。