用MnSO_4作催化剂开管测定废水COD

本研究介绍了用硫酸锰代替硫酸银作催化剂快速开管测定废水中COD的方法。该方法降低了分析成本 ,且使样品的回流时间缩短到 12min ,而准确度和精密度同标准法基本相同。此法取样量少 ,消解速率快 ,适用于大批量水样的测定。     

废旧锌锰电池生物淋滤-水热法制备纳米锰锌铁氧体

以氧化硫硫杆菌(A.thiooxidans)和氧化亚铁钩端螺旋菌(L.ferrooxidans)为混合淋滤菌株对废旧锌锰电池进行了生物浸提,并以获取的淋滤液为前驱体,采用水热法制备出系列锰锌铁氧体软磁材料(Mn_(1-x)Zn_xFe_2O_4,x=0.2~0.8);结合X射线衍射(XRD)、扫描电镜-能谱(SEMEDX)、振动样品磁强计(VSM)、透射电镜(TEM)、红外光谱(FT-IR)、热重-差热分析(TG-DTA)等表征手段对制备材料的结构、形貌、磁学性能和稳定性进行分析.结果表明,在5%固液比(质量体积比,5 g/100 mL,以下均表述为"5%固液比")下,经过5 d的外源酸调控生物浸提,分别获得了84.5%、63.2%的Zn、Mn浸出效率;当Zn∶Mn∶Fe=0.4∶0.6∶2.0(物质的量比,即x=0.4)时,制备的纳米级Mn_(0.6)Zn_(0.4)Fe_2O_4性能最优,属纯相的立方尖晶石结构,颗粒分布均匀,饱和磁化强度(M_s)、剩余磁化强度(M_r)和矫顽力(H_c)分别为68.9 emu·g~(-1)、4.7 emu·g~(-1)和53.6 Oe,具有热稳定性和耐酸碱性,有望成为一种新型的水处理磁性材料.     

催化还原SO2为单质硫技术的研究进展

催化还原法脱硫是一种能够直接回收单质硫的烟气脱硫(FGD)技术,近年来倍受关注.尽管催化还原法脱硫技术所采用的催化剂的种类繁多,但是该技术所采用的还原剂的种类却相对较少.以H2、C、CH4、NH3和CO 5种还原剂为分类标准,综述了催化还原SO2为单质硫技术的主要研究成果;讨论了相关催化剂的性质和催化反应机理;分析了不同还原脱硫技术的优缺点.最后,论述了催化还原法脱硫有待解决的关键问题与发展趋势.     

石墨烯复合材料在水处理中的应用研究

新型碳材料石墨烯,因其比表面积大,物理、化学特性优异,通常作为吸附剂或复合材料载体,用于难降解有机废水处理.载体石墨烯改性后,可优化复合材料性能,包括溶解性和可控性.基于复合材料制备,选取典型污染物废水,如染料废水、苯酚废水、农药废水,从吸附处理和催化降解两方面展开,简要介绍石墨烯复合材料的应用研究及作用效果,显示出复合材料可有效提高污染物降解效率,回用效果好.此外,石墨烯复合材料在回用及实际应用方面仍有待进一步研究.     

炭催化剂吸附剂标准物质的研制

本文介绍了炭催化剂吸附剂标准物质的研制过程。对标准物质的制备技术、均匀性检验、稳定性考察及定值和不确定度进行了逐项分析。采用活性炭浸渍、煅烧技术制得炭催化剂吸附剂标准物质。试验结果表明,该标准物质定值结果准确,均匀性、稳定性良好。铜含量的标准值为11．06％,扩展不确定度为0．13％。     

A preliminary process design and economic assessment of a catalyst rejuvenation process for waste disposal of refinery spent catalysts

Spent hydroprocessing catalysts from refineries have been classified as hazardous solid waste by the United States Environmental Protection Agency (USEPA), refiners must find a viable but economical solution to solve this serious environmental issue. Catalyst rejuvenation is an attractive option for minimizing the environmental problems associated with spent catalysts. In this study, a preliminary design for such a process and the corresponding economic analysis are performed to assess the proposed catalyst rejuvenation process for metal-fouled spent catalysts generated in residue hydroprocessing units. The scenarios used in the economic assessment are based on three options of process synthesis and two operator modes. It is found that the option of rejuvenating medium and lightly fouled spent catalyst produced by the refinery will be the best solution for refiners, both environmentally and economically.     

废催化剂浸出规律的静态实验方法

利用静态浸出实验方法对废催化剂中重金属在不同固水比和浸出次数条件下的浸出规律进行了系统研究。实验发现浸出次数大于３次后,重金属的浸出浓度和浸出速率趋于稳定,同时固水比的增加也没有明显改变废催化剂中重金属的浸出。认为在浸取次数大于３次以后,随着表面溶质的溶解,浸出过程主要为内扩散所控制。     

UV-catalytic treatment of spent caustic from ethene plant with hydrogen peroxide and ozone oxidation

The performance of UV/H2O2, UV/O3 and UV/H2O2/O3 oxidation systems for treating spent caustic from an ethylene plant was investigated, in UV/H2O2 system, with the increase of H202 dosage, removal efficiencies of COD and the ratio of biochemical oxygen demand(BOD) to chemical oxygen demand(COD) of the effluent were increased and a better performance was obtained than the H2O2 system alone. In UV/H2O2 system, removal efficiency of COD reach 68% under the optimum condition, and BOD/COD ratio was significantly increased from 0.22 to 0.52. In UV/O3 system, with the increase of O3 dosage, removal efficiency of COD and BOD/COD ratio were increased, and a better performance was obtained than the O3 system alone. Under the optimum condition, removal efficiency of COD was 54%, and BOD/COD ratio was significantly increased from 0.22 to 0.48. In UV/H2O2/O3 system, COD removal efficiency was found to be 22.0% higher than UV/O3 system.     

Cracking styrene derivative polymers in decalin solvent with metal-supported carbon catalysts

The cracking of styrene derivative polymers dissolved in decalin was conducted with metal-supported carbon catalysts under an inert gas atmosphere to recover monosubstituted styrene or monosubstituted ethylbenzene in higher yields than is obtained by pyrolysis, and to elucidate the detailed reaction mechanisms in the solvent. Poly-(4-methylstyrene), poly-(4-t-butylstyrene), poly-(α-methylstyrene), and polystyrene were used. In decalin without a catalyst, each polymer was decomposed into the monomer, dimer, and trimer derived from the corresponding polymer except for poly-(α-methylstyrene), which was decomposed into the monomer and styrene. By using metal-supported carbon, the olefinic compounds derived from the corresponding polymer were thoroughly hydrogenated to the saturated form in a nitrogen atmosphere by a hydrogen transfer reaction from decalin, which was simultaneously dehydrogenated to tetralin and naphthalene with the evolution of hydrogen gas. In comparison with metal species, Pd- and Ru-supported carbon catalysts maintained the hydrogenation activity for a longer time and with a lower evolution of hydrogen than Pt or Rh. The dehydrogenation of decalin was mainly observed not on the metal surfaces, but on the carbon surfaces over Pd-supported carbon. Stabilization of the monomers will be able to suppress the coking which occurs with repolymerization in long running process. Received: July 19, 2000 / Accepted: March 16, 2001     

用废催化剂作原料制CIM油脂氢化催化剂

介绍用废油脂氢化催化剂作原料,回收Cu2+-Ni2+液,再用此液作原料制CIM油脂氢化催化剂的工艺流程和制作方法。结果表明:其所制成的CIM催化剂的性能与用工业硫酸铜和硫酸镍为原料制的CIM催化剂的性能相同。