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Enzyme-catalyzed polymerization and precipitation of aromatic compounds from wastewater.

机译:酶催化的聚合反应和废水中芳族化合物的沉淀。

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摘要

Horseradish peroxidase (HRP) demonstrates a valuable potential for wastewater treatment by catalyzing the polymerization and precipitation of aromatic compounds from water. It acts on a broad range of compounds including those that are biorefractory or toxic to microbes and retains its catalytic ability over wide ranges of temperature, pH, and contaminant concentration. Removal efficiency is dependent on the nature of the aromatic substrate and the dose of enzyme used. Optimal catalytic lifetime was achieved in the pH range of 7 to 9 for the eight phenolic compounds used in this study. Enzymatic precipitation should be conducted at temperatures below 35$spcirc$C to prevent significant thermal inactivation of peroxidase. The stoichiometry of the reaction between aromatic compound and hydrogen peroxide was unity. Enhanced removal of hard-to-remove compounds was accomplished by co-precipitation with other substrates of HRP. A kinetic model was developed which matches the trends of data collected in a batch reactor under various conditions of enzyme, aromatic substrate and peroxide concentrations. Further development is required to define the mechanisms and kinetics of inactivation to extend application of the model to the design of a full-scale waste treatment system. The catalytic lifetime of the enzyme may be extended by maintaining a low instantaneous enzyme concentration in the reaction mixture. The enzyme catalyzed polymerization process was implemented in a continuous stirred tank reactor (CSTR) configuration because reactant and enzyme concentrations are lowered immediately upon entering the reactor causing a reduction in free radical inactivation and Compound III formation. Catalytic turnovers achieved in single and multiple CSTRu27s in series were significantly higher than those observed in batch reactors when sufficient retention time was provided.Dept. of Civil and Environmental Engineering. Paper copy at Leddy Library: Theses u26 Major Papers - Basement, West Bldg. / Call Number: Thesis1991 .N578. Source: Dissertation Abstracts International, Volume: 53-09, Section: B, page: 4923. Supervisors: J. K. Bewtra; K. E. Taylor. Thesis (Ph.D.)--University of Windsor (Canada), 1991.
机译:辣根过氧化物酶(HRP)通过催化聚合和从水中沉淀出芳香族化合物,在废水处理方面显示出了宝贵的潜力。它可作用于多种化合物,包括对微生物具有生物耐性或毒性的化合物,并在很宽的温度,pH和污染物浓度范围内保持其催化能力。去除效率取决于芳族底物的性质和所用酶的剂量。对于本研究中使用的八种酚类化合物,在7至9的pH范围内实现了最佳的催化寿命。酶促沉淀应在低于35°C的温度下进行,以防止过氧化物酶的明显热失活。芳族化合物与过氧化氢之间反应的化学计量是统一的。通过与HRP的其他底物共沉淀,可以增强去除难去除化合物的能力。建立了动力学模型,该动力学模型与在酶,芳族底物和过氧化物浓度的各种条件下在间歇反应器中收集的数据的趋势相匹配。需要进一步的发展来定义失活的机理和动力学,以将模型的应用扩展到大规模废物处理系统的设计。酶的催化寿命可以通过维持反应混合物中的低瞬时酶浓度来延长。酶催化的聚合过程是在连续搅拌釜反应器(CSTR)配置中实施的,因为进入反应器后,反应物和酶的浓度会立即降低,从而导致自由基失活和化合物III形成的减少。当提供足够的保留时间时,单个和多个CSTR u27s中实现的催化转化率显着高于分批反应器中观察到的催化转化率。土木与环境工程系。莱迪图书馆的纸质副本:论文主要论文-西楼地下室。 /致电号码:Thesis1991 .N578。资料来源:国际论文摘要,第53-09卷,第B部分,第4923页。主管:J. K. Bewtra; K. E. Taylor。论文(博士学位)-温莎大学(加拿大),1991。

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    Nicell James A.;

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