首页> 外文期刊>Bioresource Technology: Biomass, Bioenergy, Biowastes, Conversion Technologies, Biotransformations, Production Technologies >Substrates removal and growth kinetic characteristics of a heterotrophic nitrifying-aerobic denitrifying bacterium, Acinetobacter harbinensis HITLi7(T) at 2 degrees C
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Substrates removal and growth kinetic characteristics of a heterotrophic nitrifying-aerobic denitrifying bacterium, Acinetobacter harbinensis HITLi7(T) at 2 degrees C

机译:底物去除和生长动力学特性,异养硝化的硝化碳化细菌,2摄氏度的哈尔比诺斯菌HALLI7(T)

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In order to investigate the heterotrophic nitrification and aerobic denitrification ability of Acinetobacter harbinensis HITLi7(T) at 2 degrees C, both the growth parameters and substrates utilization characteristics were tested and appropriated kinetic models were obtained in this study. Under the initial concentration of 5 mg/L, the maximum NH4+-N and NO3--N degradation rates were 0.076 mg NH4+-N/L/h and 0.029 mg NO3--N/L/h, respectively. At the simultaneous presence of 2.5 mg/L NH4+-N and NO3--N, the maximum nitrate removal rate increased to 0.054 mg NO3--N/L/h (1.86 folds), while a slight decrease was observed in NH4+-N removal. Two double-substrate models, Contois-Contois (1) for NH4+-N and TOC, Monod-Contois (2) for NO3--N and TOC matched well with the experimental data. The kinetic parameters were determined as mu(max1) = 0.095 h(-1), B-A1=0.012 mg/L, B-T1=0.784 g TOC/g biomass (R-1(2) = 0.9997), and mu(max2) = 0.032 h(-1), K-N2 = 0.375 mg/L, B-T2 = 1.108 g TOC/g biomass (R-2(2) = 0.9731) by multiple regression equation.
机译:为了探讨哈比斯(T)在2摄氏度的异养硝化和有氧脱氮能力,测试生长参数和底物利用特性,并在该研究中获得了应用的动力学模型。在5mg / L的初始浓度下,分别为0.076mg NH 4 + -N / L / h和0.029mg NO 3 - N / L / h的最大NH 4 + -N和NO 3-N和NO 3-N和NO 3 -N-N / L / h。在2.5mg / l NH4 + -N和NO3 - N的同时存在下,最大硝酸盐去除率增加到0.054mg NO 3 - N / L / H(1.86倍),而NH4 + -N中观察到略微减少移动。用于NH4 + -N和TOC的两种双基板模型,CONTOIS-CONTOIS(1),NO3 - N和TOC的MONOD-CONTOIS(2)与实验数据相匹配。测定动力学参数为mu(max1)= 0.095 h(-1),b-a1 = 0.012 mg / l,b-t1 = 0.784g toc / g生物量(R-1(2)= 0.9997),和亩(MAX2)= 0.032h(-1),K-N2 = 0.375mg / L,B-T2 = 1.108g TOC / g BO / g生物质(R-2(2)= 0.9731)通过多元回归方程式。

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