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Biological granulated activated carbon fluidized bed reactor for atrazine remediation

机译:用于尿嘧啶修复的生物颗粒活性炭流化床反应器

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To show that an adsorbing biofilm carrier (GAC) can be advantageous for atrazine bioremediation over a non-adsorbing carrier, fluidized bed (FB) reactors were operated under atrazine limiting concentrations using Pseudomonas sp. strain ADP as the atrazine degrading bacteria. The following interrelated subjects were investigated: 1) atrazine adsorption to GAC under conditions of atrazine partial penetration in the biofilm, 2) differences in atrazine degradation rates and 3) stability of atrazine biodegradation under non-sterile anoxic conditions in the GAC reactor versus a reactor with a non-adsorbing biofilm carrier. Results from batch adsorption tests together with modeling best described the biofilm as patchy in nature with covered and non-biofilm covered areas. Under conditions of atrazine partial penetration in the biofilm, atrazine adsorption occurs in the non-covered areas and is consequently desorbed at the base of the biofilm substantially increasing the active biofilm surface area. The double flux of atrazine to the biofilm in the GAC reactor results in lower effluent atrazine concentrations as compared to a FB reactor with a non-adsorbing carrier. Moreover, under non-sterile denitrification conditions, atrazine degradation stability was found to be much higher (several months) using GAC as a biofilm carrier while non-adsorbing carrier reactors showed sharp deterioration within 30 days due to contamination of non-atrazine degrading bacteria.
机译:为了显示的吸附生物膜载体(GAC)可以在非吸附载体是莠去津生物修复有利的,流化床(FB)反应器下使用假单胞菌属阿特拉津浓度的限制操作。菌株ADP作为阿特拉津降解细菌。以下相关主题进行了研究:1)阿特拉津吸附到GAC生物膜中的莠去津部分穿透的条件下,2)在阿特拉津降解率的差异和3)在GAC反应器与反应器非无菌缺氧条件下阿特拉津降解的稳定性与非吸附生物膜载体。结果从分批吸附试验与建模最佳一起描述的生物膜在本质上与所覆盖的和非生物膜覆盖的区域不规则。下在生物膜阿特拉津部分穿透的条件下,莠去津吸附发生在未覆盖区域,并在所述生物膜显着增加活性生物膜表面积的基极因此解吸。莠去津以在下部流出物阿特拉津浓度GAC反应器结果生物膜的双通量相比,具有非吸附载体的FB反应器中。此外,非无菌脱氮的条件下,莠去津降解的稳定性,发现使用GAC作为生物膜载体而非吸附载体的反应器显示出在30天内急剧恶化由于非阿特拉津降解细菌的污染要高得多(几个月)。

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