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Bioremediation of hydrogen sulfide from gas stream in continuous culture with cell recycle

机译:通过细胞循环在连续培养中对气流中的硫化氢进行生物修复

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Biodesulfurization of sour gas has been carried out in a continuous stirred tank bioreactor (3.5 L)equipped with absorption tank (1.5 L) and cell recycle unit (1 L). Pure culture of sulfur oxidizedbacteria was isolated from native sulfur hot spring. Continuous biodesulfurization was conducted withcell decanter as cell separator. Cell concentration was increased from 1.35 to 1.96 g.L-1 as cell recycleratio was increased from 0 to 0.6. Maximum hydrogen sulfide transfer rate and volumetric masstransfer coefficient (kLa) was determined to be 0.0463 mol.m-3h-1 and 0.0202 h-1 at 36oC and 250 rpm,respectively. Application of absorption tank improved sulfide removal rate under cell recyclinganaerobic conditions approximately by 18%. The optimal dilution and gas flow rate were achieved at0.0186 h-1 and 2 mL.min-1. The removal of H2S at high concentration in the sour gas (5% v/v H2S, 5%v/v CO2, 10% v/v Ar, 80% v/v CH4 ) was determined to be 98%.
机译:酸性气体的生物脱硫已在配备有吸收罐(1.5 L)和细胞循环装置(1 L)的连续搅拌釜生物反应器(3.5 L)中进行。从天然硫温泉中分离出纯硫氧化细菌培养物。用细胞de析器作为细胞分离器进行连续的生物脱硫。随着细胞回收率从0增加到0.6,细胞浓度从1.35 g.L-1增加到1.96 g.L-1。在36oC和250 rpm下,最大硫化氢转移速率和体积传质系数(kLa)分别确定为0.0463 mol.m-3h-1和0.0202 h-1。吸收罐的应用使细胞回收厌氧条件下的硫化物去除率提高了约18%。在0.0186 h-1和2 mL.min-1时达到了最佳的稀释度和气体流速。酸性气体(5%v / v H2S,5%v / v CO2、10%v / v Ar,80%v / v CH4)中高浓度的H2S去除率测定为98%。

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