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两段式气相生物反应器用于同时去除硫化氢、甲醇和α-蒎烯。

Two-stage gas-phase bioreactor for the combined removal of hydrogen sulphide, methanol and alpha-pinene.

机构信息

Chemical Engineering Laboratory, Faculty ofSciences, University of La Coruña, Rúa Alejandro de la Sota, 1,15008-La Coruña, Spain.

出版信息

Environ Technol. 2009 Nov;30(12):1261-72. doi: 10.1080/09593330903196868.

Abstract

Biological treatment systems have emerged as cost-effective and eco-friendly techniques for treating waste gases from process industries at moderately high gas flow rates and low pollutant concentrations. In this study, we have assessed the performance of a two-stage bioreactor, namely a biotrickling filter packed with pall rings (BTF, 1st stage) and a perlite + pall ring mixed biofilter (BF, 2nd stage) operated in series, for handling a complex mixture of hydrogen sulphide (H2S), methanol (CH3OH) and alpha-pinene (C10H16). It has been reported that the presence of H2S can reduce the biofiltration efficiency of volatile organic compounds (VOCs) when both are present in the gas mixture. Hydrogen sulphide and methanol were removed in the first stage BTF, previously inoculated with H2S-adapted populations and a culture containing Candida boidinii, an acid-tolerant yeast, whereas, in the second stage, alpha-pinene was removed predominantly by the fungus Ophiostoma stenoceras. Experiments were conducted in five different phases, corresponding to inlet loading rates varying between 2.1 and 93.5 g m(-3) h(-1) for H2S, 55.3 and 1260.2 g m(-3) h(-1) for methanol, and 2.8 and 161.1 g m(-3) h(-1) for alpha-pinene. Empty bed residence times were varied between 83.4 and 10 s in the first stage and 146.4 and 17.6 s in the second stage. The BTF, working at a pH as low as 2.7 as a result of H2S degradation, removed most of the H2S and methanol but only very little alpha-pinene. On the other hand, the BF, at a pH around 6.0, removed the rest of the H2S, the non-degraded methanol and most of the alpha-pinene vapours. Attempts were originally made to remove the three pollutants in a single acidophilic bioreactor, but the Ophiostoma strain was hardly active at pH <4. The maximum elimination capacities (ECs) reached by the two-stage bioreactor for individual pollutants were 894.4 g m(-3) h(-1) for methanol, 45.1 g m(-3) h(-1) for H2S and 138.1 g m(-3) h(-1) for alpha-pinene. The results from this study showed the potential effectiveness of a two-stage bioreactor for treating H2S together with two hydrophilic and hydrophobic VOCs that are typically emitted from wood industries.

摘要

生物处理系统已成为在中等气流速率和低污染物浓度下处理工业废气的具有成本效益和环保的技术。在这项研究中,我们评估了两级生物反应器的性能,即填充钯环的生物滴滤器(BTF,第一级)和珍珠岩+钯环混合生物过滤器(BF,第二级)串联运行,用于处理含有硫化氢(H2S),甲醇(CH3OH)和α-蒎烯(C10H16)的复杂混合物。据报道,当两种气体都存在于气体混合物中时,H2S 的存在会降低挥发性有机化合物(VOC)的生物过滤效率。在第一级 BTF 中,先前接种了适应 H2S 的种群和一种含有耐酸酵母 Candida boidinii 的培养物,可去除 H2S 和甲醇,而在第二级中,主要通过真菌 Ophiostoma stenoceras 去除α-蒎烯。实验在五个不同的阶段进行,对应于 H2S 的入口加载速率在 2.1 和 93.5 g m(-3) h(-1)之间变化,甲醇的入口加载速率在 55.3 和 1260.2 g m(-3) h(-1)之间变化,α-蒎烯的入口加载速率在 2.8 和 161.1 g m(-3) h(-1)之间变化。在第一级中,空床停留时间在 83.4 和 10 s 之间变化,在第二级中,空床停留时间在 146.4 和 17.6 s 之间变化。由于 H2S 的降解,BTF 的工作 pH 低至 2.7,可去除大部分 H2S 和甲醇,但仅去除很少量的α-蒎烯。另一方面,BF 的 pH 值约为 6.0,可去除其余的 H2S、未降解的甲醇和大部分α-蒎烯蒸气。最初尝试在单个嗜酸生物反应器中去除这三种污染物,但在 pH <4 时,Ophiostoma 菌株几乎没有活性。两级生物反应器对单个污染物的最大去除容量(EC)分别为 894.4 g m(-3) h(-1)(甲醇),45.1 g m(-3) h(-1)(H2S)和 138.1 g m(-3) h(-1)(α-蒎烯)。这项研究的结果表明,两级生物反应器在处理同时含有两种典型木材工业排放的亲水性和疏水性 VOC 的 H2S 方面具有潜在的有效性。

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