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Removal of volatile organic compound (VOC) vapors in biotrickling filters: Process modeling and validation with chlorinated aromatic compounds.

机译:去除生物滴滤池中的挥发性有机化合物(VOC)蒸气:使用氯化芳族化合物进行工艺建模和验证。

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This study dealt with the removal of vapors of volatile organic compounds from airstreams in biotrickling filters (BTFs). A detailed general model was developed for describing the process under steady-state conditions. The model accounts for mass transfer between phases (air, liquid, biofilm) and biodegradation of pollutants in the biofilm. It also accounts for potential kinetic interactions among pollutants as well as potential process limitations by oxygen availability.; The general model was experimentally validated using mono-chlorobenzene (m-CB) and ortho-dichlorobenzene (o-DCB) as model compounds either alone or in mixture with each other. Before BTF experiments were undertaken, a systematic kinetic study was performed with suspended cultures. Two microbial consortia, called m-CB and o-DCB consortium, were used. In all cases it was found that self-inhibition (Andrews kinetics) takes place. When the two compounds are present in a mixture they are simultaneously used but are involved in a competitive cross-inhibition which is stronger from m-CB presence on o-DCB removal than vice versa. Studies on the effect of pH showed that a value of 6.8 is optimal.; Experiments in a BTF with the m-CB consortium and m-CB as model compound were performed. The percent m-CB removal observed ranged from 79 to 96% and the maximum removal rate was 60 gm{dollar}sp{lcub}-3{rcub}{dollar}-packing h{dollar}sp{lcub}-1{rcub}.{dollar} Removal of o-DCB vapor was found to be more difficult. In fact, using a BTF with the o-DCB consortium percent o-DCB removal ranged from 57 to 76% and the removal rate never exceed 30 gm{dollar}sp{lcub}-3{rcub}{dollar}-packing h{dollar}sp{lcub}-1{rcub}.{dollar} Experiments in a BTF with the o-DCB consortium and airstreams laden by both m-CB and o-DCB validated the proposed model for the case of mixtures. In all cases, a very good agreement between data and model predictions was found. Co-current operation was found to be slightly superior to the counter-current mode; this is also predicted by the model.; Regarding oxygen, it was found that an oxygen-controlled zone exists in the BTF (close to the inlet of the polluted air) when the total VOC concentration is relatively high. For the hydrophobic compounds used in this study oxygen availability does not seem to play a crucial role. Model sensitivity studies have shown that at least two kinetic constants are important and thus, zero or first-order kinetic approximations cannot and should not be made.; The model developed in this study along with the computer code generated for solving the equations can be used in (at least preliminary) scale-up calculations for the design of BTFs.
机译:这项研究涉及从生物滴滤器(BTF)中去除气流中挥发性有机化合物的蒸气。开发了详细的通用模型来描述稳态条件下的过程。该模型考虑了相(空气,液体,生物膜)之间的质量传递和生物膜中污染物的生物降解。它还考虑到了污染物之间潜在的动力学相互作用以及由于氧气的利用而可能产生的工艺限制。使用一氯苯(m-CB)和邻二氯苯(o-DCB)作为模型化合物单独或相互混合,通过实验验证了该通用模型。在进行BTF实验之前,对悬浮培养物进行了系统动力学研究。使用了两个微生物联合体,称为m-CB和o-DCB联合体。在所有情况下,都发现发生了自我抑制(安德鲁斯动力学)。当两种化合物以混合物形式存在时,它们可同时使用,但会参与竞争性交叉抑制,这比邻-DCB脱除m-CB时要强,反之亦然。 pH值影响的研究表明,最佳值为6.8。在以m-CB联盟和m-CB作为模型化合物的BTF中进行了实验。观察到的m-CB去除百分比在79%至96%之间,最大去除率为60 gm {dollar} sp {lcub} -3 {rcub} {dollar} -packing h {dollar} sp {lcub} -1 {rcub }。{dollar}发现去除o-DCB蒸气比较困难。实际上,在o-DCB联盟使用BTF的情况下,o-DCB的去除百分比范围为57%至76%,去除率永远不会超过30 gm {dollar} sp {lcub} -3 {rcub} {dollar} -packing h { dollar} sp {lcub} -1 {rcub}。{dollar}在带有o-DCB财团和m-CB和o-DCB都载有气流的BTF中进行的实验验证了所提出的混合物模型。在所有情况下,都发现数据与模型预测之间有很好的一致性。发现并流操作略优于逆流模式。模型也对此进行了预测。关于氧气,发现当总VOC浓度相对较高时,BTF中存在氧气控制区(靠近污染空气的入口)。对于本研究中使用的疏水性化合物,氧的利用似乎没有起到至关重要的作用。模型敏感性研究表明,至少两个动力学常数很重要,因此不能也不应该建立零或一阶动力学近似。本研究中开发的模型以及为求解方程式而生成的计算机代码可用于(至少是初步的)按比例放大设计BTF的计算中。

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