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纸浆和造纸工业沉淀物纤维的修复:实验室规模厌氧反应器研究及放大思路。

Remediation of sedimented fiber originating from pulp and paper industry: Laboratory scale anaerobic reactor studies and ideas of scaling up.

机构信息

Laboratory of Chemistry and Bioengineering, Tampere University of Technology, P.O. Box 541, FIN-3310, Tampere, Finland.

Laboratory of Chemistry and Bioengineering, Tampere University of Technology, P.O. Box 541, FIN-3310, Tampere, Finland; Finnish Consulting Group (FCG Suunnittelu ja tekniikka Oy), P.O. Box 950, FIN-00601, Helsinki, Finland.

出版信息

Water Res. 2018 Oct 15;143:209-217. doi: 10.1016/j.watres.2018.06.054. Epub 2018 Jun 26.

Abstract

Anaerobic treatment of sedimented fibers collected from bottom of a bay that had been receiving pulp and paper mill wastewater for about 70 years were studied for the first time in semi-continuously fed continuously stirred tank reactors (CSTR). Anaerobic treatment of the fiber sediment was shown to be feasible, without dilution and with nitrogen and buffer supplement, at organic loading rates (OLR) up to 2.5 kg VS/md and hydraulic retention times (HRT) of 60 d resulting in methane yields of 201 ± 18 L CH/kg VS. Co-digestion of sedimented fiber with sewage sludge at an OLR of 1.5 kg VS/md and HRT of 20 d resulted in a methane production of 246 ± 10 L CH/kg VS. The techno-economic feasibility of mono and co-digestion process together with several case dependent factors such as maximum operable OLR, digestate utilization needs to be evaluated before making further conclusions for larger scale remediation applications.

摘要

首次在半连续进料的连续搅拌槽式反应器(CSTR)中研究了经过大约 70 年接收制浆造纸厂废水的海湾底部收集的沉淀纤维的厌氧处理。在不稀释且补充氮和缓冲剂的情况下,在有机负荷率(OLR)高达 2.5kgVS/md 和水力停留时间(HRT)为 60d 的条件下,对纤维沉积物进行厌氧处理是可行的,其甲烷产率为 201±18LCH/kgVS。在 OLR 为 1.5kgVS/md 和 HRT 为 20d 的条件下,将沉淀纤维与污水污泥进行共消化,甲烷产量为 246±10LCH/kgVS。在做出进一步的大规模修复应用的结论之前,需要对单消化和共消化工艺的技术经济可行性以及一些取决于案例的因素(如最大可操作 OLR、消化物利用需求)进行评估。

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