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厌氧移动床生物膜反应器处理乳制品行业乳清渗透液的性能及动力学评估

Performance and kinetic evaluation of anaerobic moving bed biofilm reactor for treating milk permeate from dairy industry.

作者信息

Wang S, Rao N Chandrasekhara, Qiu R, Moletta R

机构信息

School of Environmental Science and Engineering, Sun Yat-sen University, Guangzhou 510275, China.

出版信息

Bioresour Technol. 2009 Dec;100(23):5641-7. doi: 10.1016/j.biortech.2009.06.028. Epub 2009 Jul 23.

DOI:10.1016/j.biortech.2009.06.028
PMID:19631525
Abstract

High strength milk permeate derived from ultra-filtration based cheese making process was treated in an anaerobic moving bed biofilm reactor (AMBBR) under mesophilic (35 degrees C) condition. Total chemical oxygen demand (TCOD) removal efficiencies of 86.3-73.2% were achieved at organic loading rates (OLR) of 2.0-20.0 g TCOD L(-1) d(-1). A mass balance model gave values of methane yield coefficient (Y(G/S)) and cell maintenance coefficient (k(m)) of 0.341 L CH(4) g(-1) TCOD(removed) and 0.1808 g TCOD(removed) g(-1) VSS d(-1), respectively. The maximum substrate utilization rate U(max) was determined as 89.3 g TCOD L(-1) d(-1) by a modified Stover-Kincannon model. Volumetric methane production rates (VMPR) were shown to correlate with the biodegradable TCOD concentration through a Michaelis-Menten type equation. Moreover, based on VMPR and OLR removed from the reactor, the sludge production yield was determined as 0.0794 g VSS g(-1) TCOD(removed).

摘要

源自基于超滤的奶酪制作过程的高强度乳清透过液,在中温(35摄氏度)条件下,于厌氧移动床生物膜反应器(AMBBR)中进行处理。在2.0 - 20.0 g TCOD L⁻¹ d⁻¹的有机负荷率(OLR)下,总化学需氧量(TCOD)去除效率达到86.3 - 73.2%。质量平衡模型得出甲烷产率系数(Y(G/S))和细胞维持系数(k(m))的值分别为0.341 L CH₄ g⁻¹ TCOD(去除)和0.1808 g TCOD(去除) g⁻¹ VSS d⁻¹。通过改进的Stover - Kincannon模型确定最大底物利用率U(max)为89.3 g TCOD L⁻¹ d⁻¹。通过米氏方程表明,体积甲烷产生速率(VMPR)与可生物降解的TCOD浓度相关。此外,基于从反应器中去除的VMPR和OLR,确定污泥产率为0.0794 g VSS g⁻¹ TCOD(去除)。

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