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采用修正的厌氧消化模型 No.1 对厌氧正向渗透生物反应器中的甲烷生成进行建模。

Modeling methane production in anaerobic forward osmosis bioreactor using a modified anaerobic digestion model No. 1.

机构信息

Dept. of Environmental Engineering, Korea Maritime and Ocean University, 727 Taejong-ro, Yeongdo-Gu, Busan 49112, Republic of Korea.

Department of Civil Engineering, Pukyong National University, 45 Yongso-ro, Nam-gu, Busan 48513, Republic of Korea.

出版信息

Bioresour Technol. 2018 Sep;264:211-218. doi: 10.1016/j.biortech.2018.04.125. Epub 2018 May 26.

Abstract

Anaerobic membrane bioreactor (AnMBR) using microfiltration (MF) or ultrafiltration (UF) membranes was introduced to enhance poor biomass retention of conventional anaerobic digestion (CAD). Recently, forward osmosis (FO) membrane have been applied to AnMBR, which is called AnFOMBR. FO membrane assures not only high biomass retention but also high removal efficiency for low molecular weight (LMW) matters. Methane production rates in CAD, AnMBR, and AnFOMBR were compared using a modified IWA anaerobic digestion model No. 1 (ADM1) in this work. Accumulation of biomass in AnMBR/AnFOMBR results in enhanced biochemical reaction and gains more methane production. AnFOMBR may experience a significant inhibition by accumulated free ammonia and cations, although concentrated soluble substrates rejected by FO membrane are favorable for more methane production. Rejection rate of inorganic nitrogen is a key parameter to determine the inhibition in methane production of AnFOMBR.

摘要

厌氧膜生物反应器 (AnMBR) 采用微滤 (MF) 或超滤 (UF) 膜,可提高传统厌氧消化 (CAD) 中较差的生物质保留率。最近,正向渗透 (FO) 膜已应用于 AnMBR,称为 AnFOMBR。FO 膜不仅确保了高生物质保留率,而且还确保了对低分子量 (LMW) 物质的高去除效率。本工作采用改进的 IWA 厌氧消化模型 1 (ADM1) 比较了 CAD、AnMBR 和 AnFOMBR 中的甲烷产率。在 AnMBR/AnFOMBR 中,生物质的积累增强了生化反应,从而获得更多的甲烷产量。尽管 FO 膜截留的浓缩可溶性底物有利于更多的甲烷生成,但积累的游离氨和阳离子可能会使 AnFOMBR 受到显著抑制。无机氮的去除率是决定 AnFOMBR 甲烷产量抑制的关键参数。

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