Direct fermentation of Laminaria japonica for biohydrogen production by anaerobic mixed cultures

被引:72
|
作者
Shi, Xueqing [1 ]
Jung, Kyung-Won [1 ]
Kim, Dong-Hoon [2 ]
Ahn, Yong-Tae [3 ]
Shin, Hang-Sik [1 ]
机构
[1] Korea Adv Inst Sci & Technol, Dept Civil & Environm Engn, Taejon 305701, South Korea
[2] Korea Inst Energy Res, Wastes Energy Res Ctr, Taejon 305343, South Korea
[3] Penn State Univ, Dept Civil & Environm Engn, University Pk, PA 16802 USA
关键词
Fermentative hydrogen production; Laminaria japonica; ASBR; Methane; HYDROGEN-PRODUCTION; CORNSTALK WASTES; BIOMASS; BATCH; TEMPERATURE; PH;
D O I
10.1016/j.ijhydene.2011.01.125
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
A few studies have been made on fermentative hydrogen production from marine algae, despite of their advantages compared with other biomass substrates. In this study, fermentative hydrogen production from Laminaria japonica (one brown algae species) was investigated under mesophilic condition (35 +/- 1 degrees C) without any pretreatment method. A feasibility test was first conducted through a series of batch cultivations, and 0.92 mol H-2/mol hexose(added), or 71.4 ml H-2/g TS of hydrogen yield was achieved at a substrate concentration of 20 g COD/L (based on carbohydrate), initial pH of 7.5, and cultivation pH of 5.5. Continuous operation for a period of 80 days was then carried out using anaerobic sequencing batch reactor (ASBR) with a hydraulic retention time (HRT) of 6 days. After operation for approximately 30 days, a stable hydrogen yield of 0.79 +/- 0.03 mol H-2/mol hexoseadded was obtained. To optimize bioenergy recovery from L. japonica, an up-flow anaerobic sludge blanket reactor (UASBr) was applied to treat hydrogen fermentation effluent (HFE) for methane production. A maximum methane yield of 309 +/- 12 ml CH4/g COD was achieved during the 90 days operation period, where the organic loading rate (OLR) was 3.5 g COD/L/d. Copyright (C) 2011, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:5857 / 5864
页数:8
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