Oh You-Kwan, Kim Seo Hyoung, Kim Mi-Sun, Park Sunghoon
Department of Chemical Engineering, Pusan National University, Pusan 609-735, South Korea.
Biotechnol Bioeng. 2004 Dec 20;88(6):690-8. doi: 10.1002/bit.20269.
Thermophilic H2 production from glucose was studied at 55-64 degrees C for 234 days using a continuous trickling biofilter reactor (TBR) packed with a fibrous support matrix. Important parameters investigated included pH, temperature, hydraulic retention time (HRT), and glucose concentration in the feed. The optimal pH and temperature were 5.5 and 60 degrees C, respectively. With decreasing HRT or increasing inlet glucose concentration, volumetric H2 production rate increased but the H2 production yield to glucose decreased gradually. The biogas composition was almost constant at 53 +/- 4% (v/v) of H2 and 47 +/- 4% (v/v) of CO2. No appreciable CH4 was detected when the reactor was under a normal operation. The carbon mass balance showed that, in addition to cell mass, lactate, n-butyrate, CO2, and acetate were major products that comprised more than 85% of the carbon consumed. The maximal volumetric H2 production rate and H2 yield to glucose were 1,050 +/- 63 mmol H2/l.d and 1.11 +/- 0.12 mol H2/mol glucose, respectively. These results indicate that the thermophilic TBR is superior to most suspended or immobilized reactor systems reported thus far. This is the first report on continuous H2 production by a thermophilic TBR system.
使用填充有纤维支撑基质的连续滴流生物滤池反应器(TBR),在55 - 64摄氏度下对葡萄糖嗜热产氢进行了234天的研究。研究的重要参数包括pH值、温度、水力停留时间(HRT)和进料中的葡萄糖浓度。最佳pH值和温度分别为5.5和60摄氏度。随着HRT的降低或进料中葡萄糖浓度的增加,氢气的体积产率增加,但氢气对葡萄糖的产率逐渐降低。沼气组成几乎恒定,氢气含量为53±4%(v/v),二氧化碳含量为47±4%(v/v)。反应器正常运行时未检测到明显的甲烷。碳质量平衡表明,除细胞物质外,乳酸、正丁酸、二氧化碳和乙酸是主要产物,占消耗碳的85%以上。氢气的最大体积产率和氢气对葡萄糖的产率分别为1050±63 mmol H2/l·d和1.11±0.12 mol H2/mol葡萄糖。这些结果表明,嗜热TBR优于迄今为止报道的大多数悬浮或固定化反应器系统。这是关于嗜热TBR系统连续产氢的首次报道。