Biohydrogen production from diluted-acid hydrolysate of rice straw in a continuous anaerobic packed bed biofilm reactor

被引:17
作者
Safari, Mohammad [1 ]
Tondro, Hadiseh [1 ]
Zilouei, Hamid [1 ]
机构
[1] Isfahan Univ Technol, Dept Chem Engn, Esfahan 8415683111, Iran
关键词
Dark fermentation; Bio-hydrogen; Anaerobic packed bed biofilm; reactor; Hydraulic retention time; Two-stage hydrolysis; FERMENTATIVE HYDROGEN-PRODUCTION; HYDRAULIC RETENTION TIME; ORGANIC LOADING RATE; DARK FERMENTATION; FLUIDIZED-BED; WASTE-WATER; PRETREATMENT; BIOMASS; SLUDGE; HOMOACETOGENESIS;
D O I
10.1016/j.ijhydene.2021.11.222
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
Bio-hydrogen production in a continuously operated anaerobic packed bed biofilm reactor (APBR) using acid-hydrolysate of rice straw as feedstock and inoculated with an anaerobic mesophilic sludge from a municipal wastewater treatment plant was investigated at three different HRTs (17, 8.2 and 2 h). Fermentable sugars solution achieved from a two-stage diluted acid hydrolysis of rice straw was used as the feedstock. First, rice straw was treated with 1% w v-1 sulfuric acid at 120 degrees C for 30 min with a yield of 58.5% xylose. Higher temperature of 180 degrees C for 10 min at 0.5% w v-1 sulfuric acid was applied in the second stage in which cellulosic crystalline structure was partially depolymerized to glucose with a yield of 19.3% glucose. Hydrogen production rate and yield were enhanced as the hydraulic retention time was decreased with a maximum production rate of 252 mL L-1 h-1 and yield of 1 mol H2 mol-1 sugar consumed at 2 h HRT. Experimental results illustrated the increase of COD conversion from 44% to 47% by shortening the HRT from 17 to 2 h. Furthermore, acetic acid and butyric acid production were reduced slower than other soluble metabolites like ethanol.
引用
收藏
页码:5879 / 5890
页数:12
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