Methane Production from Rice Straw Hydrolysate Treated with Dilute Acid by Anaerobic Granular Sludge

被引:10
|
作者
Cheng, Jing-Rong [1 ,2 ]
Liu, Xue-Ming [1 ]
Chen, Zhi-Yi [1 ]
机构
[1] Minist Agr, Guangdong Key Lab Agr Prod Proc, Sericultural & Agrifood Res Inst, Guangdong Acad Agr Sci,Key Lab Funct Foods, Guangzhou 510610, Guangdong, Peoples R China
[2] Chinese Acad Sci, Guangzhou Inst Energy Convers, 133 Yihenglu, Guangzhou 510640, Guangdong, Peoples R China
关键词
Methane production; Granular sludge; DSARSH; Sulfate; Anaerobic digestion; SULFATE REDUCTION; DIGESTION PROCESS; START-UP; WATER; EFFLUENT; HYDROGEN; REMOVAL; AMMONIA; ETHANOL; ENERGY;
D O I
10.1007/s12010-015-1854-1
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
The traditional anaerobic digestion process of straw to biogas faces bottlenecks of long anaerobic digestion time, low digestion rate, less gas production, etc., while straw hydrolysate has the potential to overcome these drawbacks. In this study, the dilute sulphuric acid-treated hydrolysate of rice straw (DSARSH) containing high sulfate was firstly proved to be a feasible substrate for methane production under mesophilic digestion by granular sludge within a short digestion time. Batch anaerobic digestion process was operated under different initial chemical oxygen demand (COD) values at temperature of 37 A degrees C with the pH of 8.5. Among the initial COD values ranging from 3000 to 11,000 mg/L, 5000 mg/L was proved to be the most appropriate considering high COD removal efficiency (94.17 A +/- 1.67 %), CH4 content (65.52 A +/- 3.12 %), and CH4 yield (0.346 A +/- 0.008 L-CH4/g COD (removed)) within 120 h. Furthermore, when the studied system operated at the initial COD of 5000 mg/L, the sulfate removal ratio could reach 56.28 %.
引用
收藏
页码:9 / 20
页数:12
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