ANAEROBIC CO-DIGESTION OF CRUDE GLYCERIN AND STARCH INDUSTRY EFFLUENT

被引:15
作者
Larsen, Andrea C. [1 ]
Gomes, Benedito M. [1 ]
Gomes, Simone D. [1 ]
Zenatti, Dilcemara C. [1 ]
Torres, Douglas G. B. [1 ]
机构
[1] Univ Fed Parana UFPR, Curso Super Tecnol Biocombustiveis, Maringa, Parana, Brazil
来源
ENGENHARIA AGRICOLA | 2013年 / 33卷 / 02期
关键词
cassava wastewater; biodiesel; biogas; glycerol; WASTE-WATER; REACTOR;
D O I
10.1590/S0100-69162013000200013
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
The Brazil's Biodiesel Production and Use Program introduces biodiesel in the Brazilian energy matrix, bringing along the perspective of a growth of the glycerin offer, co-product generated in the proportion of 10 kg for each 100 L of biodiesel. The aim of this study was to evaluate the addition of crude glycerin in the anaerobic digestion of cassava starch industry effluent (cassava wastewater), in a horizontal semi-continuous flow reactor of one phase in laboratory scale. It was used a reactor with a 8.77 L of useful volume, a medium support for corrugated conduit of polyvinyl chloride (PVC), temperature of 26 +/- 1 degrees C, fed with cassava wastewater and glycerin, with hydraulic detention times of 4 and 5 days and increasing volumetric organic load of 3.05; 9.32; 14.83 and 13.59 g COD L-1 d(-1), obtained with the addition of glycerin at 0; 2; 3 and 2% (v/v), respectively. The average removal efficiencies of TS and TVS were decreasing from the addition of glycerin to the cassava wastewater, averaging 81.19 to 55.58% for TS and 90.21 to 61.45% for TVS. The addition of glycerin at 2% increased the biogas production compared to the control treatment, reaching 1.979 L L-1 d(-1). The biogas production as a function of the consumed COD was higher for the control treatment than for the treatments with addition of glycerin, which indicates lower conversion of organic matter into biogas.
引用
收藏
页码:341 / 352
页数:12
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