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Coupled high solids fermentation and anaerobic filtration of cellulosic residues

Thesis/Dissertation ·
OSTI ID:5218535
A coupled high solids fermentation and attached-growth anaerobic filtration process to produce methane from cellulosic residues was developed and successfully operated for 18 months using wheat straw as the substrate. The process was conducted in eight 600 ml packed reactors and two anaerobic filters connected in series allowing semi-continuous feeding of straw at a solids concentration of 34%. The major functions of the packed reactors were the hydrolysis of the solid substrate and the production of organic acids. The volatile fatty acid COD, composed mostly by acetic, propionic, and butyric acids, was produced at a slower rate than soluble COD in the packed reactors. Specific methane production rates as high as 2.1 liter CH/sub 4/ per day per liter reactor volume and a volatile fatty acid COD removal efficiency of 98% were obtained. Total methane production per unit weight of substrate input was 104.3 ml CH/sub 4/ per gram of straw input with 40 days substrate solids retention time and 76.3 ml CH/sub 4//g straw with 18 days solids retention time. Results of a direct input study, without the liquid reservoir, suggested that the methanogenic bacteria in the anaerobic filters could sustain methane production during transient loading, although the suddenly increased substrate could not be completely utilized on the first pass. A mathematical model of solid substrate degradation in the packed reactor was developed.
Research Organization:
Michigan State Univ., East Lansing (USA)
OSTI ID:
5218535
Country of Publication:
United States
Language:
English