Environmental Engineering Reference
In-Depth Information
%LRJDVSURGXFWLRQ
/
&+
&2
+ 6
SSP
1+
SSP
&+
&2
(IIOXHQW/
&2' ˖ J/
76 ˖ F
796 ˖ F
,QIOXHQW/
&2' ˖ J/
76 ˖ F
796 ˖ F
$PPRQLDVWULSSHGFKLFNHQPDQXUH
7KHUPRSKLOLFIHUPHQWDWLRQ
+57GD\
7HPSHUDWXUH
(IIHFWYROXPH ˖ /
S+ ˖ F
S+ ˖ F
° F
%LRJDVSURGXFWLRQ
/
&+
&2
+ 6
SSP
1+
SSP
&+
&2
(IIOXHQW/
&2' ˖ J/
76 ˖ F
796 ˖ F
,QIOXHQW/
&2' ˖ J/
76 ˖ F
796 ˖ F
5DZFKLFNHQPDQXUH
7KHUPRSKLOLFIHUPHQWDWLRQ
+57GD\
7HPSHUDWXUH
(IIHFWYROXPH ˖ /
S+ ˖ F
S+ ˖ F
° F
Fig. 8.15 Average performance of the thermophilic methane fermentation on ammonia-stripped
CM and raw CM
The mean conditions for all 305 methanogenic plants operated in Japan are as
shown in Fig. 8.17 . The average gas composition was 60 % methane (36 % of CO 2
and 1164 ppm of H 2 S) and the average biogas yield was 11m 3 of gas per m 3 of
sludge processed. Average TS and VS reductions were 51 % and 57 % respectively.
The average pH in the digesters remained stable throughout the year at ~ 7.25. TS,
VS and COD reductions were 44.2, 54.2 and 60 % respectively. Biogas production
magnification ranged from 20 to 30, which was twice the average values of other
waste water treatment plants (WWTP) in Japan.
8.4.6
Co-Digestion
Anaerobic digestion can also be applied to wastes from different sources in a co-
digestion process. One example of biomass utilization based on both animal waste
Search WWH ::




Custom Search