dc.description.abstract |
Anaerobic digestion of agricultural, industrial and municipal wastes has a great
relevance in the global renewable energy scenario, since it combines waste stablisation
with net fuel production. RME is a low strength, high volume waste for which anaerobic
treatment can be economically and technologically made feasible by adopting high rate
processes. Hence, an investigation was taken up to develop an anaerobic high rate reactor
for biomethanation of RME.
It was revealed that the RME had a low pH along with high BOD and COD. The batch
digestion studies proved that it is amenable to anaerobic digestion. The semi-continuous studies
to test media compatibility could reveal that the reactor could be feed with RME without prior
neutralisation. The study established the compatibility and suitability of rubber seed outer
shells as packing media in high rate reactors and hence this was selected to be used in
Up-flow Anaerobic Hybrid Reactors (UAHRs).
Eight lab scale UAHRs were designed and fabricated, with two different media
for immobilization viz. polyurethane rings and rubber seed outer shell. The daily feeding
in the reactors were started from the 25 th day after initial charging and operated for 31
days, with a startup HRT of 10 day.
The UAHRs were then operated at HRTs of 10, 5, 4 ,3 , 2, 1 and 0.8 day and the
performance evaluated. All reactors were stable in operation and exhibited high process
efficiency characterised by good organic reduction and biogas production. This was due
to the high degree of cell immobilisation obtained in the hybrid design. The performance
deteriorated with reduction in HRT. The methane content of the biogas remained fairly
high (60-65 per cent) during the above period with a near neutral effluent pH (7.7 t0 7.8).
The reactor performance models showed a high degree of fit within the ranges of loading
rates investigated. The major parameter which affected reactor performances was HLR,
which is a function of HRT.
The maximum loading rate and volumetric gas production (at 0.8 day HRT) were
2.2 kg/m 3 .d and 855 l/m 3 (Reactor 1). The maximum specific gas production was 858.2
l/kg TS observed in Reactor 2 at 10 day HRT. The BOD reduction had the maximumvalue of 82.9 per cent at 10 day HRT in R 2 and the minimum reduction was on the 0.8
day HRT during which 77.1 per cent reduction was obtained for all reactors.
The UAHR was found to be appropriate in energy conversion of RME and 20
MJ/m3 of energy could be produced as biogas by operating the bioreactor at 2 day HRT,
simultaneously reducing the pollution load of RME considerably (81 per cent BOD
reduction). A HRT of 2 day was found optimum for moderate biogas production. An
aerobic polishing treatment would be required to meet the effluent standards prescribed
by the pollution control board. The overall performance of the reactor with rubber seed
outer shell media was found to be significantly better than the polyurethane media
reactor, possibly due to the enhanced microbial attachment on the more favorable surface. |
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