11-18A process scheme has been presented for
treating the waste stream originating from bio-gas generation unit of
distillery waste by wet oxidation after thermal pretreatment for membrane process.
The objective was not only to make the stream suitable to meet futuristic standards
but also to produce acetic acid. The pretreatment can achieve a 40% reduction
in COD with 30% color reduction. The wet oxidation of pretreated waste was
studied in the range of 180-225°C and oxygen partial pressure 0.69-1.38 MPa. Kinetic
studies were performed with and without catalyst. The overall kinetics of
distillery waste obeyed a two step mechanism namely, the fast oxidation of
organic substrate followed by slower oxidation of low molecular
weight compounds formed such as acetic
acid. Homogeneous ferrous sulfate is found to be a suitable catalyst to treat the
waste effectively, which increases the performance of wet oxidation. While
noncatalytic wet oxidation at 220°C achieved a 60% reduction in COD during 120
mins with 95% color destruction, catalytic wet oxidation achieved this at 210°C.
Catalytic .wet oxidation with FeS04
increases acetic acid formation. Also, addition of trace amount of hydroquinone
significantly increased the acid formation alongwith enhanced rates of COD destruction