Quentin
Bioengineer
- Jun 5, 2003
- 9
I have been assigned to a project involving the neutralising of high pH spikes in our plant effluent.
The effluent currently flows at up to 80 litres/sec (avg 30 litres/sec) in a 8" galvanised pipe from a contrashear pit (solids removal) via a buffer tank to a DAF (dissolved air flotation) unit.
I am considering installing a 8" static mixer in the pipeline just prior to the DAF, with a 50% (or 98%)sulphuric acid dosing point immediately prior to the mixer, and a pH probe just after.
I am concerned about localised high concentrations of corrosive acid in and around the injection point (even though we are neutralising to pH 6 - 8) as well as through the static mixer, and so am wondering if I need to replace the pipework around this area and consider use of exotic stainless steels or plastic as the mixer's material of construction?
Quentin
The effluent currently flows at up to 80 litres/sec (avg 30 litres/sec) in a 8" galvanised pipe from a contrashear pit (solids removal) via a buffer tank to a DAF (dissolved air flotation) unit.
I am considering installing a 8" static mixer in the pipeline just prior to the DAF, with a 50% (or 98%)sulphuric acid dosing point immediately prior to the mixer, and a pH probe just after.
I am concerned about localised high concentrations of corrosive acid in and around the injection point (even though we are neutralising to pH 6 - 8) as well as through the static mixer, and so am wondering if I need to replace the pipework around this area and consider use of exotic stainless steels or plastic as the mixer's material of construction?
Quentin