I am seeking feedback on the operational management of petrol-diesel transmix in pipelines. My challenge is to reduce the volume of the mixture recovered in the tank to avoid large-scale downgrading or the need to send it back for re-distillation.
Given the non-linear drop in the flash point of diesel as soon as the first traces of petrol are present, what are your best practices for:
Defining the physical cut-off points to minimise the volume sent to the slop tank without contaminating the main batch?
The actual effectiveness of kerosene buffer batches in segregating the interface?
The maximum blending ratios you have been able to validate (via Pensky-Martens tests) when reinjecting these contaminants into compliant diesel?
Given the non-linear drop in the flash point of diesel as soon as the first traces of petrol are present, what are your best practices for:
Defining the physical cut-off points to minimise the volume sent to the slop tank without contaminating the main batch?
The actual effectiveness of kerosene buffer batches in segregating the interface?
The maximum blending ratios you have been able to validate (via Pensky-Martens tests) when reinjecting these contaminants into compliant diesel?