Jafka
Chemical
- Mar 9, 2011
- 10
I've always set the design temperature of piping and equipment downstream of a cooler is based on the normal operating temperature upstream of said cooler.
e.g. Cooler E-201 reduces the temperature of a gas from 200F to 80F. All downstream piping should be designed for 200F + a design factor.
Does anyone know if there's a source of this practice that I can reference? (design guidelines, ASME, company standards, etc).
Thanks!
e.g. Cooler E-201 reduces the temperature of a gas from 200F to 80F. All downstream piping should be designed for 200F + a design factor.
Does anyone know if there's a source of this practice that I can reference? (design guidelines, ASME, company standards, etc).
Thanks!