chemebabak
Chemical
- Feb 8, 2011
- 100
What is a method for sizing a surge vessel for compressible fluids? That is, how can a pulsation dampener, surge drum, suction or discharge bottle or any other drum be sized to maintain steady flow of a compressible fluid?
Our process requires X SCFM flow of gas at temperature T and pressure P. Due to the actual conditions of the process, X flow rate varies by ~25% and P by ~10%. The downstream conditions of the gas require steady flow rate.
Actual volume can be calculated by converting from SCFM compensating for compressiblity, temperature and pressure. Does the procedure for calculating surge volume require calculating a volume for the excess gas flow? That is, the actual flow for normal flow conditions is NC ACFM. The actual flow for conditions 1 and 2 is C1 and C2, respectively. Would the surge volume be calculated as
A. SV = C2 - C1;
B. SV = maximum ( absolute(C2-NC), absolute(C1-NC) ); or
C. SV = absolute( maximum(C1, C2) - NC )?
Our process requires X SCFM flow of gas at temperature T and pressure P. Due to the actual conditions of the process, X flow rate varies by ~25% and P by ~10%. The downstream conditions of the gas require steady flow rate.
Actual volume can be calculated by converting from SCFM compensating for compressiblity, temperature and pressure. Does the procedure for calculating surge volume require calculating a volume for the excess gas flow? That is, the actual flow for normal flow conditions is NC ACFM. The actual flow for conditions 1 and 2 is C1 and C2, respectively. Would the surge volume be calculated as
A. SV = C2 - C1;
B. SV = maximum ( absolute(C2-NC), absolute(C1-NC) ); or
C. SV = absolute( maximum(C1, C2) - NC )?