BZLAM21
Petroleum
- Aug 12, 2020
- 60
Dear Members
I am new pipeline designer Please help me on Benzene unloading pipeline design technologies ,I am also confused about steam tracing or electric tracing,
Project requirement : 4'' diameter pipeline / total = 4 km / delivery to storage tank.
Benzene Specification : Density = 884 kg/m3 / Viscosity = 0.5 cP / Operating temperature = 38 °C freezing point : 6 °C
Suction pressure = -0.1 bar g ; Discharge pressure = 8 bar g ; ;
Flow rate:20 m3
Vapour pressure: 0.03 bar abs
MDMT: 1°c
WIND SPEED : 12 m /s
MP steam : 12 barg and 210 °C
LP steam : 4.5 barg and 160 °C
Electrical power available
Question ??
a) What is the best way for benzene line heat tracing
b) How to calculate and determine if a 4'' diameter pipeline needed insulation or not?
c) How to flush and clean the benzene left inside the pipeline after loading is complete.
I don't know if it is enough to leave the pipeline with full Bnezene or clean it and the pipeline is empty and clean? What is the best solution?
Merci d’avance.
I am new pipeline designer Please help me on Benzene unloading pipeline design technologies ,I am also confused about steam tracing or electric tracing,
Project requirement : 4'' diameter pipeline / total = 4 km / delivery to storage tank.
Benzene Specification : Density = 884 kg/m3 / Viscosity = 0.5 cP / Operating temperature = 38 °C freezing point : 6 °C
Suction pressure = -0.1 bar g ; Discharge pressure = 8 bar g ; ;
Flow rate:20 m3
Vapour pressure: 0.03 bar abs
MDMT: 1°c
WIND SPEED : 12 m /s
MP steam : 12 barg and 210 °C
LP steam : 4.5 barg and 160 °C
Electrical power available
Question ??
a) What is the best way for benzene line heat tracing
b) How to calculate and determine if a 4'' diameter pipeline needed insulation or not?
c) How to flush and clean the benzene left inside the pipeline after loading is complete.
I don't know if it is enough to leave the pipeline with full Bnezene or clean it and the pipeline is empty and clean? What is the best solution?
Merci d’avance.