braulium
Chemical
- Aug 20, 2008
- 3
A two phase (gas / oil/water) separator is discharging a mixture of oil and water of 68% WC through 40 metres of 10"diam pipe to a tank that is 5.5 mts above the separator level.
Liquid (oil/water) 20°C/4,5 kg/cm2
I ´ve calculated a 68 kPa (0.69 kg/cm2) total pressure drop for this line, 1.73 kg/cm2 / 100 m.
The recommended pressure drop is < 0.45 (kg/cm2 / 100 m)
the velocity is 1.3 m/s (1.2 - 2 m/s recommended)
I´ve tried larger pipe diameters with the following results
14" - 66 kPa
20" - 65 kPa
The question is ¿how can i support the design of this pipe when the pressure drop is still exceding the permissible limits for 20" diameter?
Liquid (oil/water) 20°C/4,5 kg/cm2
I ´ve calculated a 68 kPa (0.69 kg/cm2) total pressure drop for this line, 1.73 kg/cm2 / 100 m.
The recommended pressure drop is < 0.45 (kg/cm2 / 100 m)
the velocity is 1.3 m/s (1.2 - 2 m/s recommended)
I´ve tried larger pipe diameters with the following results
14" - 66 kPa
20" - 65 kPa
The question is ¿how can i support the design of this pipe when the pressure drop is still exceding the permissible limits for 20" diameter?