- #1
matthew_hanco
- 19
- 0
Orifice problem I've been given a list of quantities
Pipe before orifice head = 255mm
Diameter = 31.75mm
Pipe after orifice head = 230mm
Diameter= 20mm
Time for 10litres to fill in collection tank 67.09seconds
Assuming g= 9.81 and density = 1000
from the experiment difference in pressure head = 25mm
They wanted to know the theorectical.
Calling everything before head 1 and after head 2
u1= Q/ A where Q= 0.149 x 10^-3 m^3/s and A = 0.791x10^-3 m^2
u1 = 0.188
u2= Q/ A where Q= 0.149 x 10^-3 m^3/s and A =0.314x 10^-3 m^2
u2= 0.475
putting into equaton
P1-P2/p x g = u2^2/2g - u1^2/2g where p=density
gives the difference in theoretical head = 9.7mm
Im not sure if that is right as its a third of the experiment, if it is right how can it be because surely the theory should be higher as you don't take into account the local or frictional losses.
Hope someone can help.
Pipe before orifice head = 255mm
Diameter = 31.75mm
Pipe after orifice head = 230mm
Diameter= 20mm
Time for 10litres to fill in collection tank 67.09seconds
Assuming g= 9.81 and density = 1000
from the experiment difference in pressure head = 25mm
They wanted to know the theorectical.
Calling everything before head 1 and after head 2
u1= Q/ A where Q= 0.149 x 10^-3 m^3/s and A = 0.791x10^-3 m^2
u1 = 0.188
u2= Q/ A where Q= 0.149 x 10^-3 m^3/s and A =0.314x 10^-3 m^2
u2= 0.475
putting into equaton
P1-P2/p x g = u2^2/2g - u1^2/2g where p=density
gives the difference in theoretical head = 9.7mm
Im not sure if that is right as its a third of the experiment, if it is right how can it be because surely the theory should be higher as you don't take into account the local or frictional losses.
Hope someone can help.