bmw318be
Mechanical
- Jun 16, 2010
- 197
Hi,
I would like to understand the impact of selecting Accessories which is smaller in Port size than the Discharge Piping.
We are having a metering Pump which is 3" Discharge port, intend to downsize the pipe to 2", I believe this would increase the design pressure of the pump. Evaluating the system pressure it is still within the rated pressure of the pump.
Typical installation
Details is as followed:
Pulsation Dampener, Understand the there is formula to calculate the Minimum volume requirement of the metering pump based on this variables
(𝑉 𝑥 𝐾 (𝑃/𝑃_𝑚𝑖𝑛 )^𝑛)/〖1−(𝑃/𝑃_𝑚𝑎𝑥 )〗^𝑛
My Metering pump Parameter are as followed
CLIENT PARAMETER
Item Liquid Flow Discharge Temp SPM (Sroke Per Min)
LPH Bar DegC
1 NaOCl 8000 7 30 180
2 1300 10 30 96
Item V K P Residual Pulsation Level Pmin Pmax n
PSI PSI PSI
1 45.20 0.6 101.5 5% 96.425 106.58 1
2 14.83 0.6 145 5% 137.75 152.25 1
V=Volume per pump stroke in cubic inches
P=Mean operating pressure
D=Allowable pressure fluctuations as a percentage. Plus and Minus
n=Polytropic exponent of gas expansion. (Nitrogen=0.714, Air=1.0)
MIN REQUIRED VOL SELECTED Cubic Inch Capacity Required L Cubic Inch Capacity L
599.5 9.8 732.3 12.00
182.7 3 175.0 3
What would be the impact if we use a smaller port of dampener:
1. Item 1, Pipe discharge is 3" and I am considering 2" with sufficient Volume of 12 L
2. Item 2, Pipe discharge is 2" and I am considering 3/4" with sufficient Volume of 3 L
I am going to use adapter from 3" to 2" and 2" to 3/4" .
For the Back Pressure valve:
1. For item 1, Is it feasible if we are using 2" on the pipe discharge of 3" for item 1 having calculated the sufficient flow able to pass though
2. For item 1, Is it feasible if we are using 3/4" on the pipe discharge of 2" for item 1 having calculated the sufficient flow able to pass though
Is back pressure valve shall be the same sie as the pipe discharge, what is the minimum size that it is ensure good practice for selection ?
Appreciate if anyone could share their tips to optimize the selection
I would like to understand the impact of selecting Accessories which is smaller in Port size than the Discharge Piping.
We are having a metering Pump which is 3" Discharge port, intend to downsize the pipe to 2", I believe this would increase the design pressure of the pump. Evaluating the system pressure it is still within the rated pressure of the pump.
Typical installation
Details is as followed:
Pulsation Dampener, Understand the there is formula to calculate the Minimum volume requirement of the metering pump based on this variables
(𝑉 𝑥 𝐾 (𝑃/𝑃_𝑚𝑖𝑛 )^𝑛)/〖1−(𝑃/𝑃_𝑚𝑎𝑥 )〗^𝑛
My Metering pump Parameter are as followed
CLIENT PARAMETER
Item Liquid Flow Discharge Temp SPM (Sroke Per Min)
LPH Bar DegC
1 NaOCl 8000 7 30 180
2 1300 10 30 96
Item V K P Residual Pulsation Level Pmin Pmax n
PSI PSI PSI
1 45.20 0.6 101.5 5% 96.425 106.58 1
2 14.83 0.6 145 5% 137.75 152.25 1
V=Volume per pump stroke in cubic inches
P=Mean operating pressure
D=Allowable pressure fluctuations as a percentage. Plus and Minus
n=Polytropic exponent of gas expansion. (Nitrogen=0.714, Air=1.0)
MIN REQUIRED VOL SELECTED Cubic Inch Capacity Required L Cubic Inch Capacity L
599.5 9.8 732.3 12.00
182.7 3 175.0 3
What would be the impact if we use a smaller port of dampener:
1. Item 1, Pipe discharge is 3" and I am considering 2" with sufficient Volume of 12 L
2. Item 2, Pipe discharge is 2" and I am considering 3/4" with sufficient Volume of 3 L
I am going to use adapter from 3" to 2" and 2" to 3/4" .
For the Back Pressure valve:
1. For item 1, Is it feasible if we are using 2" on the pipe discharge of 3" for item 1 having calculated the sufficient flow able to pass though
2. For item 1, Is it feasible if we are using 3/4" on the pipe discharge of 2" for item 1 having calculated the sufficient flow able to pass though
Is back pressure valve shall be the same sie as the pipe discharge, what is the minimum size that it is ensure good practice for selection ?
Appreciate if anyone could share their tips to optimize the selection