farhadsh
Mechanical
- Mar 30, 2015
- 43
Hi,
I have a question about EJ used on piping and appreciate any feedback on it.
My piping is connected to lube oil filter from one end and to heat exchanger from other side. It is elbow and loops on it to add flexibility. It is water cooled heat exchanger and plate type. for simplicity assume a very simple system. Allowable nozzle loads on H.E is very low. Installation temperature and max oil temperature are 20 and 60C respectively. I have constraints and can not add any pipe support to piping between two equipment. I can not modify pipe model and add extra flexibility or loop if needed.
While modeling piping in Caesar it meets the stress code but nozzle loads on H.E goes beyond allowable loads. when load case is sustained load plus thermal expansion load the H.E loads will become 2x or 3x of allowable. So I decided to use EJ with tie-rod.
I assumed piping first see pressure then thermal expansion. when piping is under pressure EJ will try to expand due to thrust while tie-rod prevent from expansion. so in this case there is no extra force on H.E nozzle.
when piping temperature increases, piping thermal displacement pushes the EJ to compress but since in my case thrust is greater than thermal force it won't let the EJ to compress and so thermal displacement will add extra force to H.E nozzle. the extra force is equal to thermal displacement force.
It appears using EJ is not going to help piping system or to lower the nozzle loads on equipment
Am I right about this?
Is this valid for EJ when piping sees thermal expansion?
Is the solution to put EJ with tie-rod perpendicular to line?
Thank you,
I have a question about EJ used on piping and appreciate any feedback on it.
My piping is connected to lube oil filter from one end and to heat exchanger from other side. It is elbow and loops on it to add flexibility. It is water cooled heat exchanger and plate type. for simplicity assume a very simple system. Allowable nozzle loads on H.E is very low. Installation temperature and max oil temperature are 20 and 60C respectively. I have constraints and can not add any pipe support to piping between two equipment. I can not modify pipe model and add extra flexibility or loop if needed.
While modeling piping in Caesar it meets the stress code but nozzle loads on H.E goes beyond allowable loads. when load case is sustained load plus thermal expansion load the H.E loads will become 2x or 3x of allowable. So I decided to use EJ with tie-rod.
I assumed piping first see pressure then thermal expansion. when piping is under pressure EJ will try to expand due to thrust while tie-rod prevent from expansion. so in this case there is no extra force on H.E nozzle.
when piping temperature increases, piping thermal displacement pushes the EJ to compress but since in my case thrust is greater than thermal force it won't let the EJ to compress and so thermal displacement will add extra force to H.E nozzle. the extra force is equal to thermal displacement force.
It appears using EJ is not going to help piping system or to lower the nozzle loads on equipment
Am I right about this?
Is this valid for EJ when piping sees thermal expansion?
Is the solution to put EJ with tie-rod perpendicular to line?
Thank you,