Heat Exchanger Steam Valve Sizing
Heat Exchanger Steam Valve Sizing
(OP)
I have a question concerning control valve sizing (pressure drop assumptions) for a heat exchanger. It comes down to what pressure drop do you assume. The HX manufacturer says they don't size valves. Here is what I think should be done.
(1) - Determine the condensate loading and the pressure required to evacuate the condensate.
(2) - With this information take the maximum pressure drop possible across the valve. (ie supply press = 150 psi, required pressure for condensate removal = 10 psi, therefore the pressure drop at rated flow should be 140 psi)
(3) - I think this is important because it minimizes the valve size and a large pressure drop allows the condensate line to be sized smaller becuase there is less flashing & 2 phase flow.
I'm thinking that a smaller pressure drop (ie 15 psi) would pressurize the heat exchanger shell to 135 psi. To evacuate the condensate to an atmospheric tank would require ~ 4" line compared to something smaller if the shell pressure was reduced.
On the other hand, there could be a problem with vlave life by taking such a large pressure drop across the valve.
Feedback requested!
(1) - Determine the condensate loading and the pressure required to evacuate the condensate.
(2) - With this information take the maximum pressure drop possible across the valve. (ie supply press = 150 psi, required pressure for condensate removal = 10 psi, therefore the pressure drop at rated flow should be 140 psi)
(3) - I think this is important because it minimizes the valve size and a large pressure drop allows the condensate line to be sized smaller becuase there is less flashing & 2 phase flow.
I'm thinking that a smaller pressure drop (ie 15 psi) would pressurize the heat exchanger shell to 135 psi. To evacuate the condensate to an atmospheric tank would require ~ 4" line compared to something smaller if the shell pressure was reduced.
On the other hand, there could be a problem with vlave life by taking such a large pressure drop across the valve.
Feedback requested!
RE: Heat Exchanger Steam Valve Sizing
It is best to avoid choked (sonic) flow across a control valve where possible. For steam (k=1.3) the critical pressure ratio for choked flow is 1.83:1. In your application, this translates to keeping the steam pressure on the shell above 75 PSIG.
If the heat exchanger design is already finalized, then it will require a certain minimum pressure to meet your heat load requirement. You really are only free to play with the steam pressure on the shell if you are still in the design stage for the heat exchanger. A higher pressure on the shell will result in a smaller cheaper exchanger.
You are correct in stating that the condensate line can be rather large when high pressure steam is used. When sized for the flash steam velocity, it often ends up being larger diameter than the high pressure steam supply line.
RE: Heat Exchanger Steam Valve Sizing
Forgive my ignorance, but what does LMDT stand for?
Yes the system is designed and installed, but I always go back and evaluate how it is working. Its easy when you can trend the variables with the DCS.
My findings are:
(1) - As you mentioned, I would take more pressure drop across the valve.
(2) - The design numbers, which were given to me for sizing, were coservative.
The above factors contribute to a average control valve opening of 25% instead of 50%-60% which I would like to see.
RE: Heat Exchanger Steam Valve Sizing
RE: Heat Exchanger Steam Valve Sizing
Consider installing a flow switch in the liquid flow, tied back to the TCV. I've seen pumps fail, or get shut off, where the sensor for the TCV is in the outlet piping from the HX. The liquid surrounding the sensor is cool enough that it keeps calling for steam. Meanwhile, the liquid temp inside the HX is off the scale.
Remember to install a properly sized & rated relief valve on the liquid side of the HX, if it can be isolated, or is in a closed system. Steam valves leaking-by, or a control failure can have energy being added to a system with no load to take it away. This can result in HUGE pressures. This is a particular problem with the increased use of backflow prevention devices. The water side used to be able to expand back into the plant or municipal water systems. Now it can't. I've seen HXs fail because of this.