I have a plate heat exchanger with seawater cooling medium. Conventially the control valve is mounted downstream of the heat exchanger (hotside). However the rise in temperature increases the cost of the control valve, due to material specification eg titanium. What are the control challenges/disadvantage when mounting this valve on the upstream side of the exchanger?
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Control valve position for plate heat exchanger
- Thread starter skinflint
- Start date
EdStainless
Materials
Upstream control has some issues.
Will you keep the heat exhanger full of water? Will the reduced pressure harm heat transfer?
I really hate to see reduced flow through heat exchagers used as a control. Recirculation may take more piping, but it is the correct way to control the temp.
= = = = = = = = = = = = = = = = = = = =
Corrosion never sleeps, but it can be managed.
Will you keep the heat exhanger full of water? Will the reduced pressure harm heat transfer?
I really hate to see reduced flow through heat exchagers used as a control. Recirculation may take more piping, but it is the correct way to control the temp.
= = = = = = = = = = = = = = = = = = = =
Corrosion never sleeps, but it can be managed.
As Ed noted keeping the HX full can be a problem. However if you can design the sea water to be bottom entry/top discharge you can put the control valve on the inlet side.
You can still put the CV on the inlet side in a top entry system but you need to make sure you have air vents to bleed the air out of the system and ensure the discharge is higher than the top of the HX.
I have seen CV's on the inlet side of HX's in many applications.
Regarding recirculation- yes it is better (less scaling, lower wall temperature etc.) but not necessary.
The reduced pressure is unlikely to harm the heat transfer.
Cheers.
You can still put the CV on the inlet side in a top entry system but you need to make sure you have air vents to bleed the air out of the system and ensure the discharge is higher than the top of the HX.
I have seen CV's on the inlet side of HX's in many applications.
Regarding recirculation- yes it is better (less scaling, lower wall temperature etc.) but not necessary.
The reduced pressure is unlikely to harm the heat transfer.
Cheers.
The reduced pressure won't affect heat transfer, but the reduced flow will.
Plate hx's don't like reduced flows. The OHTC falls off rapidly when the flow is reduced below the 'sweet spot' that the exchanger is designed for.
Further, if there is any tendancy toward fouling, reduced flow hastens fouling. PHE's depend upon velocity for the 'scrubbing' action in the plates that helps prevent fouling. When the velocity falls enough to reduce the turbulence in the plates, whatever is going to plate out will easily do so.
rmw
Plate hx's don't like reduced flows. The OHTC falls off rapidly when the flow is reduced below the 'sweet spot' that the exchanger is designed for.
Further, if there is any tendancy toward fouling, reduced flow hastens fouling. PHE's depend upon velocity for the 'scrubbing' action in the plates that helps prevent fouling. When the velocity falls enough to reduce the turbulence in the plates, whatever is going to plate out will easily do so.
rmw
Montemayor
Chemical
Skin:
Go to
and read carefully what Walt Driedger recommends as controls for a heat exchanger. Although this article is for a TEMA shell & Tube model, the control logic holds also for a plate exchanger.
Go to
and read carefully what Walt Driedger recommends as controls for a heat exchanger. Although this article is for a TEMA shell & Tube model, the control logic holds also for a plate exchanger.
As the others have pointed out there are many aspects to consider in heat exchanger control, but it seems to me that in this case there are two unique or important factors that require consideration. These are the fact that you are using seawater, and that the exchanger is of the plate type.
I would like to first comment on some of the points already raised. It is almost certain that with careful piping design you can ensure that the water side remains full. As long as your pipers are aware of the requirement it can be addressed.
Recirculation has been raised as a possibility, but you have to consider what you will recirculate. If you recirculate the seawater you will still have a control valve on the hot seawater, plus you will have a large pump probably also made of exotic (expensive) material. ItDepends commented that recirculation of the seawater will give less scaling. The higher velocities will help, but you need to check the temperature effects. He (i.e. ItDepends) also said that recirculation would give lower wall temperatures, but I believe that it would be the opposite. The way recirculation reduces heat transfer is to raise the water temperature, so I think the wall temperatures would actually increase.
Not knowing your process, I may be on the wrong track, but you could also consider recirculating the process side and not controlling the seawater at all. This would result in constant high flowrate and minimum temperature rise on the water side.
RMW said that the reduced flow would reduce the heat transfer. This is the way control valves work and is the desired behavior.
An issue that nobody has raised is the question of equalization of pressures across the plates. I know that modern plate exchangers are rated to hold the design pressures for each pass individually, but I still feel happier without widely different or varying pressures across plates. It's hard to teach an old dog new tricks. Putting the CV on the inlet side will result in wider pressure fluctuations than if it were on the outlet.
As I stated in the beginning of this post, the two important issues are the seawater and the plate exchanger. Again with the caveat of not knowing your process, I would address these issues by not controlling the seawater side (i.e. constant high flow and minimum temp rise) and I would try to get a bypass or recirculation system on the process side that kept the pressure on the process side as constant as possible.
I would like to first comment on some of the points already raised. It is almost certain that with careful piping design you can ensure that the water side remains full. As long as your pipers are aware of the requirement it can be addressed.
Recirculation has been raised as a possibility, but you have to consider what you will recirculate. If you recirculate the seawater you will still have a control valve on the hot seawater, plus you will have a large pump probably also made of exotic (expensive) material. ItDepends commented that recirculation of the seawater will give less scaling. The higher velocities will help, but you need to check the temperature effects. He (i.e. ItDepends) also said that recirculation would give lower wall temperatures, but I believe that it would be the opposite. The way recirculation reduces heat transfer is to raise the water temperature, so I think the wall temperatures would actually increase.
Not knowing your process, I may be on the wrong track, but you could also consider recirculating the process side and not controlling the seawater at all. This would result in constant high flowrate and minimum temperature rise on the water side.
RMW said that the reduced flow would reduce the heat transfer. This is the way control valves work and is the desired behavior.
An issue that nobody has raised is the question of equalization of pressures across the plates. I know that modern plate exchangers are rated to hold the design pressures for each pass individually, but I still feel happier without widely different or varying pressures across plates. It's hard to teach an old dog new tricks. Putting the CV on the inlet side will result in wider pressure fluctuations than if it were on the outlet.
As I stated in the beginning of this post, the two important issues are the seawater and the plate exchanger. Again with the caveat of not knowing your process, I would address these issues by not controlling the seawater side (i.e. constant high flow and minimum temp rise) and I would try to get a bypass or recirculation system on the process side that kept the pressure on the process side as constant as possible.
hello,
why control of the cooling medium? if there are no special conditions or demands let the full flow of the cooling water and control the process side with split flow: part enters the heat exchanger and the other part bypasses the heat exchanger.
regards,
roker
why control of the cooling medium? if there are no special conditions or demands let the full flow of the cooling water and control the process side with split flow: part enters the heat exchanger and the other part bypasses the heat exchanger.
regards,
roker
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