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Pressure Drop Across Control Valves
Started by go-fish, Mar 06 2010 09:56 AM
3 replies to this topic
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#1
Posted 06 March 2010 - 09:56 AM
Hi,
I am a budding process engineer. I am interested in knowing if one can simulate pressure drop across a temperature dependent control valve.
I am using Pro II and trying to simulate a process heater using a rigorous heat exchanger where steam inlet is throttled based on the outlet temperature of the process fluid. My design case has delta T as 20 deg. C and turndown case has delta T as 10 deg. C. The process fluid flow rate is constant and steam flow is required to be throttled in the turndown case.
Thanks
I am a budding process engineer. I am interested in knowing if one can simulate pressure drop across a temperature dependent control valve.
I am using Pro II and trying to simulate a process heater using a rigorous heat exchanger where steam inlet is throttled based on the outlet temperature of the process fluid. My design case has delta T as 20 deg. C and turndown case has delta T as 10 deg. C. The process fluid flow rate is constant and steam flow is required to be throttled in the turndown case.
Thanks
#2
Posted 06 March 2010 - 10:42 AM
Nothing uncommon - that is exactly how the equipment works in reality. By opening or closing steam control valve the pressure in the exchanger channel head varies, thus varying the condensing temperature of steam. The steam header pressure is constant, and by varying control valve position you are varying DP across the valve, and the channel head pressure changes accordingly.
Read more in the attached file:
Read more in the attached file:
Attached Files
#3
Posted 06 March 2010 - 11:46 AM
Nothing uncommon - that is exactly how the equipment works in reality. By opening or closing steam control valve the pressure in the exchanger channel head varies, thus varying the condensing temperature of steam. The steam header pressure is constant, and by varying control valve position you are varying DP across the valve, and the channel head pressure changes accordingly.
Read more in the attached file:
Thank you for the reply. Is there any way by which I can get dP across the steam control valve for various positions like 100% open, 70% open, 50% open? Does simulators have any in-built library from popular control valve vendors where I can just select % opening and the output automatically adjusts the pressure?
#4
Posted 06 March 2010 - 01:41 PM
You can try to play with that in Dynamics mode. Size the valve based on the information you have and Solver will calculate DP values based on flow-DP correlations. If you don't have any information about the valve, size it by yourself and plug design figures into Hysys - it shouldn't be more complicated than that.
For general valve characteristics, download: http://www.documenta.../book/cvh99.pdf or: http://www.engr.sjsu...otes/OZ1000.pdf
For general valve characteristics, download: http://www.documenta.../book/cvh99.pdf or: http://www.engr.sjsu...otes/OZ1000.pdf
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