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Why Steam Is Expressed In Kg/cm2
#1
Posted 24 October 2011 - 12:59 AM
We all express liquid flow rate in kg/h or m3/h.
If it is a gas we express in Nm3/h.
Why we are expressing steam in kg/cm2 i.e in terms of pressure not in terms of flowrate.
I understand that based on pressure its boiling point and enthalphy changes.I agree with that.
But my doubt is why we are expressing steam flow in pipes in kg.cm2 i.e in terms of pressure instead of flowrate.
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Thanks in advance.
#2
Posted 24 October 2011 - 01:10 AM
2. However, pressure can indirectly measure flowrate, depending on piping configuration of system
3. For example, you have fixed orifice plate downstream
Edited by S.AHMAD, 24 October 2011 - 02:43 AM.
#3
Posted 24 October 2011 - 05:02 AM
By the way, two clarifications related to kg/cm2 could be useful.
1. kg/cm2 does not precisely mean pressure. The former means mass per unit area, pressure is force per unit area. In the old technical (European) system of units, force was expressed in kilograms of force (not in Nt) written as kgr*, or kp (kilopond), of kgf, or even kg. That kg has so far survived, actually meaning weight of a mass of 1 kg. Hence 1 kg/cm2 pressure means 1 kgf/cm2.
2. Velocity in pipes = volumetric flow / pipe cross section, expressed as m3/s/m2 =m/s. Mass velocity is mass flow rate / pipe cross section, expressed as kg/s/m2, or even kg/cm2/s. The kg/cm2/s indicates mass flowrate per unit area of pipe cross section.
Edited by kkala, 24 October 2011 - 05:03 AM.
#4
Posted 24 October 2011 - 11:58 AM
Thank you for your response.
As you told pressure can indirectly measure flowrate,then pls tell me what will be the flowrate of 5kg/cm2 steam that is flowing through 1 inch pipe of 20 m long.
#5
Posted 24 October 2011 - 11:59 AM
thank you
#6
Posted 24 October 2011 - 12:01 PM
Kindly share the complete details for designing a condenser.
#7
Posted 24 October 2011 - 07:18 PM
2. We need to know the downstream pressure (P2)
3. If P2 is less than about P1/2, then use choke flow equation, otherwise use sub-critical flow equation
4. For example if the downstream unit is a steam stripper operated at 1 kg/cm2, (upstream 5 kg/cm2) then use choke flow equation.
5. Deaerator operated below 1 barG, use sub-critical flow equation to estimate the venting steam
Edited by S.AHMAD, 24 October 2011 - 07:20 PM.
#8
Posted 14 November 2011 - 11:48 PM
Thanks a lot. Your reply really cleared my doubt.
Thanks & Regards
Nikhil Sharma
#9
Posted 15 November 2011 - 12:01 AM
http://www.spiraxsar...sting-pipes.asp
note : select sizing on pressure drop
Breizh
Edited by breizh, 15 November 2011 - 01:29 AM.
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