Understanding how to use steam tables

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Discussion Overview

This discussion revolves around the use of steam tables to find missing thermodynamic properties of water, specifically focusing on a dataset with a temperature of 75°C and a pressure of 500 KPa. Participants explore the implications of these values in terms of energy and steam quality, as well as the phases present in the system.

Discussion Character

  • Homework-related
  • Technical explanation
  • Exploratory
  • Debate/contested

Main Points Raised

  • One participant expresses confusion about how to approach the steam tables given the conditions of T = 75°C and P = 500 KPa, suspecting they are dealing with a compressed liquid.
  • Another participant confirms that 500 KPa is equivalent to 0.5 MPa and notes that the lowest pressure available in the compressed liquid table is 5 MPa.
  • Some participants suggest obtaining additional tables from the NIST website that cover a broader range of pressures for compressed liquid.
  • It is mentioned that the internal energy of a compressed liquid does not vary much with pressure due to water's near incompressibility, suggesting the use of saturated values instead.
  • One participant finds an entry for 0.5 MPa and 75°C in a referenced table but expresses confusion over the value, speculating it may be in kJ/kg.
  • Another participant confirms a value of 313.9 kJ/kg at saturation pressure, relating it to BTU/lb for clarity.
  • Participants discuss the intuitive nature of enthalpy values in Imperial steam tables and relate temperature differences to energy content.

Areas of Agreement / Disagreement

Participants generally agree on the conversion of pressure units and the nature of the internal energy of compressed liquids, but there remains uncertainty regarding the specific values in the steam tables and how to interpret them across different systems of measurement.

Contextual Notes

There are limitations in the availability of data for the specified conditions in the steam tables, and participants note the dependence on the definitions and formats of the tables being used. The discussion includes unresolved questions about the exact values and their interpretations.

Who May Find This Useful

This discussion may be useful for students and professionals working with thermodynamic properties of water, particularly those needing to navigate steam tables for various applications in engineering and physics.

reed2100
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Homework Statement


I have a table for 5 sets of data. Each set includes data from one ore more of the following properties - temperature, pressure, energy, and steam quality. I have to look at steam tables for water to find the missing values. For the data set in question I'm given T = 75 C, and P = 500 KPa. I need to find the energy and steam quality, and from steam quality I get number of phases present.

Homework Equations


for finding x or energy if calculation is required - u = x*(u liquid) + ((1-x)*(u gas))
just rearrange the above to find x if needed

The Attempt at a Solution


One of the data sets gives me a temperature and pressure of 75 C and 500 KPa, nothing else. I looked at water's saturated steam tables for this temperature and pressure. I found that P>Saturated Pressure and T<Saturated Temperature (at these given values), so I'm assuming that I'm actually looking at a compressed liquid. I then looked at the steam tables for compressed liquid, but I can't find a data set for 75 C and 500 KPa. The temperature range includes 75 C, but all the pressures are in the multiple MPa's. Can someone help me clarify how to properly approach these tables? I'm a bit confused here. Any and all help is appreciated, thank you.
 
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reed2100 said:

Homework Statement


I have a table for 5 sets of data. Each set includes data from one ore more of the following properties - temperature, pressure, energy, and steam quality. I have to look at steam tables for water to find the missing values. For the data set in question I'm given T = 75 C, and P = 500 KPa. I need to find the energy and steam quality, and from steam quality I get number of phases present.

Homework Equations


for finding x or energy if calculation is required - u = x*(u liquid) + ((1-x)*(u gas))
just rearrange the above to find x if needed

The Attempt at a Solution


One of the data sets gives me a temperature and pressure of 75 C and 500 KPa, nothing else. I looked at water's saturated steam tables for this temperature and pressure. I found that P>Saturated Pressure and T<Saturated Temperature (at these given values), so I'm assuming that I'm actually looking at a compressed liquid. I then looked at the steam tables for compressed liquid, but I can't find a data set for 75 C and 500 KPa. The temperature range includes 75 C, but all the pressures are in the multiple MPa's. Can someone help me clarify how to properly approach these tables? I'm a bit confused here. Any and all help is appreciated, thank you.
What is 500 KPa expressed in units of MPa? This should be a simple conversion. What do the prefixes K and M stand for in the SI system?
 
SteamKing said:
What is 500 KPa expressed in units of MPa? This should be a simple conversion. What do the prefixes K and M stand for in the SI system?
Yes, 500 KPa is .5 MPa unless I'm mistaken. I kept the conversions in mind. On the compressed liquid table the lowest pressure available is 5 MPa.
 
reed2100 said:
Yes, 500 KPa is .5 MPa unless I'm mistaken. I kept the conversions in mind. On the compressed liquid table the lowest pressure available is 5 MPa.
Then get another table.

You can get tables from the NIST website which cover a greater range of pressures for compressed liquid.

http://www.nist.gov/srd/upload/NISTIR5078-Tab3.pdf
 
The internal energy can't be varying much with pressure for a compressed liquid because water is nearly incompressible. So just use the saturated value.
 
SteamKing's link seems to exactly answer the question, i see an entry for 0.5mPa and 75C
but the number is strange to me because I'm used to ASME 1968 tables in BTU's and Fahrenheit... and that table doesn't say...
314.4 ? I suppose it's an SI value for something ? Looks about right to be kJ per kg , around 135 BTU/lb ,
per http://www.endmemo.com/sconvert/kj_kgbtu_lb.php
 
jim hardy said:
SteamKing's link seems to exactly answer the question, i see an entry for 0.5mPa and 75C
but the number is strange to me because I'm used to ASME 1968 tables in BTU's and Fahrenheit... and that table doesn't say...
314.4 ? I suppose it's an SI value for something ? Looks about right to be kJ per kg , around 135 BTU/lb ,
per http://www.endmemo.com/sconvert/kj_kgbtu_lb.php
Yes. My steam tables give 313.9 kj per kg at saturation pressure
 
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Chestermiller said:
Yes. My steam tables give 313.9 kj per kg at saturation pressure
Thanks Chestermiller ! Makes sense now.

With Imperial steam tables enthalpy of compressed water is almost intuitive, ~a BTU/lb per degF above 32.
75C is on Fahrenheit scale 135 degrees above freezing, so around 135BTU/lb . And as you said pressure has a very minor effect.

old jim
 
Last edited:
Thank you everyone for your help! I appreciate it.
 

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