Throttling Calorimeter water equivalent

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SUMMARY

The discussion centers on the calculation of the state of steam after it passes through an isenthalpic throttle device, reducing its pressure from 3.0 MN/m² to atmospheric pressure. The problem involves determining the specific enthalpy of the steam using heat transfer equations, with the initial setup including an 850g container and 8kg of water. The user calculated the specific enthalpy to be 2899.88 kJ/kg, while a textbook method yielded 2985.188 kJ/kg, leading to confusion regarding the concept of water equivalent. The user questions the validity of both methods and seeks clarification on the water equivalent concept.

PREREQUISITES
  • Understanding of thermodynamics principles, specifically heat transfer and enthalpy.
  • Familiarity with steam tables and superheated steam properties.
  • Knowledge of specific heat capacities, particularly for water and container materials.
  • Experience with mass conservation principles in thermodynamic systems.
NEXT STEPS
  • Review the concept of water equivalent in thermodynamics and its application in heat transfer calculations.
  • Study the use of steam tables to determine properties of superheated steam at various pressures.
  • Learn about isenthalpic processes and their implications in thermodynamic systems.
  • Practice solving similar problems involving heat transfer and phase changes in steam systems.
USEFUL FOR

Students and professionals in mechanical engineering, particularly those focusing on thermodynamics, heat transfer, and steam systems. This discussion is beneficial for anyone looking to deepen their understanding of steam properties and heat transfer calculations.

aldo sebastian
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Homework Statement


Steam runs through a pipe, and the state of the steam is required to be found. To do this, some of the steam was condensed inside a container filled with water.

The container weighs 850g, and has 8kg of liquid water inside it initially. The whole system was measured to be in 16 degrees celsius.

The steam is inserted into the container, and after condensation the new total weight of the container+water+condensed steam is 9.04kg and the new temperature is 31.5 degrees celsius.

The steam was originally in the pipe at 3.0 MN/m2. To safely pass the steam into the container, it was first passed through an isenthalpic throttle device to reduce the pressure to atmospheric (0.1 MN/m2).

Homework Equations



Determine the state of the steam in the pipe.

specific heat of container = 0.384 kJ/kgK and specific heat of liquid water = 4.2 kJ/kgK

The Attempt at a Solution



So I did this:
Inside the container,
Heat transferred by steam = Heat absorbed by water

specific enthalphy of steam after throttling x steam mass - steam mass x 4.2 x 31.5 (i.e. the steam that has condensed) = water mass * 4.2 * (31.5-16) + container mass * 0.384 * (31.5-16).

The steam mass is, from mass conservation, equal to 9.04-8-0.85=0.19 kg

Solving for specific enthalphy I got it to be 2899.88 kJ/kg
Since throttling doesn't change the specific enthalphy of the steam, the specific enthalphy of steam after throttling=before throttling.

And so now we know the pressure and the specific enthalphy at the pipe, we can go to steam tables and realize that the steam is superheated.

Now however in textbook I saw that they do this instead to the heat transfer equation:

specific enthalphy of steam after throttling x steam mass - steam mass x 4.2 x 31.5 (i.e. the steam that has condensed) = water mass * 4.2 * (31.5-16) + (container mass *4.2 ) * 0.384 (31.5-16)

in which they claim that it is the water equivalent of container. Doing it their way gives specific enthalphy of 2985.188 kJ/kg.

Where did I go wrong in my method? what is this water equivalent thing?
I also realized I did not use the information about the pressure after throttling. Did I do something wrong?
 
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In my judgment, you are right and they are wrong. But I don't like the way either you or they have set up the problem.
 

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