Work done by expansion of liquidfied natural gas to atmosphere

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SUMMARY

The discussion focuses on calculating the work done by the expansion of liquefied hydrocarbon gases (butane, i-butane, propane) at 40 psi when released to the atmosphere. The user, Rick, is uncertain whether to approach the problem using isothermal or adiabatic expansion principles due to the rapid release and cooling effects involved. He also inquires about the energy requirements of a battery that could replace the propellant in achieving the same work output. The conversation highlights the complexities of thermodynamic calculations in gas expansion scenarios.

PREREQUISITES
  • Understanding of thermodynamics, specifically isothermal and adiabatic processes.
  • Familiarity with the properties of hydrocarbon gases, including butane, i-butane, and propane.
  • Knowledge of pressure-volume work calculations in gas systems.
  • Basic principles of fluid dynamics related to gas ejection and velocity calculations.
NEXT STEPS
  • Research the principles of isothermal and adiabatic expansion in thermodynamics.
  • Learn about calculating work done by gases during expansion using the ideal gas law.
  • Investigate the energy requirements for battery systems to perform equivalent work as gas propellants.
  • Explore fluid dynamics concepts related to the velocity of ejecta in gas release scenarios.
USEFUL FOR

This discussion is beneficial for chemical engineers, thermodynamics students, and professionals involved in energy systems and fluid dynamics, particularly those working with gas expansion and propellant systems.

casts_by_fly
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Hi All,

Been try at this for a week now and I know I'm missing something. I'm too far out of university to remember how to do it, but just close enough to know that I should remember.

Anyway, I have a steel can containing a mixture of liquidfied hydrocarbon gasses (butane/i-butane/propane) at 40 psi internal pressure. Most of the hydrocarbons are liquified, though there is some headspace. Additionally there is another fluid in the container that is being expelled by the propellant (they are mixed, but not miscible if it matters). They are released through a valve to the atmosphere in short bursts with time between the bursts for the can to return to room temperature (nominally 300K). How much work does the compressed hydrocarbon do on the other liquid when released to the atmostphere? If I were to replace the propellant with a battery, how much energy would the battery need to hold to be able to get the same work into the other liquid?

I feel like it is an expansion problem, but can't decide between isothermal (because both the internal gas and the released gas return to room temp) or adiabatic (because the expansion is rapid and there is immediate cooling from both the expansion of the gas and the evaporation of liquid to gas in the container). Neither seems to fit though.

I tried to work it out from a kinetics standpoint by figuring out the velocity of the ejecta and the mass ejected, but the number was very low for what I was expecting.

Any help in setting this up?

Thanks,
Rick
 
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casts_by_fly said:
Hi All,

Been try at this for a week now and I know I'm missing something. I'm too far out of university to remember how to do it, but just close enough to know that I should remember.

Anyway, I have a steel can containing a mixture of liquidfied hydrocarbon gasses (butane/i-butane/propane) at 40 psi internal pressure. Most of the hydrocarbons are liquified, though there is some headspace. Additionally there is another fluid in the container that is being expelled by the propellant (they are mixed, but not miscible if it matters). They are released through a valve to the atmosphere in short bursts with time between the bursts for the can to return to room temperature (nominally 300K). How much work does the compressed hydrocarbon do on the other liquid when released to the atmostphere? If I were to replace the propellant with a battery, how much energy would the battery need to hold to be able to get the same work into the other liquid?

I feel like it is an expansion problem, but can't decide between isothermal (because both the internal gas and the released gas return to room temp) or adiabatic (because the expansion is rapid and there is immediate cooling from both the expansion of the gas and the evaporation of liquid to gas in the container). Neither seems to fit though.

I tried to work it out from a kinetics standpoint by figuring out the velocity of the ejecta and the mass ejected, but the number was very low for what I was expecting.

Any help in setting this up?

Thanks,
Rick

I'm a little surprised someone has not responded to this, It sounds a lot like some things I have brought up, my math sucks so I won't be of much help, but there are some very sharp people here, just hope I have not worn them down too much.

Bump!

RonL
 

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