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MODELING OF PROPELLANT TANK
PRESSURIZATION
By:Amr hassan ahmed darwish
LAYOUT
SELF PRESSURIZED SYSTEMS
The advantages:
•Simple design with low parts count
•Inexpensive vehicle production
•Selectable tank pressures ranging up to
7Mpa
•Very few failure modes leading to superior
reliability
INTRODUCTION
What is the major advantage of
modeling the Propellant tank
pressurization ?
Propellant tank pressurization is an
essential element of the prediction of
rocket performance. This is the case
even more so for hybrid rockets that use
a self-pressurizing oxidizer because the
thrust produced by the motor is
dependent on oxidizer tank pressure.
What is the Objective ?
Developing a model of a propellant
feed system that can be readily
incorporated into a rocket design
computer program. The model
developed is general and should
work well for propellant tanks that are
pressure fed with an inert gas and
also for self-pressurizing systems.
THE MODELING ANALYSIS
Assumptions
• Open system
• Real gas
• Two-phase (liquid-vapor) homogenous Nitrous
oxide
• The saturation layer is a thin layer
• Regular geometry shape of storage Tank
(cylinder shape)
• Frictionless flow in the tank
• Tank is in vertical position
• No chemical reactions
• No mechanical work
• Neglect change in potential energy
GOVERNING EQUATIONS
The first law of thermodynamics
FOR LIQUID CONTROL VOLUME
For gas control volume
Evaluation of Thermodynamic Properties
The Soave-Benedict-Webb Rubin Equation of State
equation
Peng –Robinson Equation of state (PR EOS)
EVALUATION OF ENTHALPY AND INTERNAL
ENERGY
EVALUATING THE RATE OF MASSES
The rate of condensed vapor
The rate of evaporated liquid
The rate of change of gas mass Equation
The mass flow rate through the propellant
Feed system
The rate of change of Liquid mass Equation
EVALUATING THE RATE OF MASSES
EVALUATING THE RATE OF VOLUME CHANGE
The rate of change of bulk Liquid
volume:-
The rate of change of gas volume
HEAT TRANSFER
During the period of time when liquid is being expelled from the tank,
vaporization takes place at the liquid -vapor mixture interface or possibly
within the bulk liquid in the form of boiling
The free convection heat transfer between liquid and liquid
surface layer is
THE SOLUTION METHODOLOGY
Initial condition: The capacity of the oxidizer tank is 0.0354 m^3
with Tmperature surround the tank and mass are well known. The injector
area is 0.0001219352 m^2 in this model.
Calculate the saturation pressure from the surround temperature
and use The Soave-Benedict-Webb Rubin Equation of State to
get the density of gas and Liquid then evaluate the mass of liquid
and vapor from mass balanced equation .
a) Integrate numerically with time using the modified Euler method
𝑇𝐿 , 𝑇𝑇𝐺 , 𝑉𝑇𝐺 , 𝑉𝐿 , 𝑚 𝐿 and 𝑚 𝑇𝐺 to obtain 𝑇𝐿, 𝑇𝑇𝐺 ,𝑃𝑇𝐺 ,𝑉𝑇𝐺 , 𝑉𝐿, 𝑚 𝑇𝐺 , 𝑚 𝐿
Assume initially 𝜌𝐿 , 𝑃𝑇𝐺 and 𝜌 𝑇𝐺 are all set to be zero.
RESULTS
TEST 1
,
Comparison of measured and ullage
pressure.
TEST 1
,
Variation temperature time history.
TEST 1
,
The variation of Propellant mass
TEST 2 ,,
Variation of tank pressure with time
,
TEST 2 ,,
The variation of Propellant mass
TEST 3 ,,,
Variation of tank pressure with time
TEST 3 ,,,
The variation of Propellant mass
TEST 4 ,,,,
Variation of tank pressure with time
TEST 4 ,,,,
The variation of Propellant mass
CONCLUSION
•A computer program of a propellant tank pressurization system
has been developed.
• This model is used to predict the self-pressurizing oxidizer
system of a moderate size hybrid rocket.
• The model does not assume thermo or phase equilibrium
(although the liquid surface is set equal to the saturated vapor
temperature) and is applicable to propellants that exhibit real-
fluid behavior.
• The results obtained are in good agreement with the published
and experimental data
REFERENCES
•M. Arif Karabeyoglu ," Modeling of Propellant Tank Pressurization",AIAA 2005-3549, 41th AIAA/ASME/ASEE
Joint Propulsion Conference, Tucson, Az, July 2005.
•V.A. Zakirov, L. Li ," 1-D, Homogenous Liquefied Gas Self –Pressurization Model", Tsinghua University, Beijing,
P.R. China, European conference Aerospace sciences (EUCASS).
•.Claus K. Zéberg-Mikkelsen," Viscosity Study of Hydrocarbon Fluids at Reservoir Conditions Modeling and
Measurements ", Department of Chemical Engineering, June 2001.
•Alok Majumdar and Todd Steadman," Numerical Modeling of Pressurization of a Propellant Tank ", Sverdrup
Technology, Huntsville, AI.
•Don W.Green and Robert H.Perry ,Perry's Chemical Engineers' Handbook, 8thEd, McGraw-Hill , Inc.,New York
,NY,2008.
•Rick Newlands," The physics of Nitrous Oxide", aspirespace, 2006.
•http://www.tsinghua.edu.cn/docsn/lxx/mainpage/a/Web/index.htm
•Margaret Mary Fernandez," Propellant Tank Pressurization Modeling for a Hybrid Rocket", Department of
Mechanical Engineering,Kate Gleason College of Engineering,Rochester Institute of Technology,Rochester, NY
14623, August 2009.
•Zakia Nasri and Housam Binous," Applications of the Peng-Robinson Equation of State using MATLAB",
National Institute of Applied Sciences and Technology.
•Matías A. Monsalvo," Phase Behavior and Viscosity Modeling of Refrigerant-Lubricant Mixtures", Ph. D. Thesis,
Technical University of Denmark, Center for Phase Equilibrium and Separation Process.
Thank you for
listening

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Modeling of Propellant Tank Pressurization

  • 1. MODELING OF PROPELLANT TANK PRESSURIZATION By:Amr hassan ahmed darwish
  • 3. SELF PRESSURIZED SYSTEMS The advantages: •Simple design with low parts count •Inexpensive vehicle production •Selectable tank pressures ranging up to 7Mpa •Very few failure modes leading to superior reliability
  • 5. What is the major advantage of modeling the Propellant tank pressurization ? Propellant tank pressurization is an essential element of the prediction of rocket performance. This is the case even more so for hybrid rockets that use a self-pressurizing oxidizer because the thrust produced by the motor is dependent on oxidizer tank pressure.
  • 6. What is the Objective ? Developing a model of a propellant feed system that can be readily incorporated into a rocket design computer program. The model developed is general and should work well for propellant tanks that are pressure fed with an inert gas and also for self-pressurizing systems.
  • 7. THE MODELING ANALYSIS Assumptions • Open system • Real gas • Two-phase (liquid-vapor) homogenous Nitrous oxide • The saturation layer is a thin layer • Regular geometry shape of storage Tank (cylinder shape) • Frictionless flow in the tank • Tank is in vertical position • No chemical reactions • No mechanical work • Neglect change in potential energy
  • 8. GOVERNING EQUATIONS The first law of thermodynamics
  • 9. FOR LIQUID CONTROL VOLUME For gas control volume
  • 10.
  • 11. Evaluation of Thermodynamic Properties The Soave-Benedict-Webb Rubin Equation of State equation Peng –Robinson Equation of state (PR EOS)
  • 12. EVALUATION OF ENTHALPY AND INTERNAL ENERGY
  • 13. EVALUATING THE RATE OF MASSES The rate of condensed vapor The rate of evaporated liquid The rate of change of gas mass Equation The mass flow rate through the propellant Feed system
  • 14. The rate of change of Liquid mass Equation EVALUATING THE RATE OF MASSES
  • 15. EVALUATING THE RATE OF VOLUME CHANGE The rate of change of bulk Liquid volume:- The rate of change of gas volume
  • 16. HEAT TRANSFER During the period of time when liquid is being expelled from the tank, vaporization takes place at the liquid -vapor mixture interface or possibly within the bulk liquid in the form of boiling The free convection heat transfer between liquid and liquid surface layer is
  • 17. THE SOLUTION METHODOLOGY Initial condition: The capacity of the oxidizer tank is 0.0354 m^3 with Tmperature surround the tank and mass are well known. The injector area is 0.0001219352 m^2 in this model. Calculate the saturation pressure from the surround temperature and use The Soave-Benedict-Webb Rubin Equation of State to get the density of gas and Liquid then evaluate the mass of liquid and vapor from mass balanced equation . a) Integrate numerically with time using the modified Euler method 𝑇𝐿 , 𝑇𝑇𝐺 , 𝑉𝑇𝐺 , 𝑉𝐿 , 𝑚 𝐿 and 𝑚 𝑇𝐺 to obtain 𝑇𝐿, 𝑇𝑇𝐺 ,𝑃𝑇𝐺 ,𝑉𝑇𝐺 , 𝑉𝐿, 𝑚 𝑇𝐺 , 𝑚 𝐿 Assume initially 𝜌𝐿 , 𝑃𝑇𝐺 and 𝜌 𝑇𝐺 are all set to be zero.
  • 18.
  • 20. TEST 1 , Comparison of measured and ullage pressure.
  • 22. TEST 1 , The variation of Propellant mass
  • 23. TEST 2 ,, Variation of tank pressure with time ,
  • 24. TEST 2 ,, The variation of Propellant mass
  • 25. TEST 3 ,,, Variation of tank pressure with time
  • 26. TEST 3 ,,, The variation of Propellant mass
  • 27. TEST 4 ,,,, Variation of tank pressure with time
  • 28. TEST 4 ,,,, The variation of Propellant mass
  • 29. CONCLUSION •A computer program of a propellant tank pressurization system has been developed. • This model is used to predict the self-pressurizing oxidizer system of a moderate size hybrid rocket. • The model does not assume thermo or phase equilibrium (although the liquid surface is set equal to the saturated vapor temperature) and is applicable to propellants that exhibit real- fluid behavior. • The results obtained are in good agreement with the published and experimental data
  • 30. REFERENCES •M. Arif Karabeyoglu ," Modeling of Propellant Tank Pressurization",AIAA 2005-3549, 41th AIAA/ASME/ASEE Joint Propulsion Conference, Tucson, Az, July 2005. •V.A. Zakirov, L. Li ," 1-D, Homogenous Liquefied Gas Self –Pressurization Model", Tsinghua University, Beijing, P.R. China, European conference Aerospace sciences (EUCASS). •.Claus K. Zéberg-Mikkelsen," Viscosity Study of Hydrocarbon Fluids at Reservoir Conditions Modeling and Measurements ", Department of Chemical Engineering, June 2001. •Alok Majumdar and Todd Steadman," Numerical Modeling of Pressurization of a Propellant Tank ", Sverdrup Technology, Huntsville, AI. •Don W.Green and Robert H.Perry ,Perry's Chemical Engineers' Handbook, 8thEd, McGraw-Hill , Inc.,New York ,NY,2008. •Rick Newlands," The physics of Nitrous Oxide", aspirespace, 2006. •http://www.tsinghua.edu.cn/docsn/lxx/mainpage/a/Web/index.htm •Margaret Mary Fernandez," Propellant Tank Pressurization Modeling for a Hybrid Rocket", Department of Mechanical Engineering,Kate Gleason College of Engineering,Rochester Institute of Technology,Rochester, NY 14623, August 2009. •Zakia Nasri and Housam Binous," Applications of the Peng-Robinson Equation of State using MATLAB", National Institute of Applied Sciences and Technology. •Matías A. Monsalvo," Phase Behavior and Viscosity Modeling of Refrigerant-Lubricant Mixtures", Ph. D. Thesis, Technical University of Denmark, Center for Phase Equilibrium and Separation Process.