thermal systems design principles of space systems design u n i v e r s i t y o f maryland thermal...
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Thermal Systems DesignPrinciples of Space Systems Design
U N I V E R S I T Y O F
MARYLAND
Thermal Systems Design
ā¢ Fundamentals of heat transferā¢ Radiative equilibriumā¢ Surface propertiesā¢ Non-ideal effects
ā Internal power generationā Environmental temperatures
ā¢ Conductionā¢ Thermal system components
Ā© 2002 David L. Akin - All rights reservedhttp://spacecraft.ssl.umd.edu
Thermal Systems DesignPrinciples of Space Systems Design
U N I V E R S I T Y O F
MARYLAND
Classical Methods of Heat Transfer
ā¢ Convectionā Heat transferred to cooler surrounding gas, which
creates currents to remove hot gas and supply new cool gas
ā Donāt (in general) have surrounding gas or gravity for convective currents
ā¢ Conductionā Direct heat transfer between touching componentsā Primary heat flow mechanism internal to vehicle
ā¢ Radiationā Heat transferred by infrared radiationā Only mechanism for dumping heat external to vehicle
Thermal Systems DesignPrinciples of Space Systems Design
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Ideal Radiative Heat Transfer
Planckās equation gives energy emitted in a specific frequency by a black body as a function of temperature
ā¢ Stefan-Boltzmann equation integrates Planckās equation over entire spectrum
ā¬
Prad =ĻT 4
ā¬
eĪ»b =2ĻhC0
2
Ī»5 expāhC0
Ī»kT
ā
ā ā
ā
ā ā ā1
ā”
ā£ ā¢
ā¤
ā¦ ā„
(Donāt worry, we wonāt actually use this equation for anythingā¦)
ā¬
Ļ =5.67x10ā8 Wm2Ā°K 4
(āStefan-Boltzmann Constantā)
Thermal Systems DesignPrinciples of Space Systems Design
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Thermodynamic Equilibrium
ā¢ First Law of Thermodynamics
heat in -heat out = work done internallyā¢ Heat in = incident energy absorbedā¢ Heat out = radiated energyā¢ Work done internally = internal power
used(negative work in this sense - adds to total heat in the system)
ā¬
QāW =dUdt
Thermal Systems DesignPrinciples of Space Systems Design
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Radiative Equilibrium Temperature
ā¢ Assume a spherical black body of radius r
ā¢ Heat in due to intercepted solar flux
ā¢ Heat out due to radiation (from total surface area)
ā¢ For equilibrium, set equal
ā¢ 1 AU: Is=1394 W/m2; Teq=280Ā°K
ā¬
Qin =IsĻr2
ā¬
Qout =4Ļr2ĻT 4
ā¬
IsĻr2 =4Ļ r2ĻT4 ā Is =4ĻT4
ā¬
Teq =Is
4Ļ
ā
ā ā
ā
ā ā
14
Thermal Systems DesignPrinciples of Space Systems Design
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Effect of Distance on Equilibrium Temp
0
50
100
150
200
250
300
350
400
450
500
0 10 20 30 40
Distance from Sun (AU)
Black Body Equilibrium Temperature
(Ā°K)
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Shape and Radiative Equilibrium
ā¢ A shape absorbs energy only via illuminated faces
ā¢ A shape radiates energy via all surface area
ā¢ Basic assumption made is that black bodies are intrinsically isothermal (perfect and instantaneous conduction of heat internally to all faces)
Thermal Systems DesignPrinciples of Space Systems Design
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Effect of Shape on Black Body Temps
Thermal Systems DesignPrinciples of Space Systems Design
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Incident Radiation on Non-Ideal Bodies
Kirchkoffās Law for total incident energy flux on solid bodies:
whereā =absorptance (or absorptivity)ā =reflectance (or reflectivity)ā =transmittance (or transmissivity)
ā¬
QIncident=Qabsorbed+Qreflected+Qtransmitted
ā¬
Qabsorbed
QIncident
+Qreflected
QIncident
+Qtransmitted
QIncident
=1
ā¬
Ī± ā”Qabsorbed
QIncident
; Ļ ā”Qreflected
QIncident
; Ļā”Qtransmitted
QIncident
Thermal Systems DesignPrinciples of Space Systems Design
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Non-Ideal Radiative Equilibrium Temp
ā¢ Assume a spherical black body of radius r
ā¢ Heat in due to intercepted solar flux
ā¢ Heat out due to radiation (from total surface area)
ā¢ For equilibrium, set equal
ā¬
Qin =IsĪ±Ļ r2
ā¬
Qout =4Ļr2ĪµĻT 4
ā¬
IsĪ±Ļr2 =4Ļr2ĪµĻT4 ā Is =4ĪµĪ±
ĻT 4
ā¬
Teq =Ī±Īµ
Is
4Ļ
ā
ā ā
ā
ā ā
14
( = āemissivityā - efficiency of surface at radiating heat)
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Effect of Surface Coating on Temperature
0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1
0 0.2 0.4 0.6 0.8 1
Teq=560Ā°K (a/e=4)Teq=471Ā°K (a/e=2)Teq=396Ā°K (a/e=1)Teq=333Ā°K (a/e=0.5)Teq=280Ā°K (a/e=0.25)
Black Ni, Cr, Cu Black Paint
White Paint
Optical Surface Reflector
Polished Metals
Aluminum Paint
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Non-Ideal Radiative Heat Transfer
ā¢ Full form of the Stefan-Boltzmann equation
where Tenv=environmental temperature (=4Ā°K for space)
ā¢ Also take into account power used internally
ā¬
Prad =ĪµĻA T 4 āTenv4
( )
ā¬
IsĪ± As+Pint =ĪµĻArad T4 āTenv4
( )
Thermal Systems DesignPrinciples of Space Systems Design
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Example: AERCam/SPRINT
ā¢ 30 cm diameter sphereā¢ =0.2; =0.8ā¢ Pint=200Wā¢ Tenv=280Ā°K (cargo bay
below; Earth above)ā¢ Analysis cases:
ā Free space w/o sunā Free space w/sunā Earth orbit w/o sunā Earth orbit w/sun
Thermal Systems DesignPrinciples of Space Systems Design
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AERCam/SPRINT Analysis (Free Space)
ā¢ As=0.0707 m2; Arad=0.2827 m2
ā¢ Free space, no sun
ā¬
Pint = ĪµĻAradT4 ā T =
200W
0.8 5.67 Ć10ā8 W
m2Ā°K 4
ā
ā ā
ā
ā ā 0.2827m2( )
ā
ā
ā ā ā ā
ā
ā
ā ā ā ā
14
= 354Ā°K
Thermal Systems DesignPrinciples of Space Systems Design
U N I V E R S I T Y O F
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AERCam/SPRINT Analysis (Free Space)
ā¢ As=0.0707 m2; Arad=0.2827 m2
ā¢ Free space with sun
ā¬
IsĪ± As + Pint = ĪµĻAradT4 ā T =
IsĪ± As + Pint
ĪµĻArad
ā
ā ā
ā
ā ā
14
= 362Ā°K
Thermal Systems DesignPrinciples of Space Systems Design
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AERCam/SPRINT Analysis (LEO Cargo Bay)
ā¢ Tenv=280Ā°K
ā¢ LEO cargo bay, no sun
ā¢ LEO cargo bay with sun
ā¬
Pint =ĪµĻArad T4 āTenv4
( )ā T =200W
0.8 5.67Ć10ā8 Wm2Ā°K4
ā
ā ā
ā
ā ā 0.2827m2( )
+(280Ā°K)4
ā
ā
ā ā ā ā ā
ā
ā
ā ā ā ā ā
14
=384Ā°K
ā¬
IsĪ± As+Pint =ĪµĻArad T4 āTenv4
( )ā T =IsĪ± As+Pint
ĪµĻArad
+Tenv4
ā
ā ā ā
ā
ā ā ā
14
=391Ā°K
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Radiative Insulation
ā¢ Thin sheet (mylar/kapton with surface coatings) used to isolate panel from solar flux
ā¢ Panel reaches equilibrium with radiation from sheet and from itself reflected from sheet
ā¢ Sheet reaches equilibrium with radiation from sun and panel, and from itself reflected off panel
Is
Tinsulation Twall
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Multi-Layer Insulation (MLI)ā¢ Multiple insulation
layers to cut down on radiative transfer
ā¢ Gets computationally intensive quickly
ā¢ Highly effective means of insulation
ā¢ Biggest problem is existence of conductive leak paths (physical connections to insulated components)
Is
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1D Conduction
ā¢ Basic law of one-dimensional heat conduction (Fourier 1822)
whereK=thermal conductivity (W/mĀ°K)A=areadT/dx=thermal gradient
ā¬
Q=āKAdTdx
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3D Conduction
General differential equation for heat flow in a solid
whereg(r,t)=internally generated heat
=density (kg/m3)
c=specific heat (J/kgĀ°K)
K/c=thermal diffusivity
ā¬
ā 2Tr r ,t( )+
g(r r ,t)K
=ĻcK
āTr r ,t( )
āt
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Simple Analytical Conduction Model
ā¢ Heat flowing from (i-1) into (i)
ā¢ Heat flowing from (i) into (i+1)
ā¢ Heat remaining in cell
TiTi-1 Ti+
1
ā¬
Qin =āKATi āTiā1
Īx
ā¬
Qout =āKATi+1 āTi
Īx
ā¬
Qout āQin =ĻcK
Ti( j +1)āTi( j)Īt
ā¦ ā¦
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Heat Pipe Schematic
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Shuttle Thermal Control Components
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Shuttle Thermal Control System Schematic
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ISS Radiator Assembly