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For <math>\mu_e/\mu_c = 1.00</math> the <font color="red">solution to this expression is <math>\xi_i = 1.668462981</math></font>.
For <math>\mu_e/\mu_c = 1.00</math> the <font color="red">solution to this expression is <math>\xi_i = 1.668462981</math></font>.
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Revision as of 23:40, 29 March 2026

Main Sequence to Red Giant to Planetary Nebula


Part I:  Background & Objective

 


Part II: 

 


Part III: 

 


Part IV: 

 

Preface

file = Dropbox/WorkFolder/Wiki edits/EmbeddedPolytropes/CombinedSequences.xlsx --- worksheet = EqSeqCombined2
file = Dropbox/WorkFolder/Wiki edits/EmbeddedPolytropes/CombinedSequences.xlsx --- worksheet = EqSeqCombined2
Figure 1:  Equilibrium Sequences
of Pressure-Truncated Polytropes

Equilibrium sequences of Pressure-Truncated Polytropes

As has been detailed in an accompanying chapter, we have successfully analyzed the relative stability of pressure-truncated polytopes. The curves shown here on the right in Figure 1 graphically present the mass-radius relationship for pressure-truncated model sequences having a variety of polytropic indexes, as labeled, over the range 1n6. (Another version of this figure includes the isothermal sequence.) On each sequence for which n3, the green filled circle identifies the model with the largest mass. We have shown analytically that the oscillation frequency of the fundamental-mode of radial oscillation is precisely zero for each one of these maximum-mass models. As a consequence, we know that each green circular marker identifies the point along its associated sequence that separates dynamically stable (larger radii) from dynamically unstable (smaller radii) models.

Key Realization: Along sequences of pressure-truncated polytropes, the maximum-mass models identify precisely where the onset of dynamical instability occurs.


The principal question is: Along bipolytropic sequences, are maximum-mass models (identified by the solid green circular markers in Fig. 2) associated with the onset of dynamical instabilities? For more details, look here.

Figure 2: Equilibrium Sequences of Bipolytropes

with (nc,ne)=(5,1) and Various μe/μc

Analytically Determined Parameters
for Models that have the Maximum Fractional Core Mass
(solid green circular markers)
Along Various Equilibrium Sequences

Extrema along Various Equilibrium Sequences

μeμc

ξi

qrcoreR

νMcoreMtot

13

0.0 2π

0.33

24.00496 0.038378833 0.52024552

0.316943

10.744571 0.068652714 0.382383875

0.31

9.014959766 0.0755022550 0.3372170064

0.3090

8.8301772 0.076265588 0.331475715

14

4.9379256 0.084824137 0.139370157

Additional model parameters can be found here.


In terms of mass (m), length (), and time (t), the units of various physical constants and variables are:

Mass-density

m3

Pressure (energy-density)

m1t2

Newtonian gravitational constant, G

m13t2

The core's polytropic constant, Kc

[m113t10]1/5

The envelope's polytropic constant, Ke

m15t2


As a result, for example (see details below), if we hold the central-density (ρ0) — as well as G and Kc — constant along an equilibrium sequence, mass will scale as …

Mass

[Kc3/2G3/2ρ01/5]

 

{[m113t10]1/5}3/2[m13t2]3/2[m3]1/5

 

[m3/10+3/21/5][39/109/2+3/5][t3+3]

 

[m+1][0][t0].

If instead (see details below) we hold Ke — as well as G and Kc — constant along an equilibrium sequence, mass will scale as …

Mass

[Kc5KeG6]1/4

 

{[m113t10][m15t2][m13t2]6}1/4

 

{[m11+6][13+518][t102+12]}1/4

 

[m+1][0][t0].

Original Model Construction

Fixed Central Density

From Examples, we find,

Mcore=Mcore*[Kc3/2G3/2ρ01/5]

=

[Kc3/2G3/2ρ01/5](6π)1/2(ξiθi)3;

Mtot=Mtot*[Kc3/2G3/2ρ01/5]

=

[Kc3/2G3/2ρ01/5](μeμc)2(2π)1/2Aηsθi;

rcore=rcore*[Kc1/2G1/2ρ02/5]

=

[Kc1/2G1/2ρ02/5](32π)1/2ξi;

R=rs*[Kc1/2G1/2ρ02/5]

=

[Kc1/2G1/2ρ02/5](μeμc)1ηs2πθi2;

where, rewriting the relevant expressions in terms of the parameters,

iξi3;       and       m33(μeμc),

we find,

θi

=

(1+i2)1/2

ηi

=

(μeμc)3θi2ξi=m3(i1+i2)

Λi

=

1ηiξi3=[1+i2m3i]i=1m3i[1+(1m3)i2]

A2

=

ηi2(1+Λi2)

 

=

m32(i1+i2)2(1+i2)m32i2[1+(1m3)2i2]

 

=

[1+(1m3)2i21+i2]

(1+Λi2)

=

ηi2[1+(1m3)2i21+i2]=1m32[(1+i2)2i2][1+(1m3)2i21+i2]=(1+i2)m32i2[1+(1m3)2i2]

ηs

=

π2+ηi+tan1(Λi)

Fixed Interface Pressure

Equilibrium Sequence Expressions

From the relevant interface conditions, we find,

(KeKc)

=

ρ04/5(μeμc)2θi4.

Inverting this last expression gives,

ρ04/5

=

(μeμc)2θi4(KeKc)1

ρ01/5

=

[(μeμc)1/2θi1(KeKc)1/4].

Hence, keeping Kc and Ke constant, we have,

Mcore

=

[Kc3/2G3/2(KeKc)1/4][(μeμc)1/2θi](6π)1/2(ξiθi)3

 

=

[Kc5KeG6]1/4(μeμc)1/2(6π)1/2ξi3θi4;

Mtot

=

[Kc3/2G3/2(KeKc)1/4][(μeμc)1/2θi](μeμc)2(2π)1/2Aηsθi

 

=

[Kc5KeG6]1/4(μeμc)3/2(2π)1/2Aηs;

rcore

=

[KeG1]1/2(μeμc)(32π)1/2ξiθi2;

R

=

[KeG1]1/2ηs2π;

ρ0

=

[KeKc]5/4(μeμc)5/2θi5;

Pi

=

[Kc][(μeμc)3θi6(KeKc)3/2]θi6

 

=

[Kc5Ke3]1/2(μeμc)3.

This last expression shows that if Kc and Ke are both held fixed, then the interface pressure, Pi, will be constant along the sequence of equilibrium models.

Note also:

νMcoreMtot

=

{[Kc5KeG6]1/4(μeμc)1/2(6π)1/2ξi3θi4}{[Kc5KeG6]1/4(μeμc)3/2(2π)1/2Aηs}1

 

=

(μeμc)23ξi3θi4Aηs;

qrcoreR

=

{[KeG1]1/2(μeμc)(32π)1/2ξiθi2}{[KeG1]1/2ηs2π}1

 

=

(μeμc)3ξiθi2ηs.

Sequence Plots

A plot of Mtot[Kc5KeG6]1/4 versus R[KeG1]1/2 at fixed interface pressure will be generated via the relations,

Ordinate: Mtot   Abscissa: R

(μeμc)3/2(2π)1/2Aηs

vs

ηs2π.

Alternatively, a plot of Mtot[Kc5KeG6]1/4 versus log10(ρ0)[KeKc]5/4 at fixed interface pressure will be generated via the relations,

Ordinate: Mtot   Abscissa: log10(ρ0)

(μeμc)3/2(2π)1/2Aηs

vs

log10[(μeμc)5/2θi5]

The expression for dMtot/di is …

[Kc5KeG6]1/4dMtotdi

=

(μeμc)3/2(2π)1/2ddi[Aηs]

  =

(μeμc)3/2(2π)1/2ddi[Aηs]

 

=

(μeμc)3/2(2π)1/2ddi{[1+(1m3)2i21+i2]1/2[π2+ηi+tan1(Λi)]}

(μeμc)3/2(2π)1/2[Kc5KeG6]1/4dMtotdi

=

12[π2+ηi+tan1(Λi)][1+(1m3)2i21+i2]1/2ddi{[1+(1m3)2i21+i2]}

 

 

+[1+(1m3)2i21+i2]1/2{dηidi}+[1+(1m3)2i21+i2]1/2{ddi[tan1(Λi)]}

 

=

12[π2+ηi+tan1(Λi)][1+(1m3)2i21+i2]1/2ddi{[1+(1m3)2i21+i2]}

 

 

+[1+(1m3)2i21+i2]1/2{ddi[m3(i1+i2)]}+[1+(1m3)2i21+i2]1/2[11+Λi2]dΛidi

The extremum in Mtot occurs when the LHS of this expression is zero, that is, when …

ηi

=

m3i(1+i2)1

Λi

=

[1+(1m3)i2]m3i

(1+Λi2)1

=

m32i2(1+i2)[1+(1m3)2i2]1

2[1+(1m3)2i21+i2]1/2{ddi[m3(i1+i2)]}+2[1+(1m3)2i21+i2]1/2[11+Λi2]dΛidi

=

[π2+ηi+tan1(Λi)][1+(1m3)2i21+i2]1/2ddi{[1+(1m3)2i21+i2]}

2m3[1+(1m3)2i21+i2]1/2ddi{i(1+i2)1}+2m3[1+(1m3)2i21+i2]1/2[11+Λi2]ddi{i1[1+(1m3)i2]}

=

[π2+ηi+tan1(Λi)][1+(1m3)2i21+i2]1/2ddi{(1+i2)1[1+(1m3)2i2]}

2m3[1+(1m3)2i21+i2]{(1+i2)12i2(1+i2)2}+2m3[1+(1m3)2i21+i2][11+Λi2]{i2[1+(1m3)i2]+[2(1m3)]}

=

[π2+ηi+tan1(Λi)]{2i(1+i2)2[1+(1m3)2i2]+(1+i2)1[2i(1m3)2]}

2m3[1+(1m3)2i2(1+i2)3]{(1+i2)2i2}+2m3[1+(1m3)2i21+i2]m32i2(1+i2)[1+(1m3)2i2]1{i2[1+(1m3)i2]+[2(1m3)]}

=

(1+i2)2[π2+ηi+tan1(Λi)]{2i[1+(1m3)2i2]+(1+i2)[2i(1m3)2]}

2m3[1+(1m3)2i2(1+i2)]{(1+i2)2i2}+2m3{[1+(1m3)i2]+[2(1m3)i2]}

=

[π2+ηi+tan1(Λi)]{2i[1+(1m3)2i2]+(1+i2)[2i(1m3)2]}

2m3[1+(1m3)2i2][(1i2)(1+i2)]+2m3[1+(1m3)i2]

=

[π2+ηi+tan1(Λi)]{[2i2(1m3)2i3]+[2i(1m3)2]+[2(1m3)2i3]}

2m3(1+i2){[1+(1m3)2i2][(1i2)]+(1+i2)[1+(1m3)i2]}

=

[π2+ηi+tan1(Λi)]{1(1m3)2}2i

2m3(1+i2){[1+(1m3)2i2]i2[1+(1m3)2i2]+[1+(1m3)i2]+i2[1+(1m3)i2]}

=

[π2+ηi+tan1(Λi)](2m3)2m3i

(1+i2)1{1+(1m3)2i2i2(1m3)2i41+(1m3)i2i2+(1m3)i4}

=

[π2+ηi+tan1(Λi)](2m3)i

1(1+i2)(2m3)i{[m33]m3i2+[1m3]m3i4}

=

[π2+ηi+tan1(Λi)]

m3i(1+i2)(2m3)[(m33)+(1m3)i2]

=

[π2+ηi+tan1(Λi)]

For μe/μc=1.00 the solution to this expression is ξi=1.668462981.



file = Dropbox/WorkFolder/Wiki edits/BiPolytrope/TwoFirstOrderODEs/Bipolytrope51New.xlsx --- worksheet = SequenceMuRatio100
file = Dropbox/WorkFolder/Wiki edits/BiPolytrope/TwoFirstOrderODEs/Bipolytrope51New.xlsx --- worksheet = SequenceMuRatio100
Example data values drawn from worksheet "SequenceMuRatio100" …

Δξ=(9.014995980.05)/99=0.0905551

ngrid ξi=0.05+(ngrid1)Δξ θi A ηs Mtot log10ρ0 R
1 0.05 0.9995836 1.00124818 3.141592582 2.510 0.0009044 1.253
2 0.140555 0.9967235 1.0097655 3.141580334 2.531 0.0071264 1.253
18 1.5894375 0.7367887 1.539943947 2.821678456 3.467 0.663285301 1.126
19 1.6799927 0.7178117 1.566601145 2.775921455 3.470 0.719947375 1.107
20 1.7705478 0.6992927 1.591530391 2.728957898 3.465 0.7767049 1.089
100 9.0149598 0.1886798 1.973119305 0.841461698 1.325 3.62137 0.336

Equilibrium Sequences of (nc,ne)=(5,1) BiPolytropes Having μe/μc=1.0

Mass vs. Radius
(Fixed Interface Pressure)
Mass vs. Central Density
(Fixed Interface Pressure)

Total Mass vs Radius

Total Mass vs Central Density

file = Dropbox/WorkFolder/Wiki edits/BiPolytrope/TwoFirstOrderODEs/Bipolytrope51New.xlsx --- worksheet = MuRatio100Fund
file = Dropbox/WorkFolder/Wiki edits/BiPolytrope/TwoFirstOrderODEs/Bipolytrope51New.xlsx --- worksheet = MuRatio100Fund
Data values drawn from worksheet "MuRatio100Fund" …

Properties of the Marginally Unstable Model

ξi θi A ηs Mtot log10ρ0 R
1.6639103 0.7211498 1.561995126 2.784147185 3.4698598 0.709872477 1.1107140

Fixed Total Mass

Equilibrium Sequence Expressions

Again, drawing from previous Examples in which ρ0 — as well as Kc and G — is held fixed, equilibrium models obey the relations,

Mtot

=

Mtot*[Kc3/2G3/2ρ01/5]=[Kc3/2G3/2ρ01/5](μeμc)2(2π)1/2Aηsθi;

R

=

R*[Kc1/2G1/2ρ02/5]=[Kc1/2G1/2ρ02/5](μeμc)1ηs2πθi2;

Pi

=

Pi*[Kcρ06/5]=[Kcρ06/5]θi6.

Let's invert the first expression in order to construct equilibrium sequences in which the total mass — rather than ρ0 — is held fixed. We find that,

ρ01/5

=

[Kc3/2G3/2Mtot1](μeμc)2(2π)1/2Aηsθi

R

=

[Kc1/2G1/2](μeμc)1ηs2πθi2{[Kc3/2G3/2Mtot1](μeμc)2(2π)1/2Aηsθi}2

 

=

[Kc1/2G1/2](μeμc)1ηs2πθi2[Kc3/2G3/2Mtot1]2(μeμc)4(π2)θi2A2ηs2

 

=

[Kc5/2G5/2Mtot2](μeμc)3(π23)1/21A2ηs.

And,

Pi

=

Kcθi6{[Kc3/2G3/2Mtot1](μeμc)2(2π)1/2Aηsθi}6

 

=

Kc{[Kc3/2G3/2Mtot1]6(μeμc)12(2π)3A6ηs6}

 

=

[Kc10G9Mtot6](μeμc)12(2π)3A6ηs6.

Note as well that,

Pi(4π3R3)

=

4π3[Kc10G9Mtot6](μeμc)12(2π)3A6ηs6{[Kc5/2G5/2Mtot2](μeμc)3(π23)1/21A2ηs}3

 

=

4π3(2π)3(π23)3/2[Kc10G9Mtot6](μeμc)12ηs3{[Kc15/2G15/2Mtot6](μeμc)9}

 

=

4π3(2π)3(π23)3/2[Kc5/2G3/2](μeμc)3ηs3

Sequence Plots

A plot of Pi[Kc10G9Mtot6] versus R3[Kc5/2G5/2Mtot2]3 at fixed interface pressure will be generated via the relations,

Ordinate   Abscissa

(μeμc)12(2π)3A6ηs6

vs

{(μeμc)3(π23)1/21A2ηs}3

Pressure vs Volume
Pressure vs Volume
nu vs q
nu vs q

Hidden Text

Following the Lead of Yabushita75

Here in the context of (nc,ne)=(5,1) bipolytropes, we want to construct an interface-pressure versus volume plot; and mass-versus-central density plots like the ones displayed for truncated isothermal spheres in Figure 1 of an accompanying discussion, and as displayed for a (nc,ne)=(,3/2) bipolytrope in Figure 1 (p. 445) of 📚 S. Yabushita (1975, MNRAS, Vol. 172, pp. 441 - 453).

In our accompanying chapter that presents example models of (nc,ne)=(5,1) bipolytropes, we have adopted the following normalizations:

ρ*

ρρ0

;    

r*

r[Kc1/2/(G1/2ρ02/5)]

P*

PKcρ06/5

;    

Mr*

Mr[Kc3/2/(G3/2ρ01/5)]

Also, from the relevant interface conditions, we find,

(KeKc)

=

ρ04/5(μeμc)2θi4.

Inverting this last expression gives,

ρ04/5

=

(μeμc)2θi4(KeKc)1

ρ01/5

=

(μeμc)1/2θi1(KeKc)1/4.

Hence, we can rewrite the "normalized" expressions as follows:

r

=

r*[Kc1/2G1/2ρ02/5]

 

=

r*{Kc1/2G1/2[(μeμc)1/2θi1(KeKc)1/4]2}

 

=

r*{Kc1/2G1/2[(μeμc)θi2(KeKc)1/2]}

 

=

r*[Ke1/2G1/2](μeμc)θi2.


Fixed Interface Pressure

Start with the model relation,

Pi

=

[Kcρ06/5]Pi*

 

=

[Kcρ06/5](1+13ξi2)3

Now, given that,

ρ01/5

=

(μeμc)1/2θi1(KeKc)1/4.

ρ06/5

=

(μeμc)3θi6(KeKc)3/2.

Fixed Total Mass

Also, from the relevant interface conditions, we find,

(KeKc)

=

ρ04/5(μeμc)2θi4.

Inverting this last expression gives,

ρ04/5

=

(μeμc)2θi4(KeKc)1

ρ01/5

=

(μeμc)1/2θi1(KeKc)1/4.

Hence, for a given specification of the interface location, ξi — test values shown (in parentheses) assuming μe/μc=1.0 and ξi=0.5 — the desired expression for the central density is,

ρ0

=

[Ke5Kc5]1/4(μeμc)5/2θi5;

and, drawing the expression for the normalized total mass from our accompanying table of parameter values, namely,

Mtot*

=

(μeμc)2(2π)1/2Aηsθi

we find,

Mr

=

Mr*[Kc3/2G3/2ρ01/5]

 

=

Mr*[Kc3/2G3/2]{(μeμc)1/2θi1(KeKc)1/4}1

 

=

Mr*[Kc3/2G3/2(KeKc)1/4](μeμc)1/2θi

Mtot

=

[Kc3/2G3/2(KeKc)1/4](μeμc)1/2θi(μeμc)2(2π)1/2Aηsθi

 

=

[KeKc5G6]1/4(μeμc)3/2(2π)1/2Aηs,

where — again, from our accompanying table of parameter values

θi

=

(1+13ξi2)1/2;

      (0.96077)

ηi

=

(μeμc)3θi2ξi;

      (0.79941)

Λi

=

1ηiξi3;

      (0.96225)

A

=

ηi(1+Λi2)1/2;

      (1.10940)

ηs

=

ηi+π2+tan1(Λi);

      (3.13637)

Mtot[KeKc5G6]1/4

=

(μeμc)3/2(2π)1/2Aηs;

      (2.77623)

ρ0[Ke5Kc5]1/4

=

(μeμc)5/2θi5.

      (1.22153)

Building on Earlier Eigenfunction Details

In the heading of Figure 6 from our accompanying presentation of the properties of marginally unstable oscillation modes in (nc,ne)=(5,1) bipolytropes, we point to the (Excel spreadsheet) "Data File" that contains most of the relevant model details. See specifically,

file = Dropbox/WorkFolder/Wiki edits/BiPolytrope/LinearPerturbation/FaulknerBipolytrope1.xlsx --- worksheet = Mode0Ensemble
file = Dropbox/WorkFolder/Wiki edits/BiPolytrope/LinearPerturbation/FaulknerBipolytrope1.xlsx --- worksheet = Mode0Ensemble
Figure 6: Eigenfunctions Associated with the Fundamental-Mode of Radial Oscillation

in Marginally Unstable Models having Various μe/μc

Relevant Instabilities

Truncated n = 5 Polytrope

In Figure 3 of an accompanying discussion, we show where various turning points lie along the equilibrium sequence of truncated n=5 polytropes.


Figure 3:   Equilibrium Sequences of Pressure-Truncated, n = 5 Polytropic Spheres
(viewed from several different astrophysical perspectives)

ξe External Pressure vs. Volume
(Fixed Mass)
Mass vs. Radius
(Fixed External Pressure)
Mass vs. Central Density
(Fixed External Pressure)
Mass vs. Central Density
(Fixed Radius)
√3 (a)
Pressure-Truncated Isothermal Equilibrium Sequence
Pressure-Truncated Isothermal Equilibrium Sequence
(b)
Pressure-Truncated Isothermal Equilibrium Sequence
Pressure-Truncated Isothermal Equilibrium Sequence
(c)
Pressure-Truncated Isothermal Equilibrium Sequence
Pressure-Truncated Isothermal Equilibrium Sequence
(d)
Pressure-Truncated Isothermal Equilibrium Sequence
Pressure-Truncated Isothermal Equilibrium Sequence
3
√15
9.01
  (23π)3[ξ18(1+ξ23)12]ξ~
vs.

(π23)5/2[ξ15(1+ξ23)9]ξ~

(23π)1/2[ξ3(1+ξ23)2]ξ~
vs.
(32π)1/2[ξ(1+ξ23)1]ξ~
(23π)1/2[ξ3(1+ξ23)2]ξ~
vs.
[(1+ξ23)5/2]ξ~
[233π]1/4[ξ5/2(1+ξ23)3/2]ξ~
vs.
[32π]5/4ξ~5/2


  • KEY RESULT:
    • The maximum "Bonnor-Ebert type" mass and external pressure occurs along the sequence precisely at ξ~=3.
    • It is precisely at this turning point that the equilibrium model is marginally (dynamically) unstable; the eigenfunction is parabolic.
    • For all 3<n<, the location along the relevant sequence presents an analogous turning point whose location and whose eigenfunction is known analytically.

    Bipolytropes with (nc, ne) = (5, 1)

    Sequence Plots

    In Figure 1 of an accompanying discussion, we show — via a plot in the (q,ν) diagram — how the (nc,ne)=(5,1) bipolytrope sequence behaves for various values of the molecular-weight ratio over the range, 14(μe/μc)1.


    Figure 1: Analytically determined plot of fractional core mass (ν) versus fractional core radius (q) for (nc,ne)=(5,1) bipolytrope model sequences having six different values of μe/μc: 1 (blue diamonds), ½ (red squares), 0.345 (dark purple crosses), ⅓ (pink triangles), 0.309 (light green dashes), and ¼ (purple asterisks). Along each of the model sequences, points marked by solid-colored circles correspond to models whose interface parameter, ξi, has one of three values: 0.5 (green circles), 1 (dark blue circles), or 3 (orange circles); the images linked to Table 2 provide plots of the density, pressure and mass profiles for nine of these identified models.

    According to our accompanying discussion, in terms of the parameters,

    iξi3;       and       m33(μeμc),

    the parameter, ν, varies with ξ as,

    νMcoreMtot=(m32i3)(1+i2)1/2[1+(1m3)2i2]1/2[m3i+(1+i2)(π2+tan1Λi)]1.


    • KEY RESULT:  Over the range, 14(μe/μc)13, there is a value of ν above which no equilibrium configurations exist. We have determined the location of this "turning point" by setting, dν/dξ=0; our derived result is,

    (π2+tan1Λi)(1+i2)[3+(1m3)2(2i2)i2]LHS

    =

    m3i[(1m3)i4(m32m3+2)i23]RHS.

    Maximum Fractional Core Mass, ν=Mcore/Mtot (solid green circular markers)
    for Equilibrium Sequences having Various Values of μe/μc

    μeμc

    ξi

    θi

    ηi

    Λi

    A

    ηs

    LHS

    RHS

    qrcoreR

    νMcoreMtot

    Extrema along Various Equilibrium Sequences

    13

    --- --- --- --- --- --- --- 0.0 2π

    0.33

    24.00496 0.0719668 0.0710624 0.2128753 0.0726547 1.8516032 -223.8157 -223.8159 0.038378833 0.52024552

    0.316943

    10.744571 0.1591479 0.1493938 0.4903393 0.1663869 2.1760793 -31.55254 -31.55254 0.068652714 0.382383875

    0.3090

    8.8301772 0.1924833 0.1750954 0.6130669 0.2053811 2.2958639 -18.47809 -18.47808 0.076265588 0.331475715

    14

    4.9379256 0.3309933 0.2342522 1.4179907 0.4064595 2.761622 -2.601255 -2.601257 0.084824137 0.139370157

    Recall that,

    iξi3;       and       m33(μeμc).


    📚 Eggleton, Faulkner, & Cannon (1998) also analytically determined the structure of models along various (nc,ne)=(5,1) sequences; their Figure 1 displays the behavior of ν versus log10 of the interface-to-core density ratio for a range of α(μe/μc)1.

    What Indicates Dynamical Instability?

    KEY RESULT (to be done):  From our original derivation, we have generated a plot intended to replicate Figure 1 from EFC98; then we have marked on each sequence the location of the mass-extremum as determined by our above analytically derived result.

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