R507A
98.86           {molecular weight}
0 {not used}
30.72180         {a} Liquid density=a+b*Tz^(1/3)+c*Tz^(2/3)+d*Tz+e*Tz^(4/3)
55.94335         {b}  +f*sqrt(Tz)+g*(Tz)^2}
18.01589         {c}     where Tz=(1-T/Tc) and Liquid Density[=]lbm/ft3
10.27205         {d}
0                {e}
0                {f}
0                {g}
-5957.1          {a}  Vapor pressure fit: lnP=a/T+b+cT+d(1-T/Tc)^1.5+eT^2
23.18835         {b}     where T[=]R and P[=]psia
-1.9393E-02      {c}
-5.2838E-02      {d}
1.2331E-05       {e}
0                {not used}
0.10859          {Gas constant in psia-ft3/lbm-R}
5.93667e-3       {b}  Constants for Martin-Hou EOS/English_units
-4.81511         {A2}
2.97383e-3       {B2}
-92.67646        {C2}
0.182139         {A3}
-1.76298E-4      {B3}
2.71787          {C3}
-1.06353E-3      {A4}
0                {B4}
0                {C4}
0                {A5}
9.9630e-9        {B5}
-1.86041e-5      {C5}
0                {A6}
0                {B6}
0                {C6}
5.475            {Bexp - Martin-Hou exponential constant}
0                {alpha}
0                {C'}
0.03040183       {a}   Cv(0 pressure) = a + b T + c T^2 + d T^3 + e/T^2
3.327499E-04     {b}           where T[=]R and Cv[=]Btu/lb-R
-8.508630E-08    {c}
0                {d}
0                {e}
35.85053         {href offset}
-0.1322604       {sref offset}
538.8            {Pc [=] psia}
619.0            {Tc [=] R} 
0.03253          {vc [=] ft3/lbm}
0                {not used}
0                {not used}
2                {Viscosity correlation type: set to 2: do not change}
200              {Lower limit of gas viscosity correlation in K}
600 {Upper limit of gas viscosity correlation in K}
-1.234153E06     {A}    GasViscosity*1E12=A+B*T+C*T^2+D*T^3 
4.951639E04       {B}    where T[=]K and GasViscosity[=]N-s/m2
-1.555160E01     {C}
0                {D}
200              {Lower limit of liquid viscosity correlation in K}
340 {Upper limit of liquid viscosity correlation in K}
5.350956E03      {A}   Liquid Viscosity*1E6=A+B*T+C*T^2+D*T^3
-4.806398E01     {B}    where T[=]K and Liquid Viscosity[=]N-s/m2
1.517747E-01     {C}
-1.654794E-4     {D}
2                {Conductivity correlation type: set to 2: do not change}
200              {Lower limit of gas conductivity correlation in K} 
600 {Upper limit of gas conductivity correlation in K}
-3.729331E-03    {A}   GasConductivity=A+B*T+C*T^2+D*T^3
3.734391E-05     {B}    where T[=]K and GasConductivity[=]W/m-K
8.074898E-08     {C}
0                {D} 
200              {Lower limit of liquid conductivity correlation in K}
340 {Upper limit of liquid conductivity correlation in K}
2.283220E-01     {A}   LiquidConductivity=A+B*T+C*T^2+D*T^3
-6.804445E-04    {B}    where T[=]K and LiquidConductivity[=]W/m-K
4.580030E-07     {C}
0   {D}
0 {not use: terminator}
