Skip to content

Test/legacy #84

New issue

Have a question about this project? Sign up for a free GitHub account to open an issue and contact its maintainers and the community.

Sign up for GitHub

By clicking “Sign up for GitHub”, you agree to our terms of service and privacy statement. We’ll occasionally send you account related emails.

Already on GitHub? Sign in to your account

Merged
markleader merged 5 commits into from
May 20, 2026
Merged

Test/legacy #84

Show file tree
Hide file tree
Changes from all commits
Commits
Show all changes
5 commits
Select commit Hold shift + click to select a range
bad4f4f
updated test formatting to output long
markleader May 18, 2026
ff92b03
updated frozen formatting
markleader May 19, 2026
55ed571
switched example2 to use long formatting
markleader May 20, 2026
8662b66
updated docs
markleader May 20, 2026
0676b0a
fixed line length CI failures
markleader May 20, 2026
File filter

Filter by extension

Filter by extension
Conversations
Failed to load comments.
Loading
Jump to
Jump to file
Failed to load files.
Loading
Diff view
Diff view
2 changes: 2 additions & 0 deletions AGENTS.md
View file
Open in desktop
Original file line number Diff line number Diff line change
Expand Up @@ -9,6 +9,8 @@ This repository is a scientific computing library (CEA). Follow these rules:
- Keep changes small and focused; avoid drive-by formatting or whitespace churn.
- In Fortran source files, keep lines within the default free-form GNU limit (target `<= 132`
characters) so CI builds that do not pass `-ffree-line-length-none` do not fail.
- Before finishing Fortran edits, check touched files for overlong lines with
`rg -n '.{133,}' path/to/file.f90`.
- Maintain backward compatibility for the legacy user base.
- If numerical behavior might change, call it out and add validation or tests when possible.
- Respect layer boundaries: Fortran core in `source/`, C bindings in `source/bind/c/`,
Expand Down
5 changes: 3 additions & 2 deletions docs/source/developer_guide.rst
View file
Open in desktop
Original file line number Diff line number Diff line change
Expand Up @@ -151,8 +151,9 @@ whenever you modify solver behavior.

* **Integration harness** – ``test/main_interface/test_main.py`` re-runs the
original RP‑1311 problems and compares the generated ``*.out`` files against
reference outputs. Ensure the ``cea`` executable is on ``PATH`` or adjust the
``run_dir`` variable near the top of the script before running::
reference outputs. Ensure the ``cea`` executable is on ``PATH``, set
``CEA_EXE`` or ``CEA_RUN_DIR``, or build ``build*/source/cea`` in this
checkout before running::

python test/main_interface/test_main.py

Expand Down
7 changes: 1 addition & 6 deletions docs/source/installation.rst
View file
Open in desktop
Original file line number Diff line number Diff line change
Expand Up @@ -271,12 +271,7 @@ Validation checks:
cd build-intel\source
python ..\..\test\main_interface\test_main.py

Expected result for this check is 13 out of 14 passing, with a small error on
example 11::

Reference | Test | Rel. Error
--------------------------------------------------------------
F- : 2.5000e-04 | 2.6000e-04 | 4.000%
Expected result for this check is 14/14 passing.

* Python binding tests (from the CEA root)::

Expand Down
3 changes: 3 additions & 0 deletions source/input.f90
View file
Open in desktop
Original file line number Diff line number Diff line change
Expand Up @@ -117,6 +117,8 @@ module cea_input
!! Dataset containing the output options
real(dp), allocatable :: trace
!! Only output species with concentrations greater than `trace`
logical :: long = .false.
!! Print extra-precision numeric output
logical :: transport = .false.
!! Optional flag to calculate mixture transport properties
logical :: mass_fractions = .false.
Expand Down Expand Up @@ -723,6 +725,7 @@ function parse_outp(buffer) result(output)
! Four letter keywords
match = .true.
select case(token(:4))
case('long'); output%long = .true.
case('tran'); output%transport = .true.
case('trac'); output%trace = scanner%read_real()
case default
Expand Down
1,405 changes: 1,090 additions & 315 deletions source/main.f90
View file
Open in desktop

Large diffs are not rendered by default.

2 changes: 1 addition & 1 deletion test/main_interface/example1.inp
View file
Open in desktop
Original file line number Diff line number Diff line change
Expand Up @@ -20,6 +20,6 @@
only Ar C CO CO2 H H2 H2O HNO HO2 HNO2 HNO3 N NH
NO N2 N2O3 O O2 OH O3
# 'output' dataset:
output calories
output calories long
# 'end' dataset
end
2 changes: 1 addition & 1 deletion test/main_interface/example10.inp
View file
Open in desktop
Original file line number Diff line number Diff line change
Expand Up @@ -10,5 +10,5 @@ reac fuel = H2(L) t,k= 20.27
oxid = O2(L) t,k= 90.17
problem o/f=5.55157 case=10 rocket fac p,bar=53.3172 ma=1333.9
pi/p=10,100,1000, sup-ae/at=25,50,75
output short
output long
end
2 changes: 1 addition & 1 deletion test/main_interface/example11.inp
View file
Open in desktop
Original file line number Diff line number Diff line change
Expand Up @@ -15,5 +15,5 @@ reac fuel = Li(cr) moles= 1. t(k)=298.15
oxid = F2(L) moles= .5556 t(k)=85.02
prob case=11 rocket equilibrium p,psia=1000 ions
pi/p=68.0457, sub,ae/at=10, sup,ae/at=10,20,100
output siunits transport
output siunits transport long
end
2 changes: 1 addition & 1 deletion test/main_interface/example12.inp
View file
Open in desktop
Original file line number Diff line number Diff line change
Expand Up @@ -19,5 +19,5 @@ prob rocket case=12 p,psia =1000, pi/p=68.0457, eql frozen nfz=2
supersonic=5,10,25,50,75,100,150,200, o/f= 2.5,
only CO CO2 H HNO HO2 H2 H2O H2O2 N NO NO2
N2 N2O O OH O2 HCO NH CH4 NH2 NH3 H2O(L) C(gr)
output siunits massf plot aeat t p ivac isp mach cf
output siunits massf long
end
2 changes: 1 addition & 1 deletion test/main_interface/example13.inp
View file
Open in desktop
Original file line number Diff line number Diff line change
Expand Up @@ -18,6 +18,6 @@ reac fuel = N2H4(L) wt%= 80 t=298.15
oxid = H2O2(L) wt%=100 t=298.15
prob rocket case=13 p,psia=3000, pi/p=3,10,30,300,equilibrium %fuel = 67.

outp trace= 1.e-10 calories
outp trace= 1.e-10 calories long
insert BeO(L)
end
2 changes: 1 addition & 1 deletion test/main_interface/example14.inp
View file
Open in desktop
Original file line number Diff line number Diff line change
Expand Up @@ -17,6 +17,6 @@ reac name H2(L) moles=100
prob tp p,atm=.05 case=14
t,k = 1000,500,350,305,304.3,304.2,304,300,

output siunits debug
output siunits long

end
2 changes: 1 addition & 1 deletion test/main_interface/example2.inp
View file
Open in desktop
Original file line number Diff line number Diff line change
Expand Up @@ -15,5 +15,5 @@
prob case=Example-2 phi,eq.ratio=1, tv t(k)=3000
rho,g/cc=9.1864d-05,8.0877d-06,6.6054d-07
only Ar C CO CO2 H H2 H2O HNO HO2 HNO2 HNO3 N NH NO N2 N2O3 O O2 OH O3
outp transport calories
outp transport calories long
end
2 changes: 1 addition & 1 deletion test/main_interface/example3.inp
View file
Open in desktop
Original file line number Diff line number Diff line change
Expand Up @@ -19,7 +19,7 @@ reac
fuel C7H8(L) wtfrac= .4 t(k)= 298.15
fuel C8H18(L),n-octa wtfrac= .6 t(k)= 298.15
prob case=Example-3 hp p(bar)=100,10,1, o/f = 17
output siunits trace=1.e-15
output siunits trace=1.e-15 long

omit CCN CNC C2N2 C2O
C3H4,allene C3H4,propyne C3H4,cyclo- C3
Expand Down
2 changes: 1 addition & 1 deletion test/main_interface/example4.inp
View file
Open in desktop
Original file line number Diff line number Diff line change
Expand Up @@ -16,7 +16,7 @@

prob case=Example-4, o/f=17 uv u/r=-45.1343, rho,kg/m**3=14.428

output trace=1.e-15
output trace=1.e-15 long

reac oxid Air wtfrac= 1 t(k)=700.0
fuel C7H8(L) wtfrac= .4 t(k)= 298.15
Expand Down
2 changes: 1 addition & 1 deletion test/main_interface/example5.inp
View file
Open in desktop
Original file line number Diff line number Diff line change
Expand Up @@ -24,7 +24,7 @@ reac

prob case=5, hp p,psia=500,250,125,50,5,

outp calories
outp calories long

omit COOH C2 C2H CHCO,ketyl C2H2,vinylidene CH2CO,ketene C2H3,vinyl
CH3CO,acetyl C2H4O,ethylen-o CH3CHO,ethanal CH3COOH (HCOOH)2
Expand Down
2 changes: 1 addition & 1 deletion test/main_interface/example6.inp
View file
Open in desktop
Original file line number Diff line number Diff line change
Expand Up @@ -12,5 +12,5 @@ reac oxid O2 wt%=100

prob detonation case=6 t=298.15,500, r,e=1, pbar=1,20

output calories transport
output calories transport long
end
1 change: 1 addition & 0 deletions test/main_interface/example7.inp
View file
Open in desktop
Original file line number Diff line number Diff line change
Expand Up @@ -22,5 +22,6 @@ reac name= H2 moles= 0.050 t(k) 300.00

problem case=7 p,mmhg=10, shock u1=1100,1200,1250,1300,1350,1400,
incd refl eql
output long

end
2 changes: 1 addition & 1 deletion test/main_interface/example8.inp
View file
Open in desktop
Original file line number Diff line number Diff line change
Expand Up @@ -15,5 +15,5 @@ case=8 p,bar=53.3172 subar=1.58,pi/p=10,100,1000,supar=25,50,75
reactants
fuel = H2(L) wt% 100. t(k) 20.27
oxid = O2(L) wt% 100. t(k) 90.17
output siunits
output siunits long
end
2 changes: 1 addition & 1 deletion test/main_interface/example9.inp
View file
Open in desktop
Original file line number Diff line number Diff line change
Expand Up @@ -8,5 +8,5 @@ reac fuel = H2(L) wt%=100. t,k= 20.27
oxid = O2(L) wt%=100. t,k= 90.17
problem o/f=5.55157 case=9 rocket fac p,bar=53.3172 acat=1.58
pi/p=10,100,1000, supar=25,50,75
output siunits
output siunits long
end
120 changes: 60 additions & 60 deletions test/main_interface/reference_output/example1.out
View file
Open in desktop
Original file line number Diff line number Diff line change
Expand Up @@ -31,7 +31,7 @@
only Ar C CO CO2 H H2 H2O HNO HO2 HNO2 HNO3 N NH
NO N2 N2O3 O O2 OH O3
# 'output' dataset:
output calories
output calories long
# 'end' dataset
end

Expand Down Expand Up @@ -102,43 +102,43 @@

REACTANT MOLES ENERGY TEMP
CAL/MOL K
FUEL H2 1.0000000 0.000 0.000
OXIDANT Air 1.0000000 0.000 0.000
FUEL H2 0.100000000000000E+01 0.000000000000000E+00 0.000000000000000E+00
OXIDANT Air 0.100000000000000E+01 0.000000000000000E+00 0.000000000000000E+00

O/F= 34.29623 %FUEL= 2.833164 R,EQ.RATIO= 1.000000 PHI,EQ.RATIO= 1.000000
O/F= 0.342962255762164E+02 %FUEL= 0.283316412357085E+01 R,EQ.RATIO= 0.100000000000000E+01 PHI,EQ.RATIO= 0.100000000000000E+01

THERMODYNAMIC PROPERTIES

P, ATM 1.0000 1.0000 0.10000 0.10000 0.01000 0.01000
T, K 3000.00 2000.00 3000.00 2000.00 3000.00 2000.00
RHO, G/CC 9.1781-5 1.4989-4 8.0851-6 1.4955-5 6.6136-7 1.4875-6
H, CAL/G 663.71 -203.57 1369.55 -191.83 2647.10 -164.35
U, CAL/G 399.86 -365.13 1070.02 -353.76 2280.92 -327.16
G, CAL/G -7974.53 -5290.41 -8616.70 -5662.79 -9380.96 -6036.51
S, CAL/(G)(K) 2.8794 2.5434 3.3287 2.7355 4.0094 2.9361

M, (1/n) 22.594 24.600 19.903 24.544 16.281 24.412
(dLV/dLP)t -1.03442 -1.00064 -1.07867 -1.00146 -1.07479 -1.00358
(dLV/dLT)p 1.6957 1.0205 2.5333 1.0463 2.4133 1.1111
Cp, CAL/(G)(K) 1.6816 0.4552 3.4398 0.5215 3.7168 0.6858
GAMMAs 1.1312 1.2258 1.1206 1.2026 1.1318 1.1668
SON VEL,M/SEC 1117.5 910.3 1185.1 902.7 1316.8 891.5
P, ATM 0.100000000000000E+01 0.100000000000000E+01 0.100000000000000E+00 0.100000000000000E+00 0.100000000000000E-01 0.100000000000000E-01
T, K 0.300000000000000E+04 0.200000000000000E+04 0.300000000000000E+04 0.200000000000000E+04 0.300000000000000E+04 0.200000000000000E+04
RHO, G/CC 0.917812621293807E-04 0.149894595170280E-03 0.808510859638209E-05 0.149553263878203E-04 0.661356498135516E-06 0.148746292064736E-05
H, CAL/G 0.663714183578615E+03 -0.203568685337744E+03 0.136954555459015E+04 -0.191833302894158E+03 0.264709897503511E+04 -0.164346463524677E+03
U, CAL/G 0.399855791873225E+03 -0.365130589465363E+03 0.107001641499410E+04 -0.353763946105474E+03 0.228092345120761E+04 -0.327155605708938E+03
G, CAL/G -0.797452759742554E+04 -0.529041249258461E+04 -0.861669930180933E+04 -0.566278878289383E+04 -0.938096063061102E+04 -0.603650927028784E+04
S, CAL/(G)(K) 0.287941392700138E+01 0.254342190362343E+01 0.332874828546649E+01 0.273547773999984E+01 0.400935320188204E+01 0.293608140338158E+01

M, (1/n) 0.225941146347108E+02 0.246000515270515E+02 0.199033949002827E+02 0.245440337142454E+02 0.162808444628060E+02 0.244115969964997E+02
(dLV/dLP)t -0.103441815622627E+01 -0.100063813453150E+01 -0.107867136959018E+01 -0.100146307345148E+01 -0.107479373388823E+01 -0.100357882925661E+01
(dLV/dLT)p 0.169574002221235E+01 0.102048076119156E+01 0.253331253467799E+01 0.104625100786942E+01 0.241332728794386E+01 0.111105039779104E+01
Cp, CAL/(G)(K) 0.168164195514646E+01 0.455164675773621E+00 0.343981135329078E+01 0.521493450222716E+00 0.371682316613401E+01 0.685772576619565E+00
GAMMAs 0.113119264857728E+01 0.122576408700420E+01 0.112058161585125E+01 0.120262736325115E+01 0.113182120989164E+01 0.116679909443605E+01
SON VEL,M/SEC 0.111750527143068E+04 0.910266931802762E+03 0.118505122626197E+04 0.902663535784243E+03 0.131682907734308E+04 0.891524481797701E+03

MOLE FRACTIONS

*Ar 0.00710 0.00773 0.00625 0.00771 0.00511 0.00767
*CO 0.00017 0.00001 0.00018 0.00002 0.00017 0.00004
*CO2 0.00007 0.00025 0.00003 0.00024 0.00001 0.00022
*H 0.04075 0.00009 0.14289 0.00041 0.31894 0.00186
HO2 0.00001 0.00000 0.00001 0.00000 0.00000 0.00000
*H2 0.06728 0.00306 0.08272 0.00638 0.04121 0.01319
H2O 0.20730 0.34207 0.09579 0.33714 0.01176 0.32637
*N 0.00001 0.00000 0.00003 0.00000 0.00009 0.00000
*NO 0.01230 0.00048 0.01371 0.00072 0.00967 0.00107
*N2 0.58568 0.64414 0.51448 0.64255 0.42158 0.63891
*O 0.01540 0.00002 0.05787 0.00010 0.14261 0.00047
*OH 0.04517 0.00113 0.05953 0.00244 0.03275 0.00519
*O2 0.01876 0.00102 0.02650 0.00228 0.01610 0.00502
*Ar 0.709816168298838E-02 0.772834654634775E-02 0.625284597753980E-02 0.771074800312285E-02 0.511478636283127E-02 0.766914171424681E-02
*CO 0.170734699895957E-03 0.103652260012927E-04 0.184174247734782E-03 0.209646651543597E-04 0.167756369387483E-03 0.408099814984045E-04
*CO2 0.710766502091342E-04 0.252885446533626E-03 0.288164481365696E-04 0.241686548192804E-03 0.646860122044504E-05 0.220423996808562E-03
*H 0.407521751641015E-01 0.895230172377970E-04 0.142894604224462E+00 0.408861803988751E-03 0.318941379135650E+00 0.185850428610297E-02
HO2 0.102569476988717E-04 0.100675295867698E-06 0.508037714881123E-05 0.102660581561951E-06 0.688700854843523E-06 0.102434581893782E-06
*H2 0.672773710148948E-01 0.306069048082573E-02 0.827178184043327E-01 0.638414984289808E-02 0.412087221569157E-01 0.131909819121077E-01
H2O 0.207295734187503E+00 0.342065042022239E+00 0.957914645779614E-01 0.337141209059766E+00 0.117607956590043E-01 0.326372696152164E+00
*N 0.105766801113053E-04 0.000000000000000E+00 0.313477645283984E-04 0.000000000000000E+00 0.897351576333643E-04 0.000000000000000E+00
*NO 0.123032417467299E-01 0.483447373852851E-03 0.137051297873082E-01 0.721494871875827E-03 0.966849822741609E-02 0.106592614945457E-02
*N2 0.585675961934690E+00 0.644136505597660E+00 0.514483914307004E+00 0.642550141059361E+00 0.421583795217339E+00 0.638908853919665E+00
*O 0.153969589793058E-01 0.212526105804491E-04 0.578683837746873E-01 0.100422671973736E-03 0.142613673933793E+00 0.470500076973319E-03
*OH 0.451741771670702E-01 0.112847719252238E-02 0.595335355526772E-01 0.243530916723217E-02 0.327473776364973E-01 0.518643639628951E-02
*O2 0.187606408986537E-01 0.102336381090258E-02 0.265008900064277E-01 0.228490964585316E-02 0.160953375734713E-01 0.501562298010663E-02

* THERMODYNAMIC PROPERTIES FITTED TO 20000.K

Expand Down Expand Up @@ -192,42 +192,42 @@

REACTANT MOLES ENERGY TEMP
CAL/MOL K
FUEL H2 1.0000000 0.000 0.000
OXIDANT Air 1.0000000 0.000 0.000
FUEL H2 0.100000000000000E+01 0.000000000000000E+00 0.000000000000000E+00
OXIDANT Air 0.100000000000000E+01 0.000000000000000E+00 0.000000000000000E+00

O/F= 22.85255 %FUEL= 4.192424 R,EQ.RATIO= 1.500000 PHI,EQ.RATIO= 1.500761
O/F= 0.228525500680035E+02 %FUEL= 0.419242385887046E+01 R,EQ.RATIO= 0.150000000000000E+01 PHI,EQ.RATIO= 0.150076142374305E+01

THERMODYNAMIC PROPERTIES

P, ATM 1.0000 1.0000 0.10000 0.10000 0.01000 0.01000
T, K 3000.00 2000.00 3000.00 2000.00 3000.00 2000.00
RHO, G/CC 8.1217-5 1.2975-4 7.1159-6 1.2964-5 5.6716-7 1.2929-6
H, CAL/G 718.65 -120.70 1550.12 -116.20 3208.24 -101.78
U, CAL/G 420.48 -307.35 1209.80 -303.01 2781.24 -289.09
G, CAL/G -8818.84 -5830.65 -9545.38 -6260.58 -10424.5 -6691.18
S, CAL/(G)(K) 3.1792 2.8550 3.6985 3.0722 4.5442 3.2947

M, (1/n) 19.994 21.293 17.518 21.275 13.962 21.219
(dLV/dLP)t -1.03310 -1.00019 -1.08571 -1.00061 -1.08710 -1.00198
(dLV/dLT)p 1.6653 1.0055 2.6677 1.0177 2.6421 1.0570
Cp, CAL/(G)(K) 1.8253 0.4671 4.1929 0.5000 4.9230 0.6077
GAMMAs 1.1337 1.2529 1.1196 1.2389 1.1296 1.2051
SON VEL,M/SEC 1189.3 989.2 1262.6 984.0 1420.6 971.8
P, ATM 0.100000000000000E+01 0.100000000000000E+01 0.100000000000000E+00 0.100000000000000E+00 0.100000000000000E-01 0.100000000000000E-01
T, K 0.300000000000000E+04 0.200000000000000E+04 0.300000000000000E+04 0.200000000000000E+04 0.300000000000000E+04 0.200000000000000E+04
RHO, G/CC 0.812173143904981E-04 0.129745591790122E-03 0.711591632569365E-05 0.129637038187800E-04 0.567158839824901E-06 0.129290278301783E-05
H, CAL/G 0.718653808576990E+03 -0.120698095997679E+03 0.155012209146243E+04 -0.116203979745566E+03 0.320823530763757E+04 -0.101779054848083E+03
U, CAL/G 0.420475317994169E+03 -0.307349957382867E+03 0.120979689501925E+04 -0.303012136987376E+03 0.278124282310491E+04 -0.289088236421831E+03
G, CAL/G -0.881884186048532E+04 -0.583064751364366E+04 -0.954537720523993E+04 -0.626057527709261E+04 -0.104244883221843E+05 -0.669118354541482E+04
S, CAL/(G)(K) 0.317916522302077E+01 0.285497470882299E+01 0.369849976556745E+01 0.307218564867352E+01 0.454424120994063E+01 0.329470224528337E+01

M, (1/n) 0.199935506342839E+02 0.212932843897338E+02 0.175175003550387E+02 0.212754690428394E+02 0.139619477285345E+02 0.212185603127157E+02
(dLV/dLP)t -0.103309534560990E+01 -0.100019301198473E+01 -0.108570593271089E+01 -0.100061377011298E+01 -0.108709935309546E+01 -0.100197661412765E+01
(dLV/dLT)p 0.166528253467781E+01 0.100554807193872E+01 0.266772264522350E+01 0.101765387665438E+01 0.264211948314090E+01 0.105696147348021E+01
Cp, CAL/(G)(K) 0.182531131405844E+01 0.467073891057589E+00 0.419285001657417E+01 0.500033855333494E+00 0.492302741773693E+01 0.607650874442986E+00
GAMMAs 0.113367190213984E+01 0.125288168249786E+01 0.111962607340458E+01 0.123890450353045E+01 0.112959134911697E+01 0.120512065959483E+01
SON VEL,M/SEC 0.118926239177003E+04 0.989161103658609E+03 0.126263955852735E+04 0.984039817891623E+03 0.142058306259463E+04 0.971830750719187E+03

MOLE FRACTIONS

*Ar 0.00619 0.00660 0.00543 0.00659 0.00432 0.00657
*CO 0.00018 0.00016 0.00017 0.00016 0.00014 0.00016
*CO2 0.00004 0.00007 0.00002 0.00007 0.00000 0.00007
*H 0.06025 0.00062 0.18236 0.00196 0.39312 0.00616
*H2 0.14706 0.14737 0.13472 0.14676 0.06261 0.14490
H2O 0.22224 0.29508 0.11131 0.29450 0.01465 0.29261
*N 0.00001 0.00000 0.00003 0.00000 0.00008 0.00000
*NO 0.00565 0.00001 0.00912 0.00003 0.00729 0.00008
*N2 0.51356 0.54995 0.44786 0.54948 0.35692 0.54799
*O 0.00755 0.00000 0.04129 0.00000 0.11694 0.00004
*OH 0.03276 0.00014 0.05421 0.00044 0.03310 0.00140
*O2 0.00451 0.00000 0.01349 0.00000 0.01082 0.00003
*Ar 0.619330246618960E-02 0.659591450941935E-02 0.542630871998807E-02 0.659039593829884E-02 0.432492291493436E-02 0.657276760478928E-02
*CO 0.175190756075451E-03 0.156340777252111E-03 0.166274414556434E-03 0.156104432265937E-03 0.142804783447023E-03 0.155386981247444E-03
*CO2 0.357717091369873E-04 0.683358622057218E-04 0.185619422696420E-04 0.683842280989678E-04 0.451506811511677E-05 0.685012051837119E-04
*H 0.602500539693314E-01 0.621205940805260E-03 0.182358411074645E+00 0.196032574879748E-02 0.393120651636903E+00 0.615959766215006E-02
*H2 0.147055845524443E+00 0.147374108707591E+00 0.134715947789133E+00 0.146759586548831E+00 0.626064574408741E-01 0.144895427901074E+00
H2O 0.222242438266501E+00 0.295081391337003E+00 0.111309747576018E+00 0.294504146511820E+00 0.146506494969705E-01 0.292605499134671E+00
*N 0.990409681232854E-05 0.000000000000000E+00 0.292477160435377E-04 0.000000000000000E+00 0.825665450457386E-04 0.000000000000000E+00
*NO 0.565078017468001E-02 0.800303404532638E-05 0.912336352518845E-02 0.253532583919663E-04 0.729441882587025E-02 0.805719884455148E-04
*N2 0.513556703997124E+00 0.549953701156226E+00 0.447860297620834E+00 0.549484895657109E+00 0.356916703704554E+00 0.547987461632437E+00
*O 0.755193619588055E-02 0.380753264353796E-06 0.412883757504629E-01 0.381599624552440E-05 0.116936841625268E+00 0.384017314821275E-04
*OH 0.327582161699072E-01 0.140289454422610E-03 0.542073391771396E-01 0.443692383511082E-03 0.330964727124708E-01 0.140297180259942E-02
*O2 0.451330182498275E-02 0.328467765979748E-06 0.134906647646800E-01 0.329929662955117E-05 0.108213258098901E-01 0.334123559200457E-04

* THERMODYNAMIC PROPERTIES FITTED TO 20000.K

Expand Down
Loading
Loading