2528df0f75
These changes make it unnecessary to copy header files around during the build process, which tends to confuse IDEs and debuggers. The headers which comprise Cantera's external C++ interface are now in the 'include' directory. All of the samples and demos are now in the 'samples' subdirectory.
87 lines
2.5 KiB
Fortran
87 lines
2.5 KiB
Fortran
c
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c Replace this sample main program with your program
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c
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c This program uses functions defined in demo_ftnlib.cpp to create
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c an ideal gas mixture and print some its properties.
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c
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c For a C++ version of this program, see ../cxx/demo.cpp.
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c
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program demo
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implicit double precision (a-h,o-z)
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parameter (MAXSP = 20, MAXRXNS = 100)
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double precision q(MAXRXNS), qf(MAXRXNS), qr(MAXRXNS)
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double precision diff(MAXSP)
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character*80 eq
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character*20 name
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c
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write(*,*)
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write(*,*) '******** Fortran 77 Test Program ********'
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call newIdealGasMix('h2o2.cti','ohmech','Mix')
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t = 1200.0
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p = 101325.0
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call setState_TPX_String(t, p,
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$ 'H2:2, O2:1, OH:0.01, H:0.01, O:0.01')
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c
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write(*,*) 'Initial state properties:'
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write(*,10) temperature(), pressure(), density(),
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$ enthalpy_mole(), entropy_mole(), cp_mole()
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c compute the equilibrium state holding the specific
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c enthalpy and pressure constant
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call equilibrate('HP')
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write(*,*) 'Equilibrium state properties:'
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write(*,10) temperature(), pressure(), density(),
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$ enthalpy_mole(), entropy_mole(), cp_mole()
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10 format(//'Temperature: ',g14.5,' K'/
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$ 'Pressure: ',g14.5,' Pa'/
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$ 'Density: ',g14.5,' kg/m3'/
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$ 'Molar Enthalpy:',g14.5,' J/kmol'/
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$ 'Molar Entropy: ',g14.5,' J/kmol-K'/
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$ 'Molar cp: ',g14.5,' J/kmol-K'//)
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c
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c Reaction information
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c
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irxns = nReactions()
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c forward and reverse rates of progress should be equal
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c in equilibrium states
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call getFwdRatesOfProgress(qf)
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call getRevRatesOfProgress(qr)
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c net rates of progress should be zero in equilibrium states
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call getNetRatesOfProgress(q)
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c for each reaction, print the equation and the rates of progress
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do i = 1,irxns
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call getReactionEqn(i,eq)
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write(*,20) eq,qf(i),qr(i),q(i)
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20 format(a27,3e14.5,' kmol/m3/s')
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end do
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c
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c Transport properties
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c
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dnu = viscosity()
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dlam = thermalConductivity()
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call getMixDiffCoeffs(diff)
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write(*,30) dnu, dlam
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30 format(//'Viscosity: ',g14.5,' Pa-s'/
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$ 'Thermal conductivity: ',g14.5,' W/m/K'/)
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write(*,*) 'Species ',
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$ ' Diffusion Coefficient'
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nsp = nSpecies()
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do k = 1, nsp
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call getSpeciesName(k, name)
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write(*,40) name, diff(k)
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40 format(' ',a20,e14.5,' m2/s')
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end do
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stop
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end
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