[3008] | 1 | MODULE massflowrateco2_mod |
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| 2 | |
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| 3 | IMPLICIT NONE |
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| 4 | |
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| 5 | CONTAINS |
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| 6 | |
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[2389] | 7 | subroutine massflowrateco2(P,T,Sat,Radius,Matm,Ic) |
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| 8 | !======================================================================================================================! |
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| 9 | ! Determination of the mass transfer rate for CO2 condensation sublimation |
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| 10 | ! |
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| 11 | ! inputs: Pressure (P), Temperature (T), saturation ratio (Sat), particle radius (Radius), molecular mass of the atm |
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| 12 | ! (Matm) |
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| 13 | ! output: MASS FLUX Ic |
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| 14 | ! |
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| 15 | ! Authors: C. Listowski (2014), J. Audouard (2016-2017), Christophe Mathé (2020) |
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| 16 | ! |
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| 17 | ! Updates: |
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| 18 | ! -------- |
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| 19 | ! December 2017 - C. Listowski - Simplification of the derivation of massflowrate by using explicit formula for |
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| 20 | ! surface temperature, No Newton-Raphson routine anymore- see comment at relevant line |
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| 21 | !======================================================================================================================! |
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| 22 | use comcstfi_h, only: pi |
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| 23 | |
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| 24 | implicit none |
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| 25 | |
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| 26 | !----------------------------------------------------------------------------------------------------------------------! |
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| 27 | ! VARIABLES DECLARATION |
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| 28 | !----------------------------------------------------------------------------------------------------------------------! |
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| 29 | ! Input arguments: |
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| 30 | !----------------- |
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| 31 | real, intent(in) :: & |
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| 32 | P, & |
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| 33 | T, & |
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| 34 | Matm |
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| 35 | |
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| 36 | real(kind=8), intent(in) :: & |
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| 37 | SAT |
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| 38 | |
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| 39 | double precision, intent(in) :: & |
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| 40 | Radius |
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| 41 | !----------------------------------------------------------------------------------------------------------------------! |
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| 42 | ! Output arguments: |
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| 43 | !------------------ |
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| 44 | double precision, intent(out) :: & |
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| 45 | Ic |
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| 46 | !----------------------------------------------------------------------------------------------------------------------! |
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| 47 | ! Local: |
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| 48 | !------- |
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| 49 | double precision :: & |
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| 50 | Ak, & |
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| 51 | C0, & |
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| 52 | C1, & |
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| 53 | C2, & |
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| 54 | kmix, & |
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| 55 | Lsub, & |
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| 56 | cond, & |
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| 57 | Tsurf |
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| 58 | !======================================================================================================================! |
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| 59 | ! BEGIN ===============================================================================================================! |
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| 60 | !======================================================================================================================! |
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| 61 | call coefffunc(P,T,Sat,Radius,Matm,kmix,Lsub,C0,C1,C2,Ak) |
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| 62 | |
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| 63 | Tsurf = 1./C1*dlog(Sat/Ak) + T |
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| 64 | |
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| 65 | ! Note by CL - dec 2017 (see also technical note) |
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| 66 | ! The above is a simplified version of Tsurf compared to the one used by Listowski et al. 2014 (Ta), where a |
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| 67 | ! Newton-Raphson routine must be used. Approximations made by considering the orders of magnitude of the different |
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| 68 | ! factors lead to simplification of the equation 5 of Listowski et al. (2014). |
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| 69 | ! The error compared to the exact value determined by NR iterations is less than 0.6% for all sizes, pressures, |
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| 70 | ! supersaturations relevant to present Mars. Should also be ok for most conditions in ancient Mars (However, needs to |
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| 71 | ! end subroutine massflowrateco2 be double-cheked, as explained in (Listowski et al. 2013,JGR) |
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| 72 | |
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| 73 | cond = 4.* pi * Radius * kmix |
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| 74 | Ic = cond * (Tsurf-T) / Lsub |
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| 75 | !======================================================================================================================! |
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| 76 | ! END =================================================================================================================! |
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| 77 | !======================================================================================================================! |
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| 78 | end subroutine massflowrateco2 |
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| 79 | |
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| 80 | !______________________________________________________________________________________________________________________! |
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| 81 | !______________________________________________________________________________________________________________________! |
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| 82 | !______________________________________________________________________________________________________________________! |
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| 83 | |
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| 84 | |
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| 85 | subroutine coefffunc(P,T,S,rc,Matm,kmix,Lsub,C0,C1,C2,Ak) |
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| 86 | !======================================================================================================================! |
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| 87 | ! Defini la fonction eq 6 papier 2014 (Listowski et al., 2014) |
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| 88 | !======================================================================================================================! |
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| 89 | use tracer_mod, only: rho_ice_co2 |
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| 90 | use comcstfi_h, only: pi |
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[3008] | 91 | use microphys_h, only: kbz, mco2, nav, rgp, sigco2 |
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[2389] | 92 | |
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| 93 | implicit none |
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[3008] | 94 | |
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[2389] | 95 | !----------------------------------------------------------------------------------------------------------------------! |
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| 96 | ! VARIABLES DECLARATION |
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| 97 | !----------------------------------------------------------------------------------------------------------------------! |
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| 98 | ! Input arguments: |
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| 99 | !----------------- |
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| 100 | real, intent(in) :: & |
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| 101 | P, & |
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| 102 | T, & |
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| 103 | Matm ! g.mol-1 ( = mmean(ig,l) ) |
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| 104 | |
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| 105 | real(kind=8), intent(in) :: & |
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| 106 | S |
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| 107 | |
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| 108 | double precision, intent(in) :: & |
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| 109 | rc |
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| 110 | !----------------------------------------------------------------------------------------------------------------------! |
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| 111 | ! Output arguments: |
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| 112 | !------------------ |
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| 113 | double precision, intent(out) :: & |
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| 114 | C0, & |
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| 115 | C1, & |
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| 116 | C2, & |
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| 117 | kmix, & |
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| 118 | Lsub |
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| 119 | !----------------------------------------------------------------------------------------------------------------------! |
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| 120 | ! Local: |
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| 121 | !------- |
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| 122 | double precision :: & |
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| 123 | Cpatm, & |
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| 124 | Cpn2, & |
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| 125 | Cpco2, & |
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| 126 | Dv, & |
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| 127 | psat, & |
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| 128 | xinf, & |
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| 129 | pco2, & |
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| 130 | l0, & |
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| 131 | l1, & |
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| 132 | l2, & |
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| 133 | l3, & |
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| 134 | l4, & |
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| 135 | Ak, & ! kelvin factor |
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| 136 | !----F and S correction |
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| 137 | knudsen,& |
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| 138 | a, & |
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| 139 | lambda, & |
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| 140 | !----For Kn,th |
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| 141 | vthatm, & |
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| 142 | lpmt, & |
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| 143 | rhoatm, & |
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| 144 | vthco2 |
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| 145 | !----------------------------------------------------------------------------------------------------------------------! |
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| 146 | ! DEFINE heat cap. J.kg-1.K-1 and To |
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| 147 | data Cpco2/0.7e3/ |
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| 148 | data Cpn2/1e3/ |
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| 149 | !======================================================================================================================! |
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| 150 | ! BEGIN ===============================================================================================================! |
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| 151 | !======================================================================================================================! |
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| 152 | kmix = 0d0 |
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| 153 | Lsub = 0d0 |
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| 154 | |
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| 155 | C0 = 0d0 |
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| 156 | C1 = 0d0 |
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| 157 | C2 = 0d0 |
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| 158 | |
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| 159 | ! Equilibirum pressure over a flat surface |
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| 160 | psat = 1.382 * 1.00e12 * exp(-3182.48/dble(T)) ! (Pa) |
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| 161 | |
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| 162 | ! Compute transport coefficient |
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| 163 | pco2 = psat * dble(S) |
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| 164 | |
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| 165 | ! Latent heat of sublimation if CO2 co2 (J.kg-1) version Azreg_Ainou (J/kg) : |
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| 166 | l0=595594. |
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| 167 | l1=903.111 |
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| 168 | l2=-11.5959 |
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| 169 | l3=0.0528288 |
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| 170 | l4=-0.000103183 |
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| 171 | |
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| 172 | Lsub = l0 + l1 * dble(T) + l2 * dble(T)**2 + l3 * dble(T)**3 + l4 * dble(T)**4 ! J/kg |
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| 173 | |
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| 174 | ! Atmospheric density |
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| 175 | rhoatm = dble(P*Matm)/(rgp*dble(T)) ! g.m-3 |
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| 176 | rhoatm = rhoatm * 1.00e-3 ! kg.m-3 |
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| 177 | |
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| 178 | ! Compute thermal cond of mixture co2/N2 |
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| 179 | call KthMixNEW(kmix,T,pco2/dble(P),rhoatm) |
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| 180 | |
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| 181 | call Diffcoeff(P, T, Dv) |
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| 182 | |
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| 183 | Dv = Dv * 1.00e-4 ! cm2.s-1 to m2.s-1 |
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| 184 | |
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| 185 | ! ----- FS correction for Diff |
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| 186 | vthco2 = sqrt(8d0*kbz*dble(T)/(dble(pi) * mco2/nav)) ! units OK: m.s-1 |
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| 187 | knudsen = 3*Dv / (vthco2 * rc) |
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| 188 | lambda = (1.333+0.71/knudsen) / (1.+1./knudsen) ! pas adaptee, Dahneke 1983? en fait si (Monschick&Black) |
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| 189 | Dv = Dv / (1. + lambda * knudsen) |
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| 190 | |
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| 191 | ! ----- FS correction for Kth |
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| 192 | vthatm = sqrt(8d0*kbz*dble(T)/(pi * 1.00e-3*dble(Matm)/nav)) ! Matm/nav = mass of "air molecule" in G , *1e-3 --> kg |
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| 193 | Cpatm = Cpco2 * pco2/dble(P) + Cpn2 * (1d0 - pco2/dble(P)) !J.kg-1.K-1 |
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| 194 | lpmt = 3 * kmix / (rhoatm * vthatm * (Cpatm - 0.5*rgp/(dble(Matm)*1.00e-3))) ! mean free path related to heat transfer |
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| 195 | knudsen = lpmt / rc |
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| 196 | lambda = (1.333+0.71/knudsen) / (1.+1./knudsen) ! pas adaptee, Dahneke 1983? en fait si (Monschick&Black) |
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| 197 | kmix = kmix / (1. + lambda * knudsen) |
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| 198 | |
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| 199 | ! --------------------- ASSIGN coeff values for FUNCTION |
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| 200 | xinf = dble(S) * psat / dble(P) |
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| 201 | Ak = exp(2d0*sigco2*mco2/(rgp* dble(rho_ice_co2*T* rc) )) |
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| 202 | C0 = mco2*Dv*psat*Lsub/(rgp*dble(T)*kmix)*Ak*exp(-Lsub*mco2/(rgp*dble(T))) |
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| 203 | C1 = Lsub*mco2/(rgp*dble(T)**2) |
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| 204 | C2 = dble(T) + dble(P)*mco2*Dv*Lsub*xinf/(kmix*rgp*dble(T)) |
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| 205 | !======================================================================================================================! |
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| 206 | ! END =================================================================================================================! |
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| 207 | !======================================================================================================================! |
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| 208 | end subroutine coefffunc |
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| 209 | |
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| 210 | !______________________________________________________________________________________________________________________! |
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| 211 | !______________________________________________________________________________________________________________________! |
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| 212 | !______________________________________________________________________________________________________________________! |
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| 213 | |
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| 214 | |
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| 215 | subroutine Diffcoeff(P, T, Diff) |
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| 216 | !======================================================================================================================! |
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| 217 | ! Compute diffusion coefficient CO2/N2 cited in Ilona's lecture - from Reid et al. 1987 |
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| 218 | !======================================================================================================================! |
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[3008] | 219 | use microphys_h, only: mco2, mn2 |
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| 220 | |
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[2389] | 221 | implicit none |
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| 222 | |
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| 223 | !----------------------------------------------------------------------------------------------------------------------! |
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| 224 | ! VARIABLES DECLARATION |
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| 225 | !----------------------------------------------------------------------------------------------------------------------! |
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| 226 | ! Input arguments: |
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| 227 | !----------------- |
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| 228 | real, intent(in) :: & |
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| 229 | P, & |
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| 230 | T |
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| 231 | !----------------------------------------------------------------------------------------------------------------------! |
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| 232 | ! Output arguments: |
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| 233 | !------------------ |
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| 234 | double precision, intent(out) :: & |
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| 235 | Diff |
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| 236 | !----------------------------------------------------------------------------------------------------------------------! |
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| 237 | ! Local: |
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| 238 | !------- |
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| 239 | real :: & |
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| 240 | Pbar ! has to be in bar for the formula |
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| 241 | |
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| 242 | double precision :: & |
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| 243 | dva, & |
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| 244 | dvb, & |
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| 245 | Mab ! Mab has to be in g.mol-1 |
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| 246 | !======================================================================================================================! |
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| 247 | ! BEGIN ===============================================================================================================! |
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| 248 | !======================================================================================================================! |
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| 249 | Pbar = P * 1d-5 |
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| 250 | |
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| 251 | Mab = 2. / ( 1./mn2 + 1./mco2 ) * 1000. |
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| 252 | |
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| 253 | dva = 26.9 ! diffusion volume of CO2, Reid et al. 1987 (cited in Ilona's lecture) |
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| 254 | dvb = 18.5 ! diffusion volume of N2 |
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| 255 | |
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| 256 | !!! Diff in cm2.s-1 |
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| 257 | Diff = 0.00143 * dble(T)**(1.75) / (dble(Pbar) * sqrt(Mab) * (dble(dva)**(1./3.) + dble(dvb)**(1./3.))**2.) |
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| 258 | |
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| 259 | !======================================================================================================================! |
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| 260 | ! END =================================================================================================================! |
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| 261 | !======================================================================================================================! |
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| 262 | end subroutine Diffcoeff |
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| 263 | |
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| 264 | |
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| 265 | !______________________________________________________________________________________________________________________! |
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| 266 | !______________________________________________________________________________________________________________________! |
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| 267 | !______________________________________________________________________________________________________________________! |
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| 268 | |
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| 269 | |
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| 270 | subroutine KthMixNEW(Kthmix,T,x,rho) |
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| 271 | !======================================================================================================================! |
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| 272 | ! Compute thermal conductivity of CO2/N2 mixture (***WITHOUT*** USE OF VISCOSITY (Mason & Saxena 1958 - Wassiljeva 1904) |
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| 273 | !======================================================================================================================! |
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[3008] | 274 | use microphys_h, only: mco2, mn2 |
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| 275 | |
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[2389] | 276 | implicit none |
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| 277 | |
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| 278 | !----------------------------------------------------------------------------------------------------------------------! |
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| 279 | ! VARIABLES DECLARATION |
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| 280 | !----------------------------------------------------------------------------------------------------------------------! |
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| 281 | ! Input arguments: |
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| 282 | !----------------- |
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| 283 | real, intent(in) :: & |
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| 284 | T |
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| 285 | |
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| 286 | double precision, intent(in) :: & |
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| 287 | x, & |
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| 288 | rho ! kg.m-3 |
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| 289 | !----------------------------------------------------------------------------------------------------------------------! |
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| 290 | ! Output arguments: |
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| 291 | !------------------ |
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| 292 | double precision, intent(out) :: & |
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| 293 | Kthmix |
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| 294 | !----------------------------------------------------------------------------------------------------------------------! |
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| 295 | ! Local: |
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| 296 | !------- |
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| 297 | double precision :: & |
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| 298 | x1, & |
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| 299 | x2, & |
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| 300 | A12, & |
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| 301 | A11, & |
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| 302 | A22, & |
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| 303 | A21, & |
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| 304 | Tc1, & |
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| 305 | Tc2, & |
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| 306 | Pc1, & |
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| 307 | Pc2, & |
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| 308 | Gamma1, & |
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| 309 | Gamma2, & |
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| 310 | M1, & |
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| 311 | M2, & |
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| 312 | lambda_trans1, & |
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| 313 | lambda_trans2, & |
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| 314 | epsilon, & |
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| 315 | kco2, & |
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| 316 | kn2 |
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| 317 | !======================================================================================================================! |
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| 318 | ! BEGIN ===============================================================================================================! |
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| 319 | !======================================================================================================================! |
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| 320 | x1 = x |
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| 321 | x2 = 1d0 - x |
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| 322 | |
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| 323 | M1 = mco2 |
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| 324 | M2 = mn2 |
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| 325 | |
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| 326 | Tc1 = 304.1282 ! (Scalabrin et al. 2006) |
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| 327 | Tc2 = 126.192 ! (Lemmon & Jacobsen 2003) |
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| 328 | |
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| 329 | Pc1 = 73.773 ! (bars) |
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| 330 | Pc2 = 33.958 ! (bars) |
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| 331 | |
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| 332 | Gamma1 = 210.*(Tc1*M1**(3.)/Pc1**(4.))**(1./6.) |
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| 333 | Gamma2 = 210.*(Tc2*M2**(3.)/Pc2**(4.))**(1./6.) |
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| 334 | |
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| 335 | ! Translational conductivities |
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| 336 | lambda_trans1 = ( exp(0.0464 * T/Tc1) - exp(-0.2412 * T/Tc1) ) / Gamma1 |
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| 337 | lambda_trans2 = ( exp(0.0464 * T/Tc2) - exp(-0.2412 * T/Tc2) ) / Gamma2 |
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| 338 | |
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| 339 | ! Coefficient of Mason and Saxena |
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| 340 | epsilon = 1. |
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| 341 | |
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| 342 | A11 = 1. |
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| 343 | A22 = 1. |
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| 344 | A12 = epsilon * (1. + sqrt(lambda_trans1/lambda_trans2)* (M1/M2)**(1./4.))**(2.) / sqrt(8*(1.+ M1/M2)) |
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| 345 | A21 = epsilon * (1. + sqrt(lambda_trans2/lambda_trans1)*(M2/M1)**(1./4.))**(2.) / sqrt(8*(1.+ M2/M1)) |
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| 346 | |
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| 347 | ! INDIVIDUAL COND. |
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| 348 | call KthCO2Scalab(kco2,T,rho) |
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| 349 | call KthN2LemJac(kn2,T,rho) |
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| 350 | |
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| 351 | ! MIXTURE COND. |
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| 352 | Kthmix = kco2*x1 /(x1*A11 + x2*A12) + kn2*x2 /(x1*A21 + x2*A22) |
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| 353 | Kthmix = Kthmix*1e-3 ! from mW.m-1.K-1 to W.m-1.K-1 |
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| 354 | !======================================================================================================================! |
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| 355 | ! END =================================================================================================================! |
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| 356 | !======================================================================================================================! |
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| 357 | end subroutine KthMixNEW |
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| 358 | |
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| 359 | |
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| 360 | !______________________________________________________________________________________________________________________! |
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| 361 | !______________________________________________________________________________________________________________________! |
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| 362 | !______________________________________________________________________________________________________________________! |
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| 363 | |
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| 364 | |
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| 365 | subroutine KthN2LemJac(kthn2,T,rho) |
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| 366 | !======================================================================================================================! |
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| 367 | ! Compute thermal cond of N2 (Lemmon and Jacobsen, 2003) WITH viscosity |
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| 368 | !======================================================================================================================! |
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[3008] | 369 | use microphys_h, only: mn2 |
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| 370 | |
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[2389] | 371 | implicit none |
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| 372 | |
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| 373 | !----------------------------------------------------------------------------------------------------------------------! |
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| 374 | ! VARIABLES DECLARATION |
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| 375 | !----------------------------------------------------------------------------------------------------------------------! |
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| 376 | ! Input arguments: |
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| 377 | !----------------- |
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| 378 | real, intent(in) :: T |
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| 379 | |
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| 380 | double precision, intent(in) :: rho ! kg.m-3 |
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| 381 | !----------------------------------------------------------------------------------------------------------------------! |
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| 382 | ! Output argument: |
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| 383 | !----------------- |
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| 384 | double precision, intent(out) :: kthn2 |
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| 385 | !----------------------------------------------------------------------------------------------------------------------! |
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| 386 | ! Local: |
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| 387 | !------- |
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| 388 | double precision :: & |
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| 389 | g1, g2, g3, g4, g5, g6, g7, g8, g9, g10, & |
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| 390 | h1, h2, h3, h4, h5, h6, h7, h8, h9, h10, & |
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| 391 | n1, n2, n3, n4, n5, n6, n7, n8, n9, n10, & |
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| 392 | d4, d5, d6, d7, d8, d9, & |
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| 393 | l4, l5, l6, l7, l8, l9, & |
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| 394 | t2, t3, t4, t5, t6, t7, t8, t9, & |
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| 395 | gamma4, gamma5, gamma6, gamma7, gamma8, gamma9, & |
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| 396 | Tc, & |
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| 397 | rhoc, & |
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| 398 | tau, & |
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| 399 | delta, & |
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| 400 | visco, & |
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| 401 | k1, & |
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| 402 | k2 |
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| 403 | !======================================================================================================================! |
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| 404 | ! BEGIN ===============================================================================================================! |
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| 405 | !======================================================================================================================! |
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| 406 | N1 = 1.511d0 |
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| 407 | N2 = 2.117d0 |
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| 408 | N3 = -3.332d0 |
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| 409 | |
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| 410 | N4 = 8.862 |
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| 411 | N5 = 31.11 |
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| 412 | N6 = -73.13 |
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| 413 | N7 = 20.03 |
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| 414 | N8 = -0.7096 |
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| 415 | N9 = 0.2672 |
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| 416 | |
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| 417 | t2 = -1.0d0 |
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| 418 | t3 = -0.7d0 |
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| 419 | t4 = 0.0d0 |
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| 420 | t5 = 0.03 |
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| 421 | t6 = 0.2 |
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| 422 | t7 = 0.8 |
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| 423 | t8 = 0.6 |
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| 424 | t9 = 1.9 |
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| 425 | |
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| 426 | d4 = 1. |
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| 427 | d5 = 2. |
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| 428 | d6 = 3. |
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| 429 | d7 = 4. |
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| 430 | d8 = 8. |
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| 431 | d9 = 10. |
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| 432 | |
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| 433 | l4 = 0. |
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| 434 | gamma4 = 0. |
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| 435 | |
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| 436 | l5 = 0. |
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| 437 | gamma5 = 0. |
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| 438 | |
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| 439 | l6 = 1. |
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| 440 | gamma6 = 1. |
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| 441 | |
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| 442 | l7 = 2. |
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| 443 | gamma7 = 1. |
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| 444 | |
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| 445 | l8 = 2. |
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| 446 | gamma8 = 1. |
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| 447 | |
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| 448 | l9 = 2. |
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| 449 | gamma9 = 1. |
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| 450 | !----------------------------------------------------------------------------------------------------------------------! |
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| 451 | call viscoN2(T,visco) !! v given in microPa.s |
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| 452 | |
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| 453 | Tc = 126.192d0 |
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| 454 | rhoc = 11.1839 * 1000 * mn2 ! from mol.dm-3 to kg.m-3 |
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| 455 | |
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| 456 | tau = Tc / T |
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| 457 | delta = rho/rhoc |
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| 458 | |
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| 459 | k1 = N1 * visco + N2 * tau**t2 + N3 * tau**t3 !!! mW m-1 K-1 |
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| 460 | |
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| 461 | !--------- residual thermal conductivity |
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| 462 | k2 = N4 * tau**t4 * delta**d4 * exp(-gamma4*delta**l4) & |
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| 463 | + N5 * tau**t5 * delta**d5 * exp(-gamma5*delta**l5) & |
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| 464 | + N6 * tau**t6 * delta**d6 * exp(-gamma6*delta**l6) & |
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| 465 | + N7 * tau**t7 * delta**d7 * exp(-gamma7*delta**l7) & |
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| 466 | + N8 * tau**t8 * delta**d8 * exp(-gamma8*delta**l8) & |
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| 467 | + N9 * tau**t9 * delta**d9 * exp(-gamma9*delta**l9) |
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| 468 | |
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| 469 | kthn2 = k1 + k2 |
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| 470 | !======================================================================================================================! |
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| 471 | ! END =================================================================================================================! |
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| 472 | !======================================================================================================================! |
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| 473 | end subroutine KthN2LemJac |
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| 474 | |
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| 475 | |
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| 476 | !______________________________________________________________________________________________________________________! |
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| 477 | !______________________________________________________________________________________________________________________! |
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| 478 | !______________________________________________________________________________________________________________________! |
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| 479 | |
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| 480 | |
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| 481 | subroutine viscoN2(T,visco) |
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| 482 | !======================================================================================================================! |
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| 483 | ! Compute viscosity of N2 (Lemmon and Jacobsen, 2003) |
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| 484 | !======================================================================================================================! |
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[3008] | 485 | use microphys_h, only: mn2 |
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| 486 | |
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[2389] | 487 | implicit none |
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| 488 | |
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| 489 | !----------------------------------------------------------------------------------------------------------------------! |
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| 490 | ! VARIABLES DECLARATION |
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| 491 | !----------------------------------------------------------------------------------------------------------------------! |
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| 492 | ! Input argument: |
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| 493 | !---------------- |
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| 494 | real, intent(in) :: T |
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| 495 | !----------------------------------------------------------------------------------------------------------------------! |
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| 496 | ! Output argument: |
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| 497 | !----------------- |
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| 498 | double precision, intent(out) :: visco |
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| 499 | !----------------------------------------------------------------------------------------------------------------------! |
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| 500 | ! Local: |
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| 501 | !------- |
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| 502 | !-----1) Parameters: |
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| 503 | !------------------- |
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| 504 | double precision, parameter :: & |
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| 505 | factor = 98.94, & ! (K) |
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| 506 | sigma = 0.3656, & ! (nm) |
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| 507 | a0 = 0.431, & |
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| 508 | a1 = -0.4623, & |
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| 509 | a2 = 0.08406, & |
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| 510 | a3 = 0.005341, & |
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| 511 | a4 = -0.00331 |
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| 512 | !----------------------------------------------------------------------------------------------------------------------! |
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| 513 | !-----2) Variables: |
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| 514 | !------------------ |
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| 515 | double precision :: & |
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| 516 | Tstar, & |
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| 517 | M2, & |
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| 518 | RGCS |
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| 519 | !======================================================================================================================! |
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| 520 | ! BEGIN ===============================================================================================================! |
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| 521 | !======================================================================================================================! |
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| 522 | M2 = mn2 * 1.00e3 !!! to g.mol-1 |
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| 523 | |
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| 524 | Tstar = T*1./factor |
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| 525 | |
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| 526 | RGCS = exp( a0 + a1 * log(Tstar) + a2 * (log(Tstar))**2. + a3 * (log(Tstar))**3. + a4 * (log(Tstar))**4. ) |
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| 527 | |
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| 528 | visco = 0.0266958 * sqrt(M2*T) / ( sigma**2. * RGCS ) !!! microPa.s |
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| 529 | |
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| 530 | return |
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| 531 | !======================================================================================================================! |
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| 532 | ! END =================================================================================================================! |
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| 533 | !======================================================================================================================! |
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| 534 | end subroutine viscoN2 |
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| 535 | |
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| 536 | |
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| 537 | !______________________________________________________________________________________________________________________! |
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| 538 | !______________________________________________________________________________________________________________________! |
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| 539 | !______________________________________________________________________________________________________________________! |
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| 540 | |
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| 541 | |
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| 542 | subroutine KthCO2Scalab(kthco2,T,rho) |
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| 543 | !======================================================================================================================! |
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| 544 | ! Compute thermal cond of CO2 (Scalabrin et al. 2006) |
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| 545 | !======================================================================================================================! |
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| 546 | implicit none |
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| 547 | !----------------------------------------------------------------------------------------------------------------------! |
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| 548 | ! VARIABLES DECLARATION |
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| 549 | !----------------------------------------------------------------------------------------------------------------------! |
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| 550 | ! Input arguments: |
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| 551 | !----------------- |
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| 552 | real, intent(in) :: T |
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| 553 | |
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| 554 | double precision, intent(in) :: rho |
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| 555 | !----------------------------------------------------------------------------------------------------------------------! |
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| 556 | ! Output argument: |
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| 557 | !----------------- |
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| 558 | double precision, intent(out) :: kthco2 |
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| 559 | !----------------------------------------------------------------------------------------------------------------------! |
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| 560 | ! Local: |
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| 561 | !------- |
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| 562 | !------- |
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| 563 | !-----1) Parameters: |
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| 564 | !------------------- |
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| 565 | double precision, parameter :: & |
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| 566 | Tc = 304.1282, & !(K) |
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| 567 | Pc = 7.3773e6, & !(MPa) |
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| 568 | rhoc = 467.6, & !(kg.m-3) |
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| 569 | Lambdac = 4.81384,& !(mW.m-1K-1) |
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| 570 | g1 = 0., & |
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| 571 | g2 = 0., & |
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| 572 | g3 = 1.5, & |
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| 573 | g4 = 0.0, & |
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| 574 | g5 = 1.0, & |
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| 575 | g6 = 1.5, & |
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| 576 | g7 = 1.5, & |
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| 577 | g8 = 1.5, & |
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| 578 | g9 = 3.5, & |
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| 579 | g10 = 5.5, & |
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| 580 | h1 = 1., & |
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| 581 | h2 = 5., & |
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| 582 | h3 = 1., & |
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| 583 | h4 = 1., & |
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| 584 | h5 = 2., & |
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| 585 | h6 = 0., & |
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| 586 | h7 = 5.0, & |
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| 587 | h8 = 9.0, & |
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| 588 | h9 = 0., & |
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| 589 | h10 = 0., & |
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| 590 | n1 = 7.69857587, & |
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| 591 | n2 = 0.159885811, & |
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| 592 | n3 = 1.56918621, & |
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| 593 | n4 = -6.73400790, & |
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| 594 | n5 = 16.3890156, & |
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| 595 | n6 = 3.69415242, & |
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| 596 | n7 = 22.3205514, & |
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| 597 | n8 = 66.1420950, & |
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| 598 | n9 = -0.171779133,& |
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| 599 | n10 = 0.00433043347 |
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| 600 | !----------------------------------------------------------------------------------------------------------------------! |
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| 601 | !-----2) Variables: |
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| 602 | !------------------ |
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| 603 | double precision :: & |
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| 604 | Tr, & |
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| 605 | rhor,& |
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| 606 | k1, & |
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| 607 | k2 |
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| 608 | !======================================================================================================================! |
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| 609 | ! BEGIN ===============================================================================================================! |
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| 610 | !======================================================================================================================! |
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| 611 | Tr = T/Tc |
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| 612 | rhor = rho/rhoc |
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| 613 | |
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| 614 | k1 = n1*Tr**(g1)*rhor**(h1) + n2*Tr**(g2)*rhor**(h2) + n3*Tr**(g3)*rhor**(h3) |
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| 615 | |
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| 616 | k2 = n4*Tr**(g4)*rhor**(h4) + n5*Tr**(g5)*rhor**(h5) & |
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| 617 | + n6*Tr**(g6)*rhor**(h6) + n7*Tr**(g7)*rhor**(h7) & |
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| 618 | + n8*Tr**(g8)*rhor**(h8) + n9*Tr**(g9)*rhor**(h9) & |
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| 619 | + n10*Tr**(g10)*rhor**(h10) |
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| 620 | |
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| 621 | k2 = k2 * exp(-5.*rhor**(2.)) |
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| 622 | |
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| 623 | kthco2 = (k1 + k2) * Lambdac ! mW |
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| 624 | !======================================================================================================================! |
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| 625 | ! END =================================================================================================================! |
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| 626 | !======================================================================================================================! |
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| 627 | end subroutine KthCO2Scalab |
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[3008] | 628 | |
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| 629 | END MODULE massflowrateco2_mod |
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