| 1 | SUBROUTINE concentrations2(pplay,t_seri,pdt,tr_seri, nqmx) |
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| 2 | |
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| 3 | use dimphy |
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| 4 | use conc, only: mmean, rho, Akknew, rnew, cpnew |
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| 5 | use cpdet_phy_mod, only: cpdet |
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| 6 | USE chemparam_mod |
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| 7 | |
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| 8 | implicit none |
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| 9 | |
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| 10 | !======================================================================= |
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| 11 | ! CALCULATION OF MEAN MOLECULAR MASS, Cp, Akk and R |
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| 12 | ! |
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| 13 | ! mmean(klon,klev) amu |
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| 14 | ! cpnew(klon,klev) J/kg/K |
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| 15 | ! rnew(klon,klev) J/kg/K |
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| 16 | ! akknew(klon,klev) coefficient of thermal conduction |
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| 17 | ! |
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| 18 | ! version: April 2012 - Franck Lefevre |
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| 19 | !======================================================================= |
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| 20 | |
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| 21 | ! declarations |
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| 22 | |
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| 23 | #include "YOMCST.h" |
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| 24 | #include "clesphys.h" |
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| 25 | c#include "comdiurn.h" |
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| 26 | c#include "chimiedata.h" |
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| 27 | c#include "tracer.h" |
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| 28 | c#include "mmol.h" |
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| 29 | |
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| 30 | ! input/output |
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| 31 | |
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| 32 | real pplay(klon,klev) |
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| 33 | c real pt(klon,klev) |
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| 34 | integer,intent(in) :: nqmx ! number of tracers |
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| 35 | real t_seri(klon, klev) |
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| 36 | real pdt(klon,klev) |
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| 37 | real n2vmr_gcm(klon,klev),nvmr_gcm(klon,klev) |
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| 38 | real tr_seri(klon,klev,nqmx) |
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| 39 | c real pdq(klon,klev,nqmx) |
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| 40 | real ptimestep |
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| 41 | |
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| 42 | ! local variables |
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| 43 | |
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| 44 | integer :: i, l, ig, iq |
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| 45 | integer, save :: nbq |
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| 46 | integer,allocatable,save :: niq(:) |
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| 47 | real :: ni(nqmx), ntot |
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| 48 | real :: zt(klon, klev) |
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| 49 | real :: zq(klon, klev, nqmx) |
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| 50 | real,allocatable,save :: aki(:) |
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| 51 | real,allocatable,save :: cpi(:) |
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| 52 | real, save :: akin,akin2 |
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| 53 | |
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| 54 | logical, save :: firstcall = .true. |
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| 55 | |
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| 56 | if (firstcall) then |
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| 57 | |
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| 58 | ! initialize thermal conductivity and specific heat coefficients |
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| 59 | ! values are taken from the literature [J/kg K] |
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| 60 | |
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| 61 | ! allocate local saved arrays: |
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| 62 | allocate(aki(nqmx)) |
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| 63 | allocate(cpi(nqmx)) |
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| 64 | allocate(niq(nqmx)) |
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| 65 | |
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| 66 | ! find index of chemical tracers to use |
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| 67 | ! initialize thermal conductivity and specific heat coefficients |
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| 68 | ! !? values are estimated |
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| 69 | |
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| 70 | nbq = 0 ! to count number of tracers used in this subroutine |
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| 71 | |
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| 72 | if (i_co2 /= 0) then |
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| 73 | nbq = nbq + 1 |
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| 74 | niq(nbq) = i_co2 |
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| 75 | aki(nbq) = 3.072e-4 |
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| 76 | cpi(nbq) = 0.834e3 |
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| 77 | end if |
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| 78 | if (i_co /= 0) then |
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| 79 | nbq = nbq + 1 |
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| 80 | niq(nbq) = i_co |
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| 81 | aki(nbq) = 4.87e-4 |
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| 82 | cpi(nbq) = 1.034e3 |
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| 83 | end if |
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| 84 | if (i_o /= 0) then |
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| 85 | nbq = nbq + 1 |
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| 86 | niq(nbq) = i_o |
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| 87 | aki(nbq) = 7.59e-4 |
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| 88 | cpi(nbq) = 1.3e3 |
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| 89 | end if |
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| 90 | if (i_o1d /= 0) then |
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| 91 | nbq = nbq + 1 |
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| 92 | niq(nbq) = i_o1d |
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| 93 | aki(nbq) = 7.59e-4 !? |
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| 94 | cpi(nbq) = 1.3e3 !? |
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| 95 | end if |
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| 96 | if (i_o2 /= 0) then |
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| 97 | nbq = nbq + 1 |
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| 98 | niq(nbq) = i_o2 |
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| 99 | aki(nbq) = 5.68e-4 |
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| 100 | cpi(nbq) = 0.9194e3 |
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| 101 | end if |
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| 102 | if (i_o3 /= 0) then |
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| 103 | nbq = nbq + 1 |
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| 104 | niq(nbq) = i_o3 |
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| 105 | aki(nbq) = 3.00e-4 !? |
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| 106 | cpi(nbq) = 0.800e3 !? |
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| 107 | end if |
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| 108 | if (i_h /= 0) then |
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| 109 | nbq = nbq + 1 |
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| 110 | niq(nbq) = i_h |
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| 111 | aki(nbq) = 0.0 |
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| 112 | cpi(nbq) = 20.780e3 |
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| 113 | end if |
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| 114 | if (i_h2 /= 0) then |
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| 115 | nbq = nbq + 1 |
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| 116 | niq(nbq) = i_h2 |
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| 117 | aki(nbq) = 36.314e-4 |
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| 118 | cpi(nbq) = 14.266e3 |
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| 119 | end if |
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| 120 | if (i_oh /= 0) then |
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| 121 | nbq = nbq + 1 |
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| 122 | niq(nbq) = i_oh |
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| 123 | aki(nbq) = 7.00e-4 !? |
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| 124 | cpi(nbq) = 1.045e3 |
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| 125 | end if |
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| 126 | if (i_ho2 /= 0) then |
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| 127 | nbq = nbq + 1 |
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| 128 | niq(nbq) = i_ho2 |
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| 129 | aki(nbq) = 0.0 |
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| 130 | cpi(nbq) = 1.065e3 !? |
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| 131 | end if |
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| 132 | if (i_n2 /= 0) then |
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| 133 | nbq = nbq + 1 |
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| 134 | niq(nbq) = i_n2 |
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| 135 | aki(nbq) = 5.6e-4 |
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| 136 | cpi(nbq) = 1.034e3 |
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| 137 | end if |
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| 138 | c if (i_ar /= 0) then |
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| 139 | c nbq = nbq + 1 |
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| 140 | c niq(nbq) = i_ar |
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| 141 | c aki(nbq) = 0.0 !? |
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| 142 | c cpi(nbq) = 1.000e3 !? |
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| 143 | c end if |
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| 144 | if (i_h2o /= 0) then |
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| 145 | nbq = nbq + 1 |
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| 146 | niq(nbq) = i_h2o |
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| 147 | aki(nbq) = 0.0 |
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| 148 | cpi(nbq) = 1.870e3 |
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| 149 | end if |
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| 150 | c if (i_n /= 0) then |
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| 151 | c nbq = nbq + 1 |
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| 152 | c niq(nbq) = i_n |
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| 153 | c aki(nbq) = 0.0 |
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| 154 | c cpi(nbq) = 0.0 |
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| 155 | c endif |
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| 156 | c if(i_no /= 0) then |
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| 157 | c nbq = nbq + 1 |
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| 158 | c niq(nbq) = i_no |
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| 159 | c aki(nbq) = 0.0 |
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| 160 | c cpi(nbq) = 0.0 |
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| 161 | c endif |
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| 162 | c if(i_no2 /= 0) then |
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| 163 | c nbq = nbq + 1 |
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| 164 | c niq(nbq) = i_no2 |
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| 165 | c aki(nbq) = 0.0 |
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| 166 | c cpi(nbq) = 0.0 |
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| 167 | c endif |
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| 168 | c if(i_n2d /= 0) then |
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| 169 | c nbq = nbq + 1 |
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| 170 | c niq(nbq) = i_n2d |
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| 171 | c aki(nbq) = 0.0 |
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| 172 | c cpi(nbq) = 0.0 |
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| 173 | c endif |
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| 174 | |
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| 175 | ! tell the world about it: |
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| 176 | write(*,*) "concentrations: firstcall, nbq=",nbq |
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| 177 | ! write(*,*) " niq(1:nbq)=",niq(1:nbq) |
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| 178 | ! write(*,*) " aki(1:nbq)=",aki(1:nbq) |
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| 179 | ! write(*,*) " cpi(1:nbq)=",cpi(1:nbq) |
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| 180 | |
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| 181 | |
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| 182 | firstcall = .false. |
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| 183 | end if ! if (firstcall) |
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| 184 | |
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| 185 | ! update temperature |
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| 186 | |
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| 187 | do l = 1,klev |
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| 188 | do ig = 1,klon |
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| 189 | zt(ig,l) = t_seri(ig,l) |
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| 190 | end do |
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| 191 | end do |
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| 192 | |
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| 193 | |
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| 194 | ! update mass mixing ratio tracers |
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| 195 | |
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| 196 | do l = 1,klev |
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| 197 | do ig = 1,klon |
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| 198 | do i = 1,nqmx |
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| 199 | ! iq = niq(i) |
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| 200 | zq(ig,l,i) = max(1.e-30, tr_seri(ig,l,i)) |
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| 201 | end do |
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| 202 | end do |
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| 203 | end do |
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| 204 | |
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| 205 | ! mmean : mean molecular mass |
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| 206 | ! rho : mass density [kg/m3] |
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| 207 | ! rnew : specific gas constant |
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| 208 | |
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| 209 | mmean(:,:) = 0. |
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| 210 | rho(:,:) = 0. |
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| 211 | |
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| 212 | do l = 1,klev |
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| 213 | do ig = 1,klon |
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| 214 | do i = 1,nqmx |
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| 215 | c iq = niq(i) |
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| 216 | mmean(ig,l) = mmean(ig,l) + zq(ig,l,i)/M_tr(i) |
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| 217 | end do |
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| 218 | mmean(ig,l) = 1./mmean(ig,l) |
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| 219 | rnew(ig,l) = 8.314/mmean(ig,l)*1.e3 ! J/kg K |
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| 220 | c write(*,*),'Mmean in concentration2: ',ig, l, mmean(ig,l) |
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| 221 | end do |
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| 222 | end do |
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| 223 | |
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| 224 | ! cpnew : specific heat |
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| 225 | ! akknew : thermal conductivity cofficient |
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| 226 | |
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| 227 | cpnew(:,:) = 0. |
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| 228 | akknew(:,:) = 0. |
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| 229 | |
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| 230 | do l = 1,klev |
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| 231 | do ig = 1,klon |
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| 232 | |
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| 233 | ntot = pplay(ig,l)/(RKBOL*zt(ig,l))*1.e-6 ! in #/cm3 |
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| 234 | rho(ig,l) = (ntot * mmean(ig,l))/RNAVO*1.e3 ! in kg/m3 |
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| 235 | |
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| 236 | c write(*,*),'Air density: ',ig, l, rho(0,l) |
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| 237 | |
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| 238 | !! WARNING -> Cp here below doesn't depend on T (cpdet) |
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| 239 | |
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| 240 | do i = 1,nbq |
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| 241 | c iq = niq(i) |
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| 242 | ni(i) = ntot*zq(ig,l,i)*mmean(ig,l)/M_tr(i) |
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| 243 | cpnew(ig,l) = cpnew(ig,l) + ni(i)*cpi(i) |
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| 244 | akknew(ig,l) = akknew(ig,l) + ni(i)*aki(i) |
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| 245 | end do |
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| 246 | |
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| 247 | |
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| 248 | cpnew(ig,l) = cpnew(ig,l)/ntot |
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| 249 | akknew(ig,l)= akknew(ig,l)/ntot |
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| 250 | |
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| 251 | |
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| 252 | end do |
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| 253 | end do |
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| 254 | |
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| 255 | return |
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| 256 | end |
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