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|
*
* pco2.F
*
* Andreas Schmittner (andreas@passagen.uni-kiel.de)
* Mai 26th 2004
*
* Returns pCO2 of water
*
*
*
SUBROUTINE pco2_init(id)
INCLUDE 'ferret_cmn/EF_Util.cmn'
INTEGER id, arg
* **********************************************************************
* USER CONFIGURABLE PORTION |
* |
* V
CALL ef_set_desc(id,
. 'returns pCO2 (ppmv=uatm) using OCMIP routines' )
CALL ef_set_num_args(id, 4)
CALL ef_set_has_vari_args(id, NO)
CALL ef_set_axis_inheritance(id, IMPLIED_BY_ARGS,
. IMPLIED_BY_ARGS, IMPLIED_BY_ARGS, IMPLIED_BY_ARGS)
CALL ef_set_piecemeal_ok(id, NO, NO, NO, NO)
arg = 1
CALL ef_set_arg_name(id, arg, 'TEMP')
CALL ef_set_arg_unit(id, arg, 'deg C')
CALL ef_set_arg_desc(id, arg, 'temperature')
CALL ef_set_axis_influence(id, arg, YES, YES, YES, YES)
arg = 2
CALL ef_set_arg_name(id, arg, 'SALT')
CALL ef_set_arg_unit(id, arg, 'su')
CALL ef_set_arg_desc(id, arg, 'salinity')
CALL ef_set_axis_influence(id, arg, YES, YES, YES, YES)
arg = 3
CALL ef_set_arg_name(id, arg, 'DIC')
CALL ef_set_arg_unit(id, arg, 'mmol/m^3')
CALL ef_set_arg_desc(id, arg, 'dissolved inorganic carbon')
CALL ef_set_axis_influence(id, arg, YES, YES, YES, YES)
arg = 4
CALL ef_set_arg_name(id, arg, 'ALK')
CALL ef_set_arg_unit(id, arg, 'mmol/m^3')
CALL ef_set_arg_desc(id, arg, 'total alkalinity')
CALL ef_set_axis_influence(id, arg, YES, YES, YES, YES)
* ^
* |
* USER CONFIGURABLE PORTION |
* **********************************************************************
RETURN
END
*
* In this subroutine we compute the result
*
SUBROUTINE pco2_compute(id, arg_1, arg_2, arg_3, arg_4, result)
INCLUDE 'ferret_cmn/EF_Util.cmn'
INCLUDE 'ferret_cmn/EF_mem_subsc.cmn'
INTEGER id
REAL bad_flag(EF_MAX_ARGS), bad_flag_result
REAL arg_1(mem1lox:mem1hix, mem1loy:mem1hiy,
. mem1loz:mem1hiz, mem1lot:mem1hit)
REAL arg_2(mem2lox:mem2hix, mem2loy:mem2hiy,
. mem2loz:mem2hiz, mem2lot:mem2hit)
REAL arg_3(mem3lox:mem3hix, mem3loy:mem3hiy,
. mem3loz:mem3hiz, mem3lot:mem3hit)
REAL arg_4(mem4lox:mem4hix, mem4loy:mem4hiy,
. mem4loz:mem4hiz, mem4lot:mem4hit)
REAL result(memreslox:memreshix, memresloy:memreshiy,
. memresloz:memreshiz, memreslot:memreshit)
* After initialization, the 'res_' arrays contain indexing information
* for the result axes. The 'arg_' arrays will contain the indexing
* information for each variable's axes.
INTEGER res_lo_ss(4), res_hi_ss(4), res_incr(4)
INTEGER arg_lo_ss(4,EF_MAX_ARGS), arg_hi_ss(4,EF_MAX_ARGS),
. arg_incr(4,EF_MAX_ARGS)
* **********************************************************************
* USER CONFIGURABLE PORTION |
* |
* V
INTEGER i,j,k,l
INTEGER i1, j1, k1, l1
INTEGER i2, j2, k2, l2
INTEGER i3, j3, k3, l3
INTEGER i4, j4, k4, l4
real pt_in,sit_in,atmpres,phlo,phhi,co2ccn, ph, co2star,
. co2starair, dco2star, pco2surf, dpco2, pco2atm
CALL ef_get_res_subscripts(id, res_lo_ss, res_hi_ss, res_incr)
CALL ef_get_arg_subscripts(id, arg_lo_ss, arg_hi_ss, arg_incr)
CALL ef_get_bad_flags(id, bad_flag, bad_flag_result)
co2ccn=280.
pt_in=0.5125e-3 !mol/m^3
atmpres=1.0 !atm
sit_in=7.6875e-03 !mol/m^3
phlo=6.
phhi=9.
i1 = arg_lo_ss(X_AXIS,ARG1)
i2 = arg_lo_ss(X_AXIS,ARG2)
i3 = arg_lo_ss(X_AXIS,ARG3)
i4 = arg_lo_ss(X_AXIS,ARG4)
DO 400 i=res_lo_ss(X_AXIS), res_hi_ss(X_AXIS)
j1 = arg_lo_ss(Y_AXIS,ARG1)
j2 = arg_lo_ss(Y_AXIS,ARG2)
j3 = arg_lo_ss(Y_AXIS,ARG3)
j4 = arg_lo_ss(Y_AXIS,ARG4)
DO 300 j=res_lo_ss(Y_AXIS), res_hi_ss(Y_AXIS)
k1 = arg_lo_ss(Z_AXIS,ARG1)
k2 = arg_lo_ss(Z_AXIS,ARG2)
k3 = arg_lo_ss(Z_AXIS,ARG3)
k4 = arg_lo_ss(Z_AXIS,ARG4)
DO 200 k=res_lo_ss(Z_AXIS), res_hi_ss(Z_AXIS)
l1 = arg_lo_ss(T_AXIS,ARG1)
l2 = arg_lo_ss(T_AXIS,ARG2)
l3 = arg_lo_ss(T_AXIS,ARG3)
l4 = arg_lo_ss(T_AXIS,ARG4)
DO 100 l=res_lo_ss(T_AXIS), res_hi_ss(T_AXIS)
IF ( arg_1(i1,j1,k1,l1) .EQ. bad_flag(1) .OR.
. arg_2(i2,j2,k2,l2) .EQ. bad_flag(2) .OR.
. arg_3(i3,j3,k3,l3) .EQ. bad_flag(3) .OR.
. arg_4(i4,j4,k4,l4) .EQ. bad_flag(4) ) THEN
result(i,j,k,l) = bad_flag_result
ELSE
call co2calc(arg_1(i1,j1,k1,l1)
& ,arg_2(i2,j2,k2,l2),arg_3(i3,j3,k3,l3)
& ,arg_4(i4,j4,k4,l4),pt_in,sit_in
& ,phlo,phhi,ph,co2ccn,atmpres,co2star
& ,co2starair,dco2star,pCO2surf,dpco2
& ,pCO2atm)
result(i,j,k,l) = pCO2surf
END IF
l1 = l1 + arg_incr(T_AXIS,ARG1)
l2 = l2 + arg_incr(T_AXIS,ARG2)
l3 = l3 + arg_incr(T_AXIS,ARG3)
l4 = l4 + arg_incr(T_AXIS,ARG4)
100 CONTINUE
k1 = k1 + arg_incr(Z_AXIS,ARG1)
k2 = k2 + arg_incr(Z_AXIS,ARG2)
k3 = k3 + arg_incr(Z_AXIS,ARG3)
k4 = k4 + arg_incr(Z_AXIS,ARG4)
200 CONTINUE
j1 = j1 + arg_incr(Y_AXIS,ARG1)
j2 = j2 + arg_incr(Y_AXIS,ARG2)
j3 = j3 + arg_incr(Y_AXIS,ARG3)
j4 = j4 + arg_incr(Y_AXIS,ARG4)
300 CONTINUE
i1 = i1 + arg_incr(X_AXIS,ARG1)
i2 = i2 + arg_incr(X_AXIS,ARG2)
i3 = i3 + arg_incr(X_AXIS,ARG3)
i4 = i4 + arg_incr(X_AXIS,ARG4)
400 CONTINUE
* ^
* |
* USER CONFIGURABLE PORTION |
* **********************************************************************
RETURN
END
c_ ---------------------------------------------------------------------
c_ RCS lines preceded by "c_ "
c_ ---------------------------------------------------------------------
c_
c_ Revision 1.1 2004/06/01 17:38:06 ansley
c_ add pco2 function from Andreas Schmittner
c_
c_ Revision 1.8 1999/07/16 11:40:33 orr
c_ Modifications by Keith Lindsay to fix inconsistency with common block
c_ "species" (not the same in "ta_iter_1.f").
c_ Also comment lines changed/added by J. Orr.
c_
c_ Revision 1.7 1999/04/26 13:04:54 orr
c_ Modified USAGE comment, to include new arguments
c_
c_ Revision 1.6 1999/04/14 12:55:52 orr
c_ Changed units for input arguments for tracers:
c_ formerly in mol/metric ton (T); now in mol/m^3.
c_ Used 1024.5 kg/m^3 as a constant conversion factor.
c_ Modelers can now pass tracers on a per volume basis, as carried in models.
c_
c_ Revision 1.5 1999/04/06 16:57:37 orr
c_ Changed calc of dpCO2 to account for diff atm pressure
c_
c_ Revision 1.4 1999/04/06 13:17:58 orr
c_ Added 2 output arguments: pCO2surf and dpCO2
c_ (see section 4 of Biotic HOWTO)
c_
c_ Revision 1.3 1999/04/05 15:59:11 orr
c_ Cleaned up comments regarding units
c_
c_ Revision 1.2 1999/04/04 02:35:00 orr
c_ Changed units for input and output tracers:
c_ previously in umol/kg; now in mol/T
c_ Can also pass input and output in mol/m^3 with little error.
c_
c_ Revision 1.1 1999/04/03 21:59:56 orr
c_ Initial revision
c_
c_ ---------------------------------------------------------------------
c_
subroutine co2calc(t,s,dic_in,ta_in,pt_in,sit_in
& ,phlo,phhi,ph,xtco2in,atmpres,co2star
& ,co2starair,dco2star,pCO2surf,dpCO2
& ,pCO2atm)
C
C-------------------------------------------------------------------------
C SUBROUTINE CO2CALC
C
C PURPOSE
C Calculate delta co2* from total alkalinity and total CO2 at
C temperature (t), salinity (s) and "atmpres" atmosphere total pressure.
C
C USAGE
C call co2calc(t,s,dic_in,ta_in,pt_in,sit_in
C & ,phlo,phhi,ph,xco2_in,atmpres
C & ,co2star,dco2star,pCO2surf,dpco2)
C
C INPUT
C dic_in = total inorganic carbon (mol/m^3)
C where 1 T = 1 metric ton = 1000 kg
C ta_in = total alkalinity (eq/m^3)
C pt_in = inorganic phosphate (mol/m^3)
C sit_in = inorganic silicate (mol/m^3)
C t = temperature (degrees C)
C s = salinity (PSU)
C phlo = lower limit of pH range
C phhi = upper limit of pH range
C xco2_in=atmospheric mole fraction CO2 in dry air (ppmv)
C atmpres= atmospheric pressure in atmospheres (1 atm==1013.25mbar)
C
C Note: arguments dic_in, ta_in, pt_in, sit_in, and xco2_in are
C used to initialize variables dic, ta, pt, sit, and xco2.
C * Variables dic, ta, pt, and sit are in the common block
C "species".
C * Variable xco2 is a local variable.
C * Variables with "_in" suffix have different units
C than those without.
C OUTPUT
C co2star = CO2*water (mol/m^3)
C dco2star = delta CO2 (mol/m^3)
c pco2surf = oceanic pCO2 (ppmv)
c dpco2 = Delta pCO2, i.e, pCO2ocn - pCO2atm (ppmv)
C
C IMPORTANT: Some words about units - (JCO, 4/4/1999)
c - Models carry tracers in mol/m^3 (on a per volume basis)
c - Conversely, this routine, which was written by observationalists
c (C. Sabine and R. Key), passes input arguments in umol/kg
c (i.e., on a per mass basis)
c - I have changed things slightly so that input arguments are in mol/m^3,
c - Thus, all input concentrations (dic_in, ta_in, pt_in, and st_in)
c should be given in mol/m^3; output arguments "co2star" and "dco2star"
c are likewise in mol/m^3.
C FILES and PROGRAMS NEEDED
C drtsafe
C ta_iter_1
C
C--------------------------------------------------------------------------
C
include "species.h"
real invtk,is,is2,xtco2in
c real k0,k1,k2,kkw,kb,ks,kf,k1p,k2p,k3p,ksi
real drtsafe
real t, s, dic_in, ta_in, pt_in, sit_in, phlo, phhi, ph,
. atmpres, co2star, co2starair, dco2star, pco2surf, dpco2,
. pco2atm, permil, permeg, xtco2, tk, tk100, tk1002, dlogtk,
. sqrtis, s2, sqrts, s15, scl, ff, x1, x2, xacc, htotal,
. htotal2
external ta_iter_1
C
c ---------------------------------------------------------------------
C Change units from the input of mol/m^3 -> mol/kg:
c (1 mol/m^3) x (1 m^3/1024.5 kg)
c where the ocean's mean surface density is 1024.5 kg/m^3
c Note: mol/kg are actually what the body of this routine uses
c for calculations.
c ---------------------------------------------------------------------
permil = 1.0 / 1024.5
c To convert input in mol/m^3 -> mol/kg
pt=pt_in*permil
sit=sit_in*permil
ta=ta_in*permil
dic=dic_in*permil
c ---------------------------------------------------------------------
C Change units from uatm to atm. That is, atm is what the body of
c this routine uses for calculations.
c ---------------------------------------------------------------------
permeg=1.e-6
c To convert input in uatm -> atm
xtco2=xtco2in*permeg
c ---------------------------------------------------------------------
C
C*************************************************************************
C Calculate all constants needed to convert between various measured
C carbon species. References for each equation are noted in the code.
C Once calculated, the constants are
C stored and passed in the common block "const". The original version of this
C code was based on the code by Dickson in Version 2 of "Handbook of Methods
C for the Analysis of the Various Parameters of the Carbon Dioxide System
C in Seawater", DOE, 1994 (SOP No. 3, p25-26).
C
C Derive simple terms used more than once
C
tk = 273.15 + t
tk100 = tk/100.0
tk1002=tk100*tk100
invtk=1.0/tk
dlogtk=log(tk)
is=19.924*s/(1000.-1.005*s)
is2=is*is
sqrtis=sqrt(is)
s2=s*s
sqrts=sqrt(s)
s15=s**1.5
scl=s/1.80655
C
C f = k0(1-pH2O)*correction term for non-ideality
C
C Weiss & Price (1980, Mar. Chem., 8, 347-359; Eq 13 with table 6 values)
C
ff = exp(-162.8301 + 218.2968/tk100 +
& 90.9241*log(tk100) - 1.47696*tk1002 +
& s * (.025695 - .025225*tk100 +
& 0.0049867*tk1002))
C
C K0 from Weiss 1974
C
k0 = exp(93.4517/tk100 - 60.2409 + 23.3585 * log(tk100) +
& s * (.023517 - 0.023656 * tk100 + 0.0047036 * tk1002))
C
C kk1 = [H][HCO3]/[H2CO3]
C k2 = [H][CO3]/[HCO3]
C
C Millero p.664 (1995) using Mehrbach et al. data on seawater scale
C
kk1=10**(-1*(3670.7*invtk - 62.008 + 9.7944*dlogtk -
& 0.0118 * s + 0.000116*s2))
C
k2=10**(-1*(1394.7*invtk + 4.777 -
& 0.0184*s + 0.000118*s2))
C
C kb = [H][BO2]/[HBO2]
C
C Millero p.669 (1995) using data from Dickson (1990)
C
kb=exp((-8966.90 - 2890.53*sqrts - 77.942*s +
& 1.728*s15 - 0.0996*s2)*invtk +
& (148.0248 + 137.1942*sqrts + 1.62142*s) +
& (-24.4344 - 25.085*sqrts - 0.2474*s) *
& dlogtk + 0.053105*sqrts*tk)
C
C k1p = [H][H2PO4]/[H3PO4]
C
C DOE(1994) eq 7.2.20 with footnote using data from Millero (1974)
C
k1p = exp(-4576.752*invtk + 115.525 - 18.453 * dlogtk +
& (-106.736*invtk + 0.69171) * sqrts +
& (-0.65643*invtk - 0.01844) * s)
C
C k2p = [H][HPO4]/[H2PO4]
C
C DOE(1994) eq 7.2.23 with footnote using data from Millero (1974))
C
k2p = exp(-8814.715*invtk + 172.0883 - 27.927 * dlogtk +
& (-160.340*invtk + 1.3566) * sqrts +
& (0.37335*invtk - 0.05778) * s)
C
C------------------------------------------------------------------------
C k3p = [H][PO4]/[HPO4]
C
C DOE(1994) eq 7.2.26 with footnote using data from Millero (1974)
C
k3p = exp(-3070.75*invtk - 18.141 +
& (17.27039*invtk + 2.81197) *
& sqrts + (-44.99486*invtk - 0.09984) * s)
C
C------------------------------------------------------------------------
C ksi = [H][SiO(OH)3]/[Si(OH)4]
C
C Millero p.671 (1995) using data from Yao and Millero (1995)
C
ksi = exp(-8904.2*invtk + 117.385 - 19.334 * dlogtk +
& (-458.79*invtk + 3.5913) * sqrtis +
& (188.74*invtk - 1.5998) * is +
& (-12.1652*invtk + 0.07871) * is2 +
& log(1.0-0.001005*s))
C
C------------------------------------------------------------------------
C kkw = [H][OH]
C
C Millero p.670 (1995) using composite data
C
kkw = exp(-13847.26*invtk + 148.9652 - 23.6521 * dlogtk +
& (118.67*invtk - 5.977 + 1.0495 * dlogtk) *
& sqrts - 0.01615 * s)
C
C------------------------------------------------------------------------
C ks = [H][SO4]/[HSO4]
C
C Dickson (1990, J. chem. Thermodynamics 22, 113)
C
ks=exp(-4276.1*invtk + 141.328 - 23.093*dlogtk +
& (-13856*invtk + 324.57 - 47.986*dlogtk) * sqrtis +
& (35474*invtk - 771.54 + 114.723*dlogtk) * is -
& 2698*invtk*is**1.5 + 1776*invtk*is2 +
& log(1.0 - 0.001005*s))
C
C------------------------------------------------------------------------
C kf = [H][F]/[HF]
C
C Dickson and Riley (1979) -- change pH scale to total
C
kf=exp(1590.2*invtk - 12.641 + 1.525*sqrtis +
& log(1.0 - 0.001005*s) +
& log(1.0 + (0.1400/96.062)*(scl)/ks))
C
C------------------------------------------------------------------------
C Calculate concentrations for borate, sulfate, and fluoride
C
C Uppstrom (1974)
bt = 0.000232 * scl/10.811
C Morris & Riley (1966)
st = 0.14 * scl/96.062
C Riley (1965)
ft = 0.000067 * scl/18.9984
c write(*,*) 'co2calc'
c write(*,*) k0,kk1,k2,kkw,kb,ks,kf,k1p,k2p,k3p,ksi
c write(*,*) ff,htotal
c write(*,*) bt,st,ft,sit,pt,ta
C*************************************************************************
C
C Calculate [H+] total when DIC and TA are known at T, S and 1 atm.
C The solution converges to err of xacc. The solution must be within
C the range x1 to x2.
C
C If DIC and TA are known then either a root finding or iterative method
C must be used to calculate htotal. In this case we use the Newton-Raphson
C "safe" method taken from "Numerical Recipes" (function "rtsafe.f" with
C error trapping removed).
C
C As currently set, this procedure iterates about 12 times. The x1 and x2
C values set below will accomodate ANY oceanographic values. If an initial
C guess of the pH is known, then the number of iterations can be reduced to
C about 5 by narrowing the gap between x1 and x2. It is recommended that
C the first few time steps be run with x1 and x2 set as below. After that,
C set x1 and x2 to the previous value of the pH +/- ~0.5. The current
C setting of xacc will result in co2star accurate to 3 significant figures
C (xx.y). Making xacc bigger will result in faster convergence also, but this
C is not recommended (xacc of 10**-9 drops precision to 2 significant figures).
C
C Parentheses added around negative exponents (Keith Lindsay)
C
x1 = 10.0**(-phhi)
x2 = 10.0**(-phlo)
xacc = 1.e-10
htotal=drtsafe(ta_iter_1,x1,x2,xacc)
c write(*,*) 'htotal', htotal
C
C Calculate [CO2*] as defined in DOE Methods Handbook 1994 Ver.2,
C ORNL/CDIAC-74, Dickson and Goyet, eds. (Ch 2 p 10, Eq A.49)
C
htotal2=htotal*htotal
co2star = 1.0
co2star=dic*htotal2/(htotal2 + kk1*htotal + kk1*k2)
co2starair=xtco2*ff*atmpres
dco2star=co2starair-co2star
ph=-log10(htotal)
c write(*,*) 'co2calc'
c write(*,*) k12,k12p,k123p
c write(*,*) k0,kk1,k2,kkw,kb,ks,kf,k1p,k2p,k3p,ksi
c write(*,*) 'co2calc',ff,htotal
c write(*,*) bt,st,ft,sit,pt,ta
c write(*,*) 'CO2CALC'
c write(*,*) 'starair, star', co2starair, co2star
c write(*,*) 'dic, dic_in', dic, dic_in
c write(*,*) 'dco2star', dco2star
c write(*,*) 'ph',ph
c
c ---------------------------------------------------------------
cc Add two output arguments for storing pCO2surf
cc Should we be using K0 or ff for the solubility here?
c ---------------------------------------------------------------
pCO2surf = co2star / ff
dpCO2 = pCO2surf - xtco2*atmpres
pCO2atm = (pCO2surf - dpCO2) / permeg
c dco2star = dpCO2*ff
C
C Convert units of output arguments
c Note: co2star and dco2star are calculated in mol/kg within this routine
c Thus Convert now from mol/kg -> mol/m^3
co2star = co2star / permil
dco2star = dco2star / permil
c Note: pCO2surf and dpCO2 are calculated in atm above.
c Thus convert now to uatm
pCO2surf = pCO2surf / permeg
dpCO2 = dpCO2 / permeg
c dco2star = dco2star/ permeg
C
return
end
! source file: /home/andreas/models/UVic/2.6/npzd_co2/ctr/updates/ta_iter_1.F
c_ ---------------------------------------------------------------------
c_ RCS lines preceded by "c_ "
c_ ---------------------------------------------------------------------
c_
c_ Revision 1.1 2004/06/01 17:38:06 ansley
c_ add pco2 function from Andreas Schmittner
c_
c_ Revision 1.2 1999/09/01 17:55:41 orr
c_ Fixed sign error in dfn/dx following remarks of C. Voelker (10/Aug/1999)
c_
c_ Revision 1.1 1999/04/03 22:00:42 orr
c_ Initial revision
c_
c_ ---------------------------------------------------------------------
c_
subroutine ta_iter_1(x,fn,df)
include "species.h"
real k12,k12p,k123p
real x, fn, df, x2, x3, c, a, a2, da, b, b2, db
c real k0,k1,k2,kw,kb,ks,kf,k1p,k2p,k3p,ksi
C
C This routine expresses TA as a function of DIC, htotal and constants.
C It also calculates the derivative of this function with respect to
C htotal. It is used in the iterative solution for htotal. In the call
C "x" is the input value for htotal, "fn" is the calculated value for TA
C and "df" is the value for dTA/dhtotal
C
c write(*,*) 'ta_iter_1'
c write(*,*) k0,k1,k2,kw,kb,ks,kf,k1p,k2p,k3p,ksi
c write(*,*) ff,htotal
c write(*,*) bt,st,ft,sit,pt,ta
c write(*,*) x
x2=x*x
x3=x2*x
k12 = kk1*k2
k12p = k1p*k2p
k123p = k12p*k3p
c = 1.0 + st/ks
a = x3 + k1p*x2 + k12p*x + k123p
a2=a*a
da = 3.0*x2 + 2.0*k1p*x + k12p
b = x2 + kk1*x + k12
b2=b*b
db = 2.0*x + kk1
C
C fn = hco3+co3+borate+oh+hpo4+2*po4+silicate+hfree+hso4+hf+h3po4-ta
C
fn = kk1*x*dic/b +
& 2.0*dic*k12/b +
& bt/(1.0 + x/kb) +
& kkw/x +
& pt*k12p*x/a +
& 2.0*pt*k123p/a +
& sit/(1.0 + x/ksi) -
& x/c -
& st/(1.0 + ks/(x*c)) -
& ft/(1.0 + kf/x) -
& pt*x3/a -
& ta
C
C df = dfn/dx
C
df = ((kk1*dic*b) - kk1*x*dic*db)/b2 -
& 2.0*dic*k12*db/b2 -
& bt/kb/(1.0+x/kb)**2. -
& kkw/x2 +
& (pt*k12p*(a - x*da))/a2 -
& 2.0*pt*k123p*da/a2 -
& sit/ksi/(1.0+x/ksi)**2. -
& 1.0/c +
& st*(1.0 + ks/(x*c))**(-2.0)*(ks/(c*x2)) +
& ft*(1.0 + kf/x)**(-2.)*kf/x2 -
& pt*x2*(3.0*a-x*da)/a2
c write(*,*) k12,k12p,k123p
c write(*,*) fn, df
return
end
! source file: /home/andreas/models/UVic/2.6/npzd_co2/ctr/updates/drtsafe.F
c_ ---------------------------------------------------------------------
c_ RCS lines preceded by "c_ "
c_ ---------------------------------------------------------------------
c_
c_ Revision 1.1 2004/06/01 17:38:06 ansley
c_ add pco2 function from Andreas Schmittner
c_
c_ Revision 1.1 1999/04/03 22:00:42 orr
c_ Initial revision
c_
c_ ---------------------------------------------------------------------
c_
REAL FUNCTION DRTSAFE(FUNCD,X1,X2,XACC)
include "species.h"
real funcd, x1, x2, xacc, fl, df, fh, xl, xh, swap, dxold,
. dx, f, temp
integer j, maxit
C
C File taken from Numerical Recipes. Modified R.M.Key 4/94
C
MAXIT=100
CALL FUNCD(X1,FL,DF)
CALL FUNCD(X2,FH,DF)
IF(FL .LT. 0.0) THEN
XL=X1
XH=X2
ELSE
XH=X1
XL=X2
SWAP=FL
FL=FH
FH=SWAP
END IF
DRTSAFE=.5*(X1+X2)
DXOLD=ABS(X2-X1)
DX=DXOLD
CALL FUNCD(DRTSAFE,F,DF)
DO 100, J=1,MAXIT
IF(((DRTSAFE-XH)*DF-F)*((DRTSAFE-XL)*DF-F) .GE. 0.0 .OR.
& ABS(2.0*F) .GT. ABS(DXOLD*DF)) THEN
DXOLD=DX
DX=0.5*(XH-XL)
DRTSAFE=XL+DX
IF(XL .EQ. DRTSAFE)RETURN
ELSE
DXOLD=DX
DX=F/DF
TEMP=DRTSAFE
DRTSAFE=DRTSAFE-DX
IF(TEMP .EQ. DRTSAFE)RETURN
END IF
IF(ABS(DX) .LT. XACC)RETURN
CALL FUNCD(DRTSAFE,F,DF)
IF(F .LT. 0.0) THEN
XL=DRTSAFE
FL=F
ELSE
XH=DRTSAFE
FH=F
END IF
100 CONTINUE
RETURN
END
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