Modified version that runs through current chem preprocessor

gold2718 · Aug 31, 2023 · 64f5990 · 64f5990
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diff --git a/src/chemistry/pp_trop_mam_oslo/chem_mech.doc b/src/chemistry/pp_trop_mam_oslo/chem_mech.doc
@@ -1,16 +1,5 @@
 
 
-           |--------------------------------------------------------------------------------------------------|
-           |                                                                                                  |
-           |                                                                                                  |
-           |                              This is a mam-oslo simulation with :                                |
-           |                              (1)  comments to add                                                |
-           |                              (2)  comments to add                                                |
-           |                                                                                                  |
-           |                                                                                                  |
-           |--------------------------------------------------------------------------------------------------|
-
-
      Solution species
       (  1)  SO2             
       (  2)  H2SO4           

diff --git a/src/chemistry/pp_trop_mam_oslo/chem_mech.in b/src/chemistry/pp_trop_mam_oslo/chem_mech.in
@@ -1,17 +1,16 @@
-BEGSIM 
   SPECIES
 
       Solution
  SO2, H2SO4
  DMS -> CH3SCH3, H2O2
  SO4_NA->H2SO4, SO4_A1->H2SO4, SO4_A2->NH4HSO4
  SO4_AC->H2SO4, SO4_PR->H2SO4, BC_N->C
- BC_AX->C, BC_NI->C, BC_A->C, BC_AI->C 
+ BC_AX->C, BC_NI->C, BC_A->C, BC_AI->C
  BC_AC->C, OM_NI->C, OM_AI->C, OM_AC->C
  DST_A2->AlSiO5, DST_A3->AlSiO5
  SS_A1->NaCl, SS_A2->NaCl, SS_A3->NaCl
 * Approximate soa species with those of monoterpene oxidation products
-* based on Paasonen et al. (2010); Taipale et al. (2008). 
+* based on Paasonen et al. (2010); Taipale et al. (2008).
  SOA_NA->C10H16O2, SOA_A1->C10H16O2
  SOA_LV ->C10H16O2, SOA_SV->C10H16O2
  monoterp -> C10H16, isoprene -> C5H8
@@ -36,7 +35,7 @@ BEGSIM
         DMS, SO2, H2O2
         SO4_NA, SO4_A1, SO4_A2
         SO4_AC, SO4_PR, BC_N
-        BC_AX, BC_NI, BC_A, BC_AI 
+        BC_AX, BC_NI, BC_A, BC_AI
         BC_AC, OM_NI, OM_AI, OM_AC
         DST_A2, DST_A3
         SS_A1, SS_A2, SS_A3 , H2SO4
@@ -61,7 +60,7 @@ BEGSIM
 * Then account for 0.25 which is 0.25 MSA molec per DMS molec (the other 0.75 goes to SO2)
 * Then 0.2 assumed yield for SOA_LV and 0.8 assumed  yield for SOA_SV gives the coefficients below
 * reaction rate from Chin et al 1996, JGR, vol 101, no D13
-* 
+*
  [usr_DMS_OH]  DMS + OH -> .75 * SO2 + .5 * HO2 + 0.029*SOA_LV + 0.114*SOA_SV
 *
 *cka: added organic vapor oxidation with constants from IUPAC below
@@ -106,4 +105,3 @@ BEGSIM
      End Version Options
 
    END SIMULATION PARAMETERS
-ENDSIM