/[ascend]/trunk/models/steam/dsgsat2.a4c
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revision 1122 by johnpye, Fri Jan 12 02:43:17 2007 UTC revision 1123 by johnpye, Fri Jan 12 12:17:37 2007 UTC
# Line 26  MODEL dsgsat2; Line 26  MODEL dsgsat2;
26      A, A_w IS_A area;      A, A_w IS_A area;
27      h_int IS_A heat_transfer_coefficient; (* internal *)      h_int IS_A heat_transfer_coefficient; (* internal *)
28      h_ext IS_A heat_transfer_coefficient; (* external *)      h_ext IS_A heat_transfer_coefficient; (* external *)
29      A = 1{PI}*D^2/4;      z_A: A = 1{PI}*D^2/4;
30      A_w = 1{PI}*(D_2^2 - D^2)/4;      z_Aw: A_w = 1{PI}*(D_2^2 - D^2)/4;
31      dz IS_A distance;      dz IS_A distance;
32      L IS_A distance;      L IS_A distance;
33      dz = L / n;      z_dz: dz = L / n;
34    
35      (* fluid properties *)      (* fluid properties *)
36      node[1..n] IS_A satsteamstream;      node[1..n] IS_A satsteamstream;
37            
38      (* flow properties *)      (* flow properties *)
39      vel[1..n] IS_A speed;      vel[1..n] IS_A speed;
40      T_w[1..n] IS_A temperature;      T_w[2..n] IS_A temperature;
41      T[1..n] IS_A temperature;      T[1..n] IS_A temperature;
42    
43      (* constants, for the moment: *)      (* constants, for the moment: *)
44      f IS_A positive_factor;      f IS_A positive_factor;
45      mu_f IS_A viscosity;      (* mu_f IS_A viscosity; *)
46      T_amb IS_A temperature;      T_amb IS_A temperature;
47    
48      (* system dynamics *)        (* system dynamics *)  
# Line 51  MODEL dsgsat2; Line 51  MODEL dsgsat2;
51      rhou[1..n] IS_A energy_per_volume;      rhou[1..n] IS_A energy_per_volume;
52    
53      FOR i IN [1..n] CREATE      FOR i IN [1..n] CREATE
54          vel[i] = node[i].v*node[i].mdot/A;          z_vel[i]: vel[i] = node[i].v*node[i].mdot/A;
55          rhou[i] = node[i].rho * node[i].u;          z_rhou[i]: rhou[i] = node[i].rho * node[i].u;
56      END FOR;      END FOR;
57    
58      (* some aliases just for easier review of the state of the model *)      (* some aliases just for easier review of the state of the model *)
# Line 100  METHOD configure_steady; Line 100  METHOD configure_steady;
100  END configure_steady;  END configure_steady;
101  METHOD bound_steady;  METHOD bound_steady;
102      RUN bound_self;      RUN bound_self;
103      T_w[1..n].upper_bound := 1000 {K};      T_w[2..n].upper_bound := 1000 {K};
104  END bound_steady;  END bound_steady;
105  METHOD specify_steady;  METHOD specify_steady;
106      (* change to a proper steady-state problem, with fluid properties FREEd *)      (* change to a proper steady-state problem, with fluid properties FREEd *)
# Line 114  METHOD specify_steady; Line 114  METHOD specify_steady;
114      FIX qdot_s;      FIX qdot_s;
115      FIX D, D_2, L;      FIX D, D_2, L;
116      FIX h_int, c_w, rho_w, h_ext;      FIX h_int, c_w, rho_w, h_ext;
117      FIX f, mu_f;      FIX f;
118        (* FIX mu_f; *)
119      FIX T_amb;      FIX T_amb;
120      (* fix derivatives to zero *)      (* fix derivatives to zero *)
121      FOR i IN [2..n] DO      FOR i IN [2..n] DO
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john.pye@anu.edu.au
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