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Setting up web subdirectory in repository
1 REQUIRE "column.a4l";
2 (* => column.a4l, flash.a4l, stream_holdup.a4l, thermodynamics.a4l,
3 * components.a4l, phases.a4l, atoms.a4l, measures.a4l, system.a4l,
4 * basemodel.a4l *)
5 REQUIRE "plot.a4l";
6 (* => plot.a4l, atoms.a4l, measures.a4l, system.a4l, basemodel.a4l *)
7 PROVIDE "plotcol.a4c";
8 (*
9 * This file is part of the ASCEND Modeling Library and is released
10 * under the GNU Public License as described at the end of this file.
11 *)
12
13 MODEL demo_plot_column(
14 components IS_A set OF symbol_constant;
15 reference IS_A symbol_constant;
16 n_trays IS_A integer_constant;
17 feed_location IS_A integer_constant;
18 ) WHERE (
19 reference IN components == TRUE;
20 n_trays > 5;
21 feed_location > 2;
22 feed_location < n_trays - 2;
23 ) REFINES demo_column;
24
25 z_eq_tray_set ALIASES Column.VLE_set;
26 z_eq_tray_coord[z_eq_tray_set] IS_A real;
27
28 z_eq_tray_above_set IS_A set OF integer_constant;
29 z_eq_tray_above_set :== [0 .. Column.N_trays-1];
30 z_eq_tray_above_coord[z_eq_tray_above_set] IS_A real;
31
32 z_all_tray_set IS_A set OF integer_constant;
33 z_all_tray_set :== [0 .. Column.N_trays];
34 z_all_tray_coord[z_all_tray_set] IS_A real;
35
36 z_icmp IS_A set OF integer_constant;
37 z_icmp :== [1..CARD[components]];
38
39 Profile IS_A simple_column_profiles(Column);
40
41 FOR i IN [components] CREATE
42 x_curves[i] IS_A plt_curve(
43 Profile.zx[i],
44 Profile.x[i],
45 z_eq_tray_coord
46 );
47 y_curves[i] IS_A plt_curve(
48 Profile.zy[i],
49 Profile.y[i],
50 z_eq_tray_coord
51 );
52 k_curves[i] IS_A plt_curve(
53 Profile.zk[i],
54 Profile.kvalues_when_full_thermo[i],
55 z_eq_tray_coord
56 );
57 END FOR;
58
59 t_curve IS_A plt_curve(Profile.zT,Profile.T,z_eq_tray_coord);
60 t_curves[1] ALIASES t_curve;
61
62 p_curve IS_A plt_curve(Profile.zP,Profile.P,z_eq_tray_coord);
63 p_curves[2] ALIASES p_curve;
64
65 Q_curve IS_A plt_curve(Profile.zQ,Profile.Qin,z_all_tray_coord);
66 Q_curves[3] ALIASES Q_curve;
67
68 L_curve IS_A plt_curve(Profile.zL,Profile.Lin,z_eq_tray_coord);
69 L_curves[4] ALIASES L_curve;
70
71 V_curve IS_A plt_curve(Profile.zV,Profile.Vin,z_eq_tray_above_coord);
72 V_curves[5] ALIASES V_curve;
73
74 Plot_x IS_A plt_plot_symbol(components,x_curves);
75 Plot_y IS_A plt_plot_symbol(components,y_curves);
76 Plot_K IS_A plt_plot_symbol(components,k_curves);
77 Plot_T IS_A plt_plot_integer([1],t_curves);
78 Plot_P IS_A plt_plot_integer([2],p_curves);
79 Plot_Q IS_A plt_plot_integer([3],Q_curves);
80 Plot_L IS_A plt_plot_integer([4],L_curves);
81 Plot_V IS_A plt_plot_integer([5],V_curves);
82
83 (* this stuff needs work
84 (* in conversion process from bob's mcplot code.
85 SELECT (CARD[components])
86 CASE 2:
87 (* mccabe thiele plot only for 2 components *)
88
89 (* these get mapped into parameters *)
90 mceq.npnt :== Plot_x.curve[reference].npnt;
91 mcstages.npnt :== 2*(Plot_x.curve[reference].npnt) + 1;
92 mcopline.npnt :== Plot_x.curve[reference].npnt+1;
93 mcident.npnt :== 2;
94 mcqline.npnt :== 2;
95
96
97 FOR j IN [1..mceq.npnt] CREATE
98 mceq.pnt[j].x, Plot_x.curve[reference].pnt[j].y ARE_THE_SAME;
99 mceq.pnt[j].y, Plot_y.curve[reference].pnt[j].y ARE_THE_SAME;
100
101 mcstages.pnt[2*j-1], mcopline.pnt[j] ARE_THE_SAME;
102 mcstages.pnt[2*j], mceq.pnt[j] ARE_THE_SAME;
103 END FOR;
104
105 FOR j IN [2..mcopline.npnt-1] CREATE
106 mcopline.pnt[j].x, Plot_x.curve[reference].pnt[j-1].y
107 ARE_THE_SAME;
108 mcopline.pnt[j].y, Plot_y.curve[reference].pnt[j].y
109 ARE_THE_SAME;
110 END FOR;
111
112 mcstages.pnt[1].x, mcstages.pnt[1].y, Plot_y.curve[reference].pnt[1].y
113 ARE_THE_SAME;
114
115 mcstages.pnt[2*(Plot_x.curve[reference].npnt)+1].x,
116 mcstages.pnt[2*(Plot_x.curve[reference].npnt)+1].y,
117 Plot_x.curve[reference].pnt[Plot_x.curve[reference].npnt].y
118 ARE_THE_SAME;
119
120 mcstages.pnt[2*(Plot_x.curve[reference].npnt)+1],
121 mcopline.pnt[Plot_x.curve[reference].npnt+1] ARE_THE_SAME;
122
123 mcident.pnt[1], mcopline.pnt[1] ARE_THE_SAME;
124 mcident.pnt[2], mcopline.pnt[mcopline.npnt] ARE_THE_SAME;
125
126 mcqline.pnt[2], mceq.pnt[col.feed_loc] ARE_THE_SAME;
127
128 (* stuff below here or something very like should work when complete *)
129
130 (* I may be missing the distillate from mceq and mcstagex *)
131 mceq IS_A plt_curve(
132 Column.zx[reference],
133 Column.Profile_x[reference],
134 Column.Profile_y[reference]
135 );
136
137 mcstagex[mc_sx_pts] ALIASES ((
138 (Column.Profile_x[reference][k],Column.Profile_x[reference][k])
139 | k IN z_eq_tray_set),
140 Column.Profile_x[reference][Column.N_trays])
141 WHERE mc_sx_pts IS_A set OF integer_constant;
142
143 (* this one may be way off *)
144 mcstagey[mc_sy_pts] ALIASES ((
145 (Column.Profile_Y[reference][k+1],
146 Column.Profile_Y[reference][k])
147 | k IN z_eq_tray_set),
148 Column.Profile_x[reference][Column.N_trays])
149 WHERE mc_sy_pts IS_A set OF integer_constant;
150
151 (* If we get all the curves built ok, this part is a nobrainer *)
152 mc_curves[mc_set] ALIASES (mceq,mcstages,mcopline,mcident,mcqline)
153 WHERE mc_set IS_A set OF integer_constant;
154
155 Plot_MT IS_A plt_plot_integer(mc_set,mc_curves);
156
157 OTHERWISE
158 END FOR; (* select CARD components *)
159
160 *)
161 *)
162
163 METHODS
164 METHOD values;
165 RUN demo_column::values;
166 z_all_tray_coord[0] := 0;
167 FOR i IN z_eq_tray_set DO
168 z_all_tray_coord[i] := i;
169 z_eq_tray_coord[i] := i;
170 z_eq_tray_above_coord[i-1] := i-1;
171 END FOR;
172 t_curve.legend := 'temperature';
173 p_curve.legend := 'pressure';
174 Q_curve.legend := 'enthalpy';
175 V_curve.legend := 'entering vapor';
176 L_curve.legend := 'entering liquid';
177 FOR i IN components DO
178 y_curves[i].legend := i;
179 x_curves[i].legend := i;
180 k_curves[i].legend := i;
181 END FOR;
182 Plot_x.title := 'Liquid Compositions';
183 Plot_y.title := 'Vapor Compositions';
184 Plot_K.title := 'Volatilities';
185 Plot_T.title := 'Temperature';
186 Plot_P.title := 'Pressure';
187 Plot_Q.title := 'Input heat';
188 Plot_L.title := 'Liquid Flow';
189 Plot_V.title := 'Vapor Flow';
190 Plot_P.XLabel := 'tray number';
191 Plot_T.XLabel := 'tray number';
192 Plot_y.XLabel := 'tray number';
193 Plot_x.XLabel := 'tray number';
194 Plot_K.XLabel := 'tray number';
195 Plot_Q.XLabel := 'tray number';
196 Plot_L.XLabel := 'tray number';
197 Plot_V.XLabel := 'tray number';
198 Plot_T.YLabel := '{K}';
199 Plot_P.YLabel := '{Pascal}';
200 Plot_y.YLabel := 'mole fraction';
201 Plot_x.YLabel := 'mole fraction';
202 Plot_K.YLabel := 'K value';
203 Plot_Q.YLabel := 'watt';
204 Plot_L.YLabel := 'mole/s';
205 Plot_V.YLabel := 'mole/s';
206 (* make composition plots cover 0 - 1 *)
207 Plot_x.Ylow := 0;
208 Plot_x.Yhigh := 1;
209 Plot_y.Ylow := 0;
210 Plot_y.Yhigh := 1;
211
212 (* This part ok when Plot_MT is finished above.
213 IF CARD[components] == 2 THEN
214 Plot_MT.title := 'McCabe-Thiele Diagram';
215 Plot_MT.XLabel := 'Liquid composition';
216 Plot_MT.YLabel := 'Vapor composition';
217 mceq.legend := 'equilibrium';
218 mcstages.legend := 'stages';
219 mcopline.legend := 'operating line';
220 mcident.legend := 'x=y';
221 mcqline.legend := 'qline';
222 END FOR;
223 *)
224 END values;
225
226 END demo_plot_column;
227
228 MODEL testdemoplotmodel() REFINES testcmumodel();
229 METHODS
230 METHOD check_self;
231 RUN demo.check_self;
232 END check_self;
233 METHOD check_all;
234 RUN demo.check_all;
235 END check_all;
236 METHOD default_self;
237 RUN demo.default_self;
238 END default_self;
239 METHOD default_all;
240 RUN demo.scale_all;
241 END default_all;
242 METHOD scale_self;
243 RUN demo.scale_self;
244 END scale_self;
245 METHOD scale_all;
246 RUN demo.scale_all;
247 END scale_all;
248 METHOD bound_self;
249 RUN demo.bound_self;
250 END bound_self;
251 METHOD bound_all;
252 RUN demo.bound_all;
253 END bound_all;
254
255 METHOD specify;
256 RUN demo.specify;
257 END specify;
258
259 METHOD values;
260 RUN demo.values;
261 END values;
262 METHOD reset_to_mass_balance;
263 RUN demo.Column.reset_to_mass_balance;
264 END reset_to_mass_balance;
265
266 METHOD reset_to_full_thermo;
267 RUN demo.Column.reset_to_full_thermo;
268 END reset_to_full_thermo;
269
270 METHOD reset_to_adiabatic;
271 RUN demo.Column.reset_to_adiabatic;
272 END reset_to_adiabatic;
273
274 END testdemoplotmodel;
275
276 MODEL mw_demo_plot_column() REFINES testdemoplotmodel();
277 demo IS_A demo_plot_column(['methanol','water'],'water',13,7);
278 END mw_demo_plot_column;
279
280 MODEL abc_demo_plot_column() REFINES testdemoplotmodel();
281 demo IS_A
282 demo_plot_column(['benzene','chloroform','acetone'],'benzene',13,7);
283 END abc_demo_plot_column;
284
285 MODEL c567_demo_plot_column() REFINES testdemoplotmodel();
286 demo IS_A
287 demo_plot_column(['n_pentane','n_hexane','n_heptane'],'n_heptane',13,7);
288 END c567_demo_plot_column;
289
290
291 (*
292 * plotcol.a4c
293 * by Benjamin A Allan
294 * Part of the ASCEND Library
295 * $Date: 1998/06/17 19:22:22 $
296 * $Revision: 1.3 $
297 * $Author: mthomas $
298 * $Source: /afs/cs.cmu.edu/project/ascend/Repository/models/plotcol.a4c,v $
299 *
300 * This file is part of the ASCEND Modeling Library.
301 *
302 * Copyright (C) 1998 Carnegie Mellon University
303 * Copyright (C) 1997 Benjamin A Allan
304 *
305 * The ASCEND Modeling Library is free software; you can redistribute
306 * it and/or modify it under the terms of the GNU General Public
307 * License as published by the Free Software Foundation; either
308 * version 2 of the License, or (at your option) any later version.
309 *
310 * The ASCEND Modeling Library is distributed in hope that it
311 * will be useful, but WITHOUT ANY WARRANTY; without even the implied
312 * warranty of MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.
313 * See the GNU General Public License for more details.
314 *
315 * You should have received a copy of the GNU General Public License
316 * along with the program; if not, write to the Free Software
317 * Foundation, Inc., 675 Mass Ave, Cambridge, MA 02139 USA.
318 *)

john.pye@anu.edu.au
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