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Lim y = Kw, Lim y = z; Lim x = w, Lim x = z/K.
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Relative humidity is 64 percent. -1 maximum of 2.907 lb of water is vaporized for every pound of steam condensed. d masimum of 5.814 lb of solution can be fed for each pound of steam. 1 2 . 4 Mother liquor to feed ratio is 0.535 lb/lb. 12.5 Heavy distillate is O.O21F, light distillate is 0.709P; reflus is 0.54F, and vapor flow is 1.27E . 12.6 Heavy distillate is manipulated to control interface level in the decanter. Because reflus flow is less than that of light distillate, it can be accurately manipulated for composition control; decanter level is then controlled by manipulation of light distillate. Vapor and reflus flow interact in their effect on bottoms comp o s i t i o n . They can be determined from feed composition by I = F(9zc - ze), L = 1 (8zc - 22B). Two bottoms-composition controllers are necessary, their o u t p u t s mn and mc taking the place of the unknown feed compositions in the prev i o u s e q u a t i o n s . Then the decoupling control system manipulates heat input and reflus with a forward loop from feed rate: V = F(9mc - mE), 1, = ZF(8mc - 2me).
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A Absorption, 326-328 combined with stripping, 328329 material balance in, 328 optimizing control of, 225-227 Absorption coefficient, 226 Accumulator, reflux, 302-304 Accuracy, in decoupling systems, 199 in feedforward systems, 219 Acids, ionization of, 275-277 Adaptation in feedforward-feedback systems, 223, 224 Adaptive control, 170-179 dividers in, 176, 177 dynamic, 171-174, 223 feedforward, 175, 223-227 programmed, 172 self-adaptive, 173, 176-179 steady-state, 174-179, 225-227 Adiabatic drying, 344, 345
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Adjusting controllers (see Controller settings) Adjusting dynamic compensation, 217-219 Agitation (see Mixing) Analyzers, in distillation, 303-305 response of, 83, 84 sampling, 110 Answers to problems, 349-353 Antiwindup switch, 97, 98 Auctioneering, 168 Averaging control, 147, 148 Azeotrope, 340 binary, 340, 341 heterogeneous, 340 homogeneous, 341, 342 ternary, 341 Azeotropic distillation, 340-342 B Bases, ionization of, 275-277 Batch distillation (see Distillation, batch) 357
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Index Batch-process control, 96-98 (See also Reactors, batch) Bias in proportional control, 10 Blending systems, 80-86 coupling in, 191, 195, 200-202 digital, 164-167 Boilers, drum, 244-246 feedforward control of, 245-249 once-through, 246-249 Boiling-point rise, 333 Boilup, in distillation, 292 in stripping, 329 Boilup ratio, 292-294 constant, 294, 295, 308 minimum, 293 variable, 295, 308, 309 Buffering of weak acids and bases, 277 Composition control, in distillation, batch, 319-323 continuous, 303-311 in reactors, batch, 285, 286 continuous, 270 with recycle, 270, 271 (See also End-point control; pH control) Compressors, antisurge control of, 254, 255 centrifugal, 253-255 reciprocating, 253 selective control of, 167, 168 Computing systems, for controlled variables, 187, 188 for conversion in reactors, 273, 274 for decoupling, 200-202 for economic variables, 188 for feedforward control, 208-226 Condensers, 239-241 in distillation, 299-302 Contour plots, 227 for distillation, 314 Control algorithms for DDC, 119, 120 Control interval of a sampling controller, 114 Control loop, dynamic elements in, 3-35 interrupting, 110-117 properties of, 4-6 Control valves (see Valves) Controller, with complementary feedback, 103-110 integral (reset), 12-14 linear (see Linear controllers) load response with, 93-95 nonlinear (see Nonlinear controllers) nonlinearity in, 124 on-off, 131 with differential gap, 132 in dual-mode systems, 137-141 limit cycle due to, 131 with proportional time, 133, 134 with reset and derivative, 135 three-state, 134, 135 peak-seeking, 178 pneumatic (see Pneumatic controllers) proportional, 9 input-output graph for, 126 proportional-plus-derivative, 29, 30 proportional-plus-reset, 15-17 sampling, 114-117
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C , 49 Capacity, 18 dead time and, 31-34 double, 24-31 multiple, 41-44 interacting, 38-44 noninteracting, 38-41 single, 18-24, 107 Cascade control, 154-160 of flow, 158,159 of ratio, 162, 163 of temperature, 159, 160 in distillation, 305 in reactors, 268, 283 of valve position, 158 Catalyst, 259, 260 Chemical reactions, controlling, 257-286 batch reactors, 282-286 continuous reactors, 269-274 pH control, 275-282 principles governing, 258-268 Closed loop, 14, 206 oscillation in, 4, 5 response of, 155-158 Closed-loop testing, 57 Combustion control, 241-243 Complementary feedback, 103-110 Composition control, 80-86 in blending systems, 182, 183, 191 in distillation, 288-295
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