>From ekh@chembio.ntnu.no Sun Jun 4 12:26:07 2000 ------------------------------------------ SPEEDUP files by Katrine Hilmen ------------------------------------------ -model described within each input file -recipe on how to run speedup -explanation of commands 9.0k Jun 4 10:47 batch_4comp.speedup 17k Jun 4 10:47 batch_nonideal.speedup 23k Jun 4 11:53 ex_batch_ewetg_20trays.speedup 34k Jun 4 11:52 ex_middle_amw_PI_PI_basic.speedup 37k Jun 4 11:18 ex_middle_amw_PI_PI_liqbypass.speedup 9.1k Jun 4 11:04 simple_nonideal.speedup 22k Jun 4 10:34 threevessel_alphaconst_infty.speedup 32k Jun 4 11:13 threevessel_mep_30trays.speedup 26k Jun 4 11:15 twovessel_acb_15trays.speedup 19k Jun 4 11:16 twovessel_alphaconst_low.speedup 26k Jun 4 11:14 twovessel_amw_15trays.speedup REGULAR MULTICOMPONENT BATCH DISTILLATION (constant reflux policy) batch_4comp.speedup: ideal constant relative volatility mixture with four components batch_nonideal.speedup: nonideal ternary mixture (Antoine and Wilson equation) MULTIVESSEL BATCH DISTILLATION (closed operation with P-control of temperature) twovessel_alphaconst_low.speedup: two vessels, ternary constant relative volatility mixture twovessel_acb_15trays.speedup: two vessels, acetone-chloroform-benzene twovessel_amw_15trays.speedup: two vessels, acetone-methanol-water threevessel_alphaconst_infty.speedup: three vessels, constant relative volatility mixture threevessel_mep_30trays.speedup: three vessels, methanol-ethanol-propanol EXTRACTIVE BATCH DISTILLATION IN CONVENTIONAL COLUMN ex_batch_ewetg_20trays.speedup: ternary azeotropic mixture, ethanol-water-ethylene glycol EXTRACTIVE BATCH DISTILLATION IN MIDDLE VESSEL COLUMN ex_middle_amw_PI_PI_basic.speedup: both vapor and liquid flow through the middle vessel, PI-control of temperature, acetone-methanol-water ex_middle_amw_PI_PI_liqbypass.speedup:liquid flow bypasses middle vessel, PI-control of temperature, acetone-methanol-water SIMPLE DISTILLATION (also called Raleigh distillation) simple_nonideal.speedup: calculation of residue curves, ternary azeotropic mixture, methanol-acetone-chloroform MATLAB files for calculation of nonideal VLE are located in separate directory -Katrine >From ekh@chembio.ntnu.no Tue Nov 28 10:22:23 2000 Speedup fila (App. A) med extractive middle vessel, liquid bypass, variable reboiler holdup og CC- og TC- loop (PI control) ligger under ex_middle_amw_PI_PI_liqbypass_reb.speedup