p4_f06 - [WINGEMS PROJECT HEADER] SOURCE FILE = C:\old...

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[WINGEMS PROJECT HEADER] SOURCE FILE = C:\old transfer documents\WPS417\p4_f06.wg DATE = Wednesday, November 15, 2006 TIME = 9:36 AM VERSION DESC = 5.3 (Build 305) WINGEMS VERSION = 400 PROJECT VERSION = 3048 COMPATIBILITY = 48 LICENSE KEY = NETWORK CLICKS = 253 139 C [FILE OPTIONS] LST CLEAN = 0 KOP = 11 KPORT = 0 ADDL LST REPORT = 0 STREAM TOPOLOGY = 1 DEBUGGING INFO = 1 KPWIDE = 72 NRLINE = 60 OUT CLEAN = 0 ADDL OUT REPORTS = 0 RTWINDOW = 0 0 0 0 0 LSTWINDOW = 18 23 178 47 0 OUTWINDOW = 0 0 0 0 0 SHOW = 799 348 15 S [BROWSER TEXT] COUNT = 5 0 0 Liquor: %s#:Flow %u / %s#:SSol %u / %s#:Temp %u 1 0 Steam: %s#:Flow %u / %s#:GasPress %u / %s#:Temp %u 2 0 Gas: %s#:Flow %u / %s#:GasPress %u / %s#:Temp %u 3 0 Special gas: %s#:SGFlow %u / %s#:SGTemp %u 4 0 Generic 4 [STREAM TAG TEXT] %s#:Flow / %s#:SSol / %s#:Temp %s#:Flow / %s#:GasPress / %s#:Temp %s#:Flow / %s#:GasPress / %s#:Temp %s#:SGFlow / %s#:SGTemp Generic STRM_TAG_SIZE = 8 STRM_TAG_FONT = Arial S [STREAM TYPE COLORS] LIQUOR = 0 STEAM = 0 GAS = 0 SPGAS = 0 GENERIC = 0 G [UNITS] COUNT = 106 ARITY = 5 frac % ratio-frac ratio% cons-frac cons% moist-frac moist% sec min hr day weeks months years m cm mm um ft in m2 cm2 mm2 ft2
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in2 m3 dm3 cm3 mm3 ft3 in3 l ml gal Igal deg K deg C deg R deg F DC DF atm bars ftH2O inHg inH2O kPa mmHg mmH2O Pa psia psig DmmHg DinHg Dpsia DPa DkPa Datm Dbars mol kmol lbmol mt st g kg lb klb %mass total total liquor liquor solids od ad cal kcal Mcal Btu kBtu MMBtu J kJ MJ kWH MWH Hpdays W kW J/s kJ/s hp kappa k-num mN-m2/g Nm/g asNaOH asNa2O iter ppm pH %RelHum H2O/dry H [RESOURCES] 0 BLOCKSET 1 1 1 COMPONENTS 0 0 2 STREAMSTRUCTURE 0 0 3 UNITSET 0 0 4 UNITSET 1 0 5 UNITSET 2 0 6 DIAGRAM 0 0 7 CBPROFILE 0 1 8 END 0 0 8 [UNIT RULES] SETS = 3 CURRENT = 1 SET1 = 0 GEMS (Native) SET2 = 21 English Units 1 0 0 0 0 2 0 0 0 0 3 0 0 0 0 6 0 0 0 0 5 0 0 0 0 6 0 0 0 0 22 0 0 0 0 25 0 0 0 0 27 0 0 0 0 35 0 0 0 0 27 -11 0 0 0 35 -10 0 0 0 38 0 0 0 0 40 0 0 0 0 41 0 0 0 0 42 0 0 0 0 49 0 0 0 0 53 0 0 0 0 64 -11 0 0 0 68 -11 0 0 0 67 -64 0 0 0 70 0 0 0 0 67 -64 0 0 0 68 -68 0 0 0 67 -22 -11 -54 22 68 -25 -11 -56 25 72 27 -11 0 0 72 35 -10 0 0 73 64 -11 0 0 72 35 -10 0 0 76 64 -11 0 0 76 65 -11 0 0 79 -22 -11 -41 0 81 -25 -11 -42 0 80 -64 0 0 0 81 -68 0 0 0 80 -25 -11 -41 0 81 -25 -11 -42 0 80 -22 -11 -41 22 81 -25 -11 -42 25 88 -76 -64 0 0 88 -76 -65 0 0 SET3 = 7 Metric Units 1 0 0 0 0 2 0 0 0 0 3 0 0 0 0 6 0 0 0 0 5 0 0 0 0 6 0 0 0 0
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49 0 0 0 0 48 0 0 0 0 67 -64 0 0 0 70 0 0 0 0 67 -64 0 0 0 67 -67 0 0 0 73 64 -11 0 0 72 33 -10 0 0 [COMPONENT LIST] COUNT = 155 0 0 0 0 0.000000 0 0.000000 0.000000 0 0 0 0 0 1 3 1 -1 Liquor flow Flow 0.001000 0 0.000000 0.000000 0 0 0 0 0 2 3 1 -1 Suspended solids SuspSol 0.001000 0 0.000000 0.000000 0 0 0 0 0 2 3 1 -1 Susp. solid/Gas pr. SSol/Pr 0.001000 0 0.000000 0.000000 0 0 0 0 0 3 3 1 -1 Temperature Temp 0.001000 0 0.000000 0.000000 0 0 0 0 0 0 3 1 3 Gas temperature GasTemp 0.001000 0 0.000000 0.000000 0 0 0 0 0 2 13 1 32 Gas pressure GasPress 0.001000 0
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This note was uploaded on 08/22/2011 for the course WPS 417 taught by Professor Kirkman during the Spring '11 term at N.C. State.

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p4_f06 - [WINGEMS PROJECT HEADER] SOURCE FILE = C:\old...

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