DAMPING COEFFICIENT DESIGN CHARTS FOR SAMPLED-DATA CONTROL OF PROCESSES WITH DEADTIMELUYBEN WL.1972; A.I.CH.E.J., NEW YORK; U.S.A.; DA. 1972; VOL. 18; NO 5; PP. 1048-1052; BIBL. 3 REF.Serial Issue

SAMPLED-DATA CONTROL OF SECOND-ORDER OPEN-LOOP UNSTABLE PROCESSESLUYBEN WL.1972; INDUSTR. ENGNG CHEM., FUNDAM.; U.S.A.; DA. 1972; VOL. 11; NO 4; PP. 557-563; BIBL. 4 REF.Serial Issue

AZEOTROPIC TOWER DESIGN BY GRAPH = CONCEPTION D'UNE TOUR AZEOTROPIQUE PAR METHODE GRAPHIQUELUYBEN WL.1973; HYDROCARBON. PROCESSG; U.S.A.; DA. 1973; VOL. 52; NO 1; PP. 109-112; BIBL. 2 REF.Serial Issue

CONSIDER REACTOR CONTROL LAGS.LUYBEN WL; MELCIC M.1978; HYDROCARBON PROCESSG; U.S.A.; DA. 1978; VOL. 57; NO 3; PP. 115-117; BIBL. 4 REF.Article

CONTROL OF SIDESTREAM COLUMNS SEPARATING TERNARY MIXTURES.DOUKAS N; LUYBEN WL.1978; INSTRUMENT. TECHNOL.; U.S.A.; DA. 1978; VOL. 25; NO 6; PP. 43-48; BIBL. 5 REF.Article

CONTROLLING HEAT INTEGRATED DISTILLATION COLUMNS.TYREUS BD; LUYBEN WL.1976; CHEM. ENGNG PROGR.; U.S.A.; DA. 1976; VOL. 72; NO 9; PP. 59-66; BIBL. 6 REF.Article

CONTROL OF A BINARY DISTILLATION COLUMN WITH SIDESTREAM DRAWOFFTYREUS B; LUYBEN WL.1975; INDUSTR. ENGNG CHEM., PROCESS DESIGN DEVELOP.; U.S.A.; DA. 1975; VOL. 14; NO 4; PP. 391-398; BIBL. 4 REF.Article

PRACTICAL CONTROL STUDIES OF BATCH REACTORS USING REALISTIC MATHEMATICAL MODELSMARROQUIN G; LUYBEN WL.1973; CHEM. ENGNG SCI.; G.B.; DA. 1973; VOL. 28; NO 4; PP. 993-1003; BIBL. 8 REF.Serial Issue

ALTERNATIVE DISTILLATION CONFIGURATIONS FOR ENERGY CONSERVATION IN FOUR-COMPONENT SEPARATIONSABOLGHASEM ELAAHL; LUYBEN WL.1983; IND. ENG. CHEM., PROCESS DES. DEV.; ISSN 0019-7882; USA; DA. 1983; VOL. 22; NO 1; PP. 80-86; BIBL. 23 REF.Article

CONTROL OF AN ENERGY-CONSERVING PREFRACTIONATOR/SIDESTREAM COLUMN DISTILLATION SYSTEMDOUKAS NP; LUYBEN WL.1981; IND. ENG. CHEM., PROCESS DES. DEV.; ISSN 0019-7882; USA; DA. 1981; VOL. 20; NO 1; PP. 147-153; BIBL. 7 REF.Article

ECONOMICS OF ALTERNATIVE DISTILLATION CONFIGURATIONS FOR THE SEPARATION OF TERNARY MIXTURESDOUKAS N; LUYBEN WL.1978; INDUSTR. ENGNG CHEM., PROCESS DESIGN. DEVELOP.; USA; DA. 1978; VOL. 17; NO 3; PP. 272-281; BIBL. 17 REF.Article

SAMPLED-DATA FEEDBACK CONTROL OF A BINARY DISTILLATION COLUMNSHUNTA JP; LUYBEN WL.1972; CANAD. J. CHEM. ENGNG; CANADA; DA. 1972; VOL. 50; NO 3; PP. 365-371; ABS. FR.; BIBL. 8 REF.Serial Issue

SAMPLED-DATA NONINTERACTING CONTROL FOR DISTILLATION COLUMNSSHUNTA JP; LUYBEN WL.1972; CHEM. ENGNG SCI.; G.B.; DA. 1972; VOL. 27; NO 6; PP. 1325-1335; ABS. FR. ALLEM.; BIBL. 7 REF.Serial Issue

CONTROL OF HIGH-PURITY DISTILLATION COLUMNSFUENTES C; LUYBEN WL.1983; INDUSTRIAL AND ENGINEERING CHEMISTRY. PROCESS DESIGN AND DEVELOPMENT; ISSN 0019-7882; USA; DA. 1983; VOL. 22; NO 3; PP. 361-366; BIBL. 4 REF.Article

COMPARISON OF ENERGY MODELS FOR DISTILLATION COLUMNSFUENTES C; LUYBEN WL.1982; IND. ENG. CHEM., FUNDAM.; ISSN 0019-7874; USA; DA. 1982; VOL. 21; NO 3; PP. 323-324; BIBL. 10 REF.Article

LIQUID-LEVEL CONTROL IN SINGLE TANKS AND CASCADES OF TANKS WITH PROPORTIONAL-ONLY AND PROPORTIONAL-INTEGRAL FEEDBACK CONTROLLERSCHEUNG TF; LUYBEN WL.1979; INDUSTR. ENGNG CHEM., FUNDAM.; USA; DA. 1979; VOL. 18; NO 1; PP. 15-21; BIBL. 4 REF.Article

PD CONTROL IMPROVES REACTOR STABILITYCHEUNG TF; LUYBEN WL.1979; HYDROCARBON PROCESSG; USA; DA. 1979; VOL. 58; NO 9; PP. 215-218; BIBL. 3 REF.Article

A FURTHER STUDY OF THE PL LEVEL CONTROLLERCHEUNG TF; LUYBEN WL.1979; I.S.A. TRANS.; USA; DA. 1979; VOL. 18; NO 2; PP. 73-77; BIBL. 2 REF.Article

REACTORS: SIZE VERSUS STABILITY.DEVIA N; LUYBEN WL.1978; HYDROCARBON PROCESSG; USA; DA. 1978; VOL. 57; NO 6 PART. 1; PP. 119-122; BIBL. 2 REF.Article

EXPERIMENTAL EVALUATION OF DIGITAL ALGORITHMS FOR ANTIRES ET WINDUP.JAWAHAR KHANDHERIA; LUYBEN WL.1976; INDUSTR. ENGNG CHEM., PROCESS DESIGN DEVELOP.; U.S.A.; DA. 1976; VOL. 15; NO 2; PP. 278-285; BIBL. 6 REF.Article

COMPARISON OF ENERGY CONSUMPTION IN FIVE HEAT-INTEGRATED DISTILLATION CONFIGURATIONSTEH PING CHIANG; LUYBEN WL.1983; INDUSTRIAL AND ENGINEERING CHEMISTRY. PROCESS DESIGN AND DEVELOPMENT; ISSN 0019-7882; USA; DA. 1983; VOL. 22; NO 2; PP. 175-179; BIBL. 10 REF.Article

STIFFNESS IN DISTILLATION MODELS AND THE USE OF AN IMPLICIT INTEGRATION METHOD TO REDUCE COMPUTATION TIMESTYREUS BD; LUYBEN WL; SCHIESSER WE et al.1975; INDUSTR. ENGNG CHEM., PROCESS DESIGN DEVELOP.; U.S.A.; DA. 1975; VOL. 14; NO 4; PP. 427-433; BIBL. 11 REF.Article

NON LINEAR AND NON CONVENTIONAL LIQUID LEVEL CONTROLLERSTAK FAI CHEUNG; LUYBEN WL.1980; INDUSTR. ENGNG. CHEM., FUNDAM.; USA; DA. 1980; VOL. 19; NO 1; PP. 93-98; BIBL. 8 REF.Article

A FLUIDIC-ELECTRONIC HYBRID SYSTEM FOR MEASURING THE COMPOSITION OF BINARY MIXTURES = SYSTEME HYBRIDE FLUIDIQUE-ELECTRONIQUE POUR MESURER LA COMPOSITION DES MELANGES BINAIRESANDERSON C; BARNETT DM; LUYBEN WL et al.1972; INDUSTR. ENGNG CHEM., FUNDAM.; U.S.A.; DA. 1972; VOL. 11; NO 3; PP. 407-409; BIBL. 5 REF.Serial Issue

HOW TO USE A SMALL CALCULATOR IN DISTILLATION COLUMN DESIGN.BUCKLEY PS; COX RK; LUYBEN WL et al.1978; CHEM. ENGNG PROGR.; U.S.A.; DA. 1978; VOL. 74; NO 6; PP. 49-55; BIBL. 14 REF.Article