NONLINEAR LEAST SQUARES ANALYSIS OF CATALYTIC RATE MODELS

[1] CATALYTIC REDUCTION OF NITRIC OXIDE [J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1962, 1 (03): : 204 - &

[2] BLAKEMORE JW, 1963, CHEM ENG PROGR S SER, V59, P14

[3] FITTING EMPIRICAL DATA [J]. ANNALS OF THE NEW YORK ACADEMY OF SCIENCES, 1960, 86 (03) : 792 - 816

[4] BOX GEP, 1965, IBM SCI COMP S STAT, P113

[5] BOX GEP, 1965, 51 DEP STAT TECH REP

[6] LEAST SQUARES [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1958, 50 (05): : 799 - 802

[7] Solid catalysts and reaction rates [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1943, 35 : 529 - 541

[8] HOUGEN OA, 1947, CHEMICAL PROCESS P 3

[9] DESIGNS FOR DISCRIMINATING BETWEEN 2 RIVAL MODELS [J]. TECHNOMETRICS, 1965, 7 (03) : 307 - &

[10] KITTRELL JR, TO BE PUBLISHED

[1] CATALYTIC REDUCTION OF NITRIC OXIDE [J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1962, 1 (03): : 204 - &

[2] BLAKEMORE JW, 1963, CHEM ENG PROGR S SER, V59, P14

[3] FITTING EMPIRICAL DATA [J]. ANNALS OF THE NEW YORK ACADEMY OF SCIENCES, 1960, 86 (03) : 792 - 816

[4] BOX GEP, 1965, IBM SCI COMP S STAT, P113

[5] BOX GEP, 1965, 51 DEP STAT TECH REP

[6] LEAST SQUARES [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1958, 50 (05): : 799 - 802

[7] Solid catalysts and reaction rates [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1943, 35 : 529 - 541

[8] HOUGEN OA, 1947, CHEMICAL PROCESS P 3

[9] DESIGNS FOR DISCRIMINATING BETWEEN 2 RIVAL MODELS [J]. TECHNOMETRICS, 1965, 7 (03) : 307 - &

[10] KITTRELL JR, TO BE PUBLISHED