TRANSIENT RESPONSE STUDY OF GAS FLOWING THROUGH IRRIGATED PACKING

[1] SOME REMARKS ON LONGITUDINAL MIXING OR DIFFUSION IN FIXED BEDS [J]. AICHE JOURNAL, 1957, 3 (02) : 280 - 282

[2] AXIAL DISPERSION OF MASS IN FLOW THROUGH FIXED BEDS [J]. AICHE JOURNAL, 1958, 4 (03) : 367 - 375

[3] DYNAMIC CHARACTERISTICS OF DOUBLE-PIPE HEAT EXCHANGERS [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1956, 48 (06): : 1031 - 1034

[4] Cramer H, 1955, ELEMENTS PROBABILITY

[5] THE DISTRIBUTION OF RESIDENCE-TIMES IN AN INDUSTRIAL FLUIDISED REACTOR [J]. CHEMICAL ENGINEERING SCIENCE, 1954, 3 (01) : 26 - 35

[6] CONTINUOUS FLOW SYSTEMS - DISTRIBUTION OF RESIDENCE TIMES [J]. CHEMICAL ENGINEERING SCIENCE, 1953, 2 (01) : 1 - 13

[7] GAS ABSORPTION ACCOMPANIED BY CHEMICAL REACTION [J]. AICHE JOURNAL, 1955, 1 (04) : 456 - 463

[8] DIFFUSION IN BEDS OF POROUS SOLIDS - MEASUREMENT BY FREQUENCY RESPONSE TECHNIQUES [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1953, 45 (06): : 1219 - 1227

[9] DEISLER PF, 1955, ANAL CHEM, V27, P1366

[10] DEMARIA F, 1958, THESIS U MICH ANN AR

[1] SOME REMARKS ON LONGITUDINAL MIXING OR DIFFUSION IN FIXED BEDS [J]. AICHE JOURNAL, 1957, 3 (02) : 280 - 282

[2] AXIAL DISPERSION OF MASS IN FLOW THROUGH FIXED BEDS [J]. AICHE JOURNAL, 1958, 4 (03) : 367 - 375

[3] DYNAMIC CHARACTERISTICS OF DOUBLE-PIPE HEAT EXCHANGERS [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1956, 48 (06): : 1031 - 1034

[4] Cramer H, 1955, ELEMENTS PROBABILITY

[5] THE DISTRIBUTION OF RESIDENCE-TIMES IN AN INDUSTRIAL FLUIDISED REACTOR [J]. CHEMICAL ENGINEERING SCIENCE, 1954, 3 (01) : 26 - 35

[6] CONTINUOUS FLOW SYSTEMS - DISTRIBUTION OF RESIDENCE TIMES [J]. CHEMICAL ENGINEERING SCIENCE, 1953, 2 (01) : 1 - 13

[7] GAS ABSORPTION ACCOMPANIED BY CHEMICAL REACTION [J]. AICHE JOURNAL, 1955, 1 (04) : 456 - 463

[8] DIFFUSION IN BEDS OF POROUS SOLIDS - MEASUREMENT BY FREQUENCY RESPONSE TECHNIQUES [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1953, 45 (06): : 1219 - 1227

[9] DEISLER PF, 1955, ANAL CHEM, V27, P1366

[10] DEMARIA F, 1958, THESIS U MICH ANN AR