LABORATORY REACTORS FOR CATALYTIC GAS-SOLID REACTIONS - NEW DEVELOPMENTS

[1] BARD Y, 1974, NONLINEAR PARAMETER

[2] TRANSIENT METHOD AND ELEMENTARY STEPS IN HETEROGENEOUS CATALYSIS [J]. CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 1976, 13 (02): : 121 - 148

[3] BUB G, COMMUNICATION

[4] BULIRSCH R, UNPUBLISHED

[5] DETERMINATION OF REACTION-ENGINEERING PARAMETERS IN A FIXED-BED INTEGRAL REACTOR - BOUNDARY-VALUE PROBLEM [J]. CHEMIE INGENIEUR TECHNIK, 1979, 51 (04) : 313 - 313

[6] DIEHL E, 1977, THESIS TU MUNCHEN

[7] DORAISWAMY LK, 1974, CATAL REV, V10, P177, DOI 10.1080/01614947408079629

[8] EMIG G, 1972, 5TH P EUR S CHEM REA, pB5

[9] EMIG G, 1975, CHEM ENG SCI, V29, P2339

[10] Finlayson B. A., 1972, METHOD WEIGHTED RESI

[1] BARD Y, 1974, NONLINEAR PARAMETER

[2] TRANSIENT METHOD AND ELEMENTARY STEPS IN HETEROGENEOUS CATALYSIS [J]. CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 1976, 13 (02): : 121 - 148

[3] BUB G, COMMUNICATION

[4] BULIRSCH R, UNPUBLISHED

[5] DETERMINATION OF REACTION-ENGINEERING PARAMETERS IN A FIXED-BED INTEGRAL REACTOR - BOUNDARY-VALUE PROBLEM [J]. CHEMIE INGENIEUR TECHNIK, 1979, 51 (04) : 313 - 313

[6] DIEHL E, 1977, THESIS TU MUNCHEN

[7] DORAISWAMY LK, 1974, CATAL REV, V10, P177, DOI 10.1080/01614947408079629

[8] EMIG G, 1972, 5TH P EUR S CHEM REA, pB5

[9] EMIG G, 1975, CHEM ENG SCI, V29, P2339

[10] Finlayson B. A., 1972, METHOD WEIGHTED RESI