DESIGN OF DIRECT CONTACT COOLER-CONDENSERS

[1] ACKERMANN G, 1937, FORSCHUNGSHEFT, V382, P1

[2] BRAS GH, 1955, CHEM ENG, V62, P195

[3] BRAS GHP, 1954, CHEM ENG, V61, P191

[4] BRAS GHP, 1956, PETROL REFINER, V35, P215

[5] BRAS GHP, 1956, PETROL REFINER, V35, P191

[6] UNI-DIRECTIONAL HEAT AND MASS TRANSFER AT HIGH HUMIDITIES IN A WETTED WALL COLUMN [J]. CHEMICAL ENGINEERING SCIENCE, 1955, 4 (05) : 221 - 228

[7] Mass transfer (absorption) coefficients - Prediction from data on great transfer and fluid friction [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1934, 26 : 1183 - 1187

[8] Colburn AP, 1937, T AM INST CHEM ENG, V33, P0197

[9] Design of cooler condensers for mixtures of vapors with noncondensing gases [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1934, 26 : 1178 - 1182

[10] Rate of absorption of ammonia by water in a packed tower [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1941, 33 : 485 - 492

[1] ACKERMANN G, 1937, FORSCHUNGSHEFT, V382, P1

[2] BRAS GH, 1955, CHEM ENG, V62, P195

[3] BRAS GHP, 1954, CHEM ENG, V61, P191

[4] BRAS GHP, 1956, PETROL REFINER, V35, P215

[5] BRAS GHP, 1956, PETROL REFINER, V35, P191

[6] UNI-DIRECTIONAL HEAT AND MASS TRANSFER AT HIGH HUMIDITIES IN A WETTED WALL COLUMN [J]. CHEMICAL ENGINEERING SCIENCE, 1955, 4 (05) : 221 - 228

[7] Mass transfer (absorption) coefficients - Prediction from data on great transfer and fluid friction [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1934, 26 : 1183 - 1187

[8] Colburn AP, 1937, T AM INST CHEM ENG, V33, P0197

[9] Design of cooler condensers for mixtures of vapors with noncondensing gases [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1934, 26 : 1178 - 1182

[10] Rate of absorption of ammonia by water in a packed tower [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1941, 33 : 485 - 492