STIRRED TANKS AND MIXERS FOR LIQUID EXTRACTION

[51] SEEWALD M, 1960, THESIS NEW YORK U

[52] STATISTICAL THEORIES OF TURBULENCE IN ... PREDICTING PARTICLE SIZE IN AGITATED DISPERSIONS [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1960, 52 (03): : 253 - 256

[53] PHASE SEPARATION AND MASS TRANSFER IN A LIQUID-LIQUID CYCLONE [J]. AICHE JOURNAL, 1956, 2 (04) : 545 - 551

[54] THORNTON JD, 1956, NUCLEAR ENG, V1, P204

[55] THORNTON JD, 1956, NUCLEAR ENGNG, V1, P156

[56] TREYBAL RE, 1960, AICHE J, V6, pM5

[57] THE ECONOMIC DESIGN OF MIXER-SETTLER EXTRACTORS [J]. AICHE JOURNAL, 1959, 5 (04) : 474 - 482

[58] ESTIMATION OF THE STAGE EFFICIENCY OF SIMPLE, AGITATED VESSELS USED IN MIXER-SETTLER EXTRACTORS [J]. AICHE JOURNAL, 1958, 4 (02) : 202 - 207

[59] TRICE VG, 1957, ANL5741 US AT EN COM

[60] THEORY FOR IRREVERSIBLE AND CONSTANT-PATTERN SOLID DIFFUSION [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1953, 45 (08): : 1664 - 1670

[51] SEEWALD M, 1960, THESIS NEW YORK U

[52] STATISTICAL THEORIES OF TURBULENCE IN ... PREDICTING PARTICLE SIZE IN AGITATED DISPERSIONS [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1960, 52 (03): : 253 - 256

[53] PHASE SEPARATION AND MASS TRANSFER IN A LIQUID-LIQUID CYCLONE [J]. AICHE JOURNAL, 1956, 2 (04) : 545 - 551

[54] THORNTON JD, 1956, NUCLEAR ENG, V1, P204

[55] THORNTON JD, 1956, NUCLEAR ENGNG, V1, P156

[56] TREYBAL RE, 1960, AICHE J, V6, pM5

[57] THE ECONOMIC DESIGN OF MIXER-SETTLER EXTRACTORS [J]. AICHE JOURNAL, 1959, 5 (04) : 474 - 482

[58] ESTIMATION OF THE STAGE EFFICIENCY OF SIMPLE, AGITATED VESSELS USED IN MIXER-SETTLER EXTRACTORS [J]. AICHE JOURNAL, 1958, 4 (02) : 202 - 207

[59] TRICE VG, 1957, ANL5741 US AT EN COM

[60] THEORY FOR IRREVERSIBLE AND CONSTANT-PATTERN SOLID DIFFUSION [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1953, 45 (08): : 1664 - 1670