The Synergistic Extraction of Lanthanides with Trifluoroacetylcycloalkanones and Trioctylphosphine Oxide

1997 ◽  
Vol 26 (8) ◽  
pp. 771-772 ◽  
Author(s):  
Shigeo Umetani ◽  
Yusuke Kawase ◽  
Quyen T. H. Le ◽  
Masakazu Matsui
Keyword(s):  
Synergistic Extraction ◽  
Trioctylphosphine Oxide

scholarly journals Preconcentration of cadmium(II) using synergistic extraction with dithizone and trioctylphosphine oxide.

1982 ◽  
Vol 31 (4) ◽  
pp. E151-E155 ◽  
Author(s):  
Hideo AKAIWA ◽  
Hiroshi KAWAMOTO ◽  
Takako KOIZUMI ◽  
P.W. SCHINDLER
Keyword(s):  
Synergistic Extraction ◽  
Trioctylphosphine Oxide

Evaluation of Kinetic Parameters at the Transport of Indole-3-acetic Acid Through Bulk Liquid Membranes

2017 ◽  
Vol 68 (5) ◽  
pp. 903-907
Author(s):  
Ecaterina Anca Serban ◽  
Ioana Diaconu ◽  
Elena Ruse ◽  
Georgiana Ileana Badea ◽  
Adriana Cuciureanu ◽  
...  
Keyword(s):  
Acetic Acid ◽  
Kinetic Parameters ◽  
Trioctylphosphine Oxide ◽  
Bulk Liquid ◽  
Transport Parameters ◽  
Kinetics Parameters ◽  
First Order ◽  
Phase Concentration ◽  
Feed Phase ◽  
Indole 3 Acetic Acid

Indole-3-acetic acid is a growth phytohormone considered the most important representative of auxin class. This paper presents the assessment of some kinetic parameters in the process of transport of indole-3-acetic acid taking into consideration the kinetic model of consecutive irreversible first order reactions. It was pursued the influence upon the process of parameters such as: feed phase concentration, stripping phase concentration in the presence of two type carriers: tributyl phosphate (TBP) and trioctylphosphine oxide (TOPO). Depending on these transport parameters were calculated kinetics parameters such as: pseudo-first-order apparent membrane entrance and exit rate constants, the maximum flux at the entrance and exit out of the membrane. The highest values of the transport flux is obtained in the presence of carrier trioctylphosphine oxide (TOPO) at the concentration in the feed phase of 10-4 mol/L indole-3-acetic acid and a concentration of 10--2mol/L NaOH in the stripping phase.

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