Kazuko Morisaku
National Institute of Advanced Industrial Science and Technology
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Publication
Featured researches published by Kazuko Morisaku.
Chemical Communications | 2008
Hirokazu Narita; Kazuko Morisaku; Mikiya Tanaka
The first effective extractant capable of the selective recovery of rhodium3+ from hydrochloric acid solution, N-n-hexyl-bis(N-methyl-N-n-octylethylamide)amine (HBMOEAA), has been developed.
Solvent Extraction and Ion Exchange | 2015
Hirokazu Narita; Kazuko Morisaku; Mikiya Tanaka
Extraction of Rh(III) from a HCl solution with N,N-disubstituted amide–containing tertiary amine (ACTA) compounds (N,N-di-n-hexyl(N-methyl-N-n-octyl-ethylamide)amine (MonoAA), N-n-hexyl-bis(N-methyl-N-n-octyl-ethylamide)amine (BisAA), and tris(N-methyl-N-n-octyl-ethylamide)amine (TrisAA)) was investigated. The ACTAs extract Rh(III) more efficiently than tri-n-octylamine (TOA), and the extraction efficiency increases with increasing number of amide groups: TrisAA > BisAA > MonoAA ≫ TOA. For all ACTAs, the predominant Rh(III) complex extracted from 2 M HCl is probably {[RhCl5(H2O)]·(ACTA·H)2}. The apparent basicity of the ACTAs and TOA varies in the opposite order from that observed for the Rh(III) extraction efficiency. Rh(III) can be readily back-extracted using 10 M HCl solution possessing a high selectivity over similarly loaded Pd(II) and Pt(IV).
Solvent Extraction and Ion Exchange | 2015
Hirokazu Narita; Kazuko Morisaku; Mikiya Tanaka
Synergistic extraction of Rh(III) from relatively concentrated HCl solution was studied using two mixed solvents (di-n-hexyl sulfide (DHS)–tri-n-octylamine (TOA) and N,N′-dimethyl-N,N′-di-n-octyl-thiodiglycolamide (TDGA)–TOA) in chloroform. The Rh(III) extraction efficiency is poor when 0.5 M TOA, DHS, or TDGA is used independently. In contrast, the 0.5 M TDGA–0.5 M TOA and 0.5 M DHS–0.5 M TOA mixed solvents extract ˜90% and ˜70% of Rh(III), respectively, at maximum. Slope analyses and Job’s plots for the distribution ratios of Rh(III) at 2 M HCl show that the apparent stoichiometry of Rh(III):TOA:(DHS or TDGA) in the extracted complex is 1:2:1.
Minerals Engineering | 2008
Hirokazu Narita; Mikiya Tanaka; Kazuko Morisaku
Hydrometallurgy | 2006
Hirokazu Narita; Mikiya Tanaka; Kazuko Morisaku; Tsutomu Abe
Chemistry Letters | 2004
Hirokazu Narita; Mikiya Tanaka; Kazuko Morisaku; Tsutomu Abe
Industrial & Engineering Chemistry Research | 2014
Hirokazu Narita; Kazuko Morisaku; Ken Tamura; Mikiya Tanaka; Hideaki Shiwaku; Yoshihiro Okamoto; Shinichi Suzuki; Tsuyoshi Yaita
Solvent Extraction Research and Development-japan | 2006
Hirokazu Narita; Mikiya Tanaka; Kazuko Morisaku
Artificial Organs | 2004
Motohiro Niwa; Hiroyoshi Kawakami; Shoji Nagaoka; Toshiyuki Kanamori; Kazuko Morisaku; Toshio Shinbo; Toshiaki Matsuda; Kazunari Sakai; Sunao Kubota
Solvent Extraction Research and Development-japan | 2005
Hirokazu Narita; Mikiya Tanaka; Kazuko Morisaku
Collaboration
Dive into the Kazuko Morisaku's collaboration.
National Institute of Advanced Industrial Science and Technology
View shared research outputsNational Institute of Advanced Industrial Science and Technology
View shared research outputsNational Institute of Advanced Industrial Science and Technology
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