High-speed recovery of antimony using chelating porous hollow-fiber membrane

• Published in: Journal of membrane science Vol. 214; no. 2; pp. 275 - 281
• Main Authors: Nishiyama, Shin-ya, Saito, Kaori, Saito, Kyoichi, Sugita, Kazuyuki, Sato, Katsuyuki, Akiba, Mitsuo, Saito, Tomonori, Tsuneda, Satoshi, Hirata, Akira, Tamada, Masao, Sugo, Takanobu
• Format: Journal Article
• Language: English
• Published: Elsevier B.V 01.04.2003
• Subjects: Antimony; Chelating porous membrane; Hollow-fiber; Iminodiethanol group; Antimony; Iminodiethanol group; Hollow-fiber; Chelating porous membrane
• ISSN: 0376-7388; 1873-3123
• DOI: 10.1016/S0376-7388(02)00558-6

A porous hollow-fiber membrane containing an iminodiethanol (IDE) group as the chelate-forming group was applied to the recovery of antimony in the permeation mode. An antimony solution was forced to permeate through the pores of the chelating porous hollow-fiber membrane, driven by a transmembrane pressure. The membrane with a thickness of 0.7 mm and a porosity of 70% had an iminodiethanol group of 1.6 mol/kg of the membrane and a water flux of 0.95 m/h at 0.1 MPa and 298 K. The breakthrough curves of antimony overlapped irrespective of the permeation rate of the antimony solution ranging from 2 to 20 ml/min, i.e. the residence time across the membrane thickness ranging from 3.4 to 0.34 s, because of negligible diffusional mass-transfer resistance of the ionic species of antimony to the iminodiethanol group. At antimony concentrations below 10 mg/l (pH 4.0), a linear adsorption isotherm was obtained. The adsorbed antimony was quantitatively eluted by permeation of 2 M hydrochloric acid through the pores of the membrane.