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Poly(amide imide)s and poly(amide imide) composite membranes by interfacial polymerization
Author(s) -
Buch Premang R,
Mohan D Jagan,
Reddy Alamuru VR
Publication year - 2006
Publication title -
polymer international
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.592
H-Index - 105
eISSN - 1097-0126
pISSN - 0959-8103
DOI - 10.1002/pi.1907
Subject(s) - polymer chemistry , polyamide , interfacial polymerization , terephthaloyl chloride , imide , condensation polymer , amide , aqueous solution , chemistry , polymerization , chloride , dimethylformamide , glass transition , monomer , materials science , polymer , organic chemistry , solvent
Novel amic acid diamines (AADs) (2‐carboxyterephthalamido‐bis(alkyl or aryl amine)s, H 2 NXNH(O)CC 6 H 3 (COOH)C(O)NHXNH 2 , where X iswere synthesized by reacting trimellitic anhydride chloride with aromatic or aliphatic diamines in dimethylformamide at 5–10 °C. Poly(amide imide)s (PAIs) with an amide to imide ratio of three in the polymer chains were prepared by interfacial polycondensation of the AADs in aqueous alkaline solution with isophthaloyl chloride or terephthaloyl chloride in dichloromethane at ambient temperature to form poly(amide amic acid)s, followed by their subsequent thermal cycloimidization. All of the PAIs were soluble in polar aprotic solvents such as dimethylformamide, dimethylacetamide, dimethyl sulfoxide and N ‐methylpyrrolidone, and have inherent viscosities in the range 0.15–0.48 dL g −1 . The polymers were characterized by IR and NMR spectroscopy, TGA and DSC techniques. The PAIs have initial decomposition temperatures in the range 250–460 °C in air, and glass transition temperatures of 128–320 °C, depending upon the structures of the monomers. Composite membranes containing a poly(amide amic acid) and poly(amide imide) barrier layer on the top of a porous polyethersulfone support were prepared by in situ interfacial polymerization of the AADs in aqueous alkaline solution with trimesoyl chloride in hexane, and subsequent curing. The performances of these membranes were evaluated by using aqueous feed solutions containing 2000 ppm NaCl, Na 2 SO 4 or CaCl 2 . Copyright © 2006 Society of Chemical Industry