4.7 Article

Selective recovery of carboxylic acid through PVDF blended anion exchange membranes using electrodialysis

期刊

出版社

ELSEVIER
DOI: 10.1016/j.seppur.2022.121069

关键词

Ion-exchange equilibrium; Multivalent anions recovery; Membrane adsorption; Transport number; Membrane conductivity

资金

  1. Uchchatar Avishkar Yojana program of Ministry of Human Resource Development, Government of India
  2. Ministry of Environment, Forest and Climate Change, Government of India
  3. Permionics Membranes Private Limited, India [UAY-IITR_007, CSR/UAY/2016/SN]
  4. Imprint2 program of Science and Engineering Research Board, Government of India [IMP/2018/000282]
  5. University Grant Commission (UGC), India
  6. Gujarat Council of Science and Technology, Department of Science and Technology, GUJCOST [GUJCOST/STI/2020-2021/2251]

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Selective transport of carboxylic acids (acetic, AA; malic, MA; and citric, CA) from their equimolar ternary mixture was investigated through electrodialysis. The study found that BM-2 membrane exhibited higher selectivity for AA, which was attributed to its highest ion exchange capacity and ion conductivity.
Selective transport of carboxylic acids (acetic, AA; malic, MA; and citric, CA) from their equimolar (0.1 mol.L-1) ternary mixture was investigated through electrodialysis (ED) using three different anion exchange membranes [(i) Fumatech, FAB-PK-130, and two indigenous membranes made by solution blend of polyvinylidene fluoride (PVDF): copolymer of polymethyl methacrylate-co-polychloromethyl styrene (PMMA-co-PCMSt) at (ii) 50:50 wt % (BM-1), and (iii) 30:70 wt% (BM-2) followed by aminating them using tetramethyl 1,6 diamino hexane]. Recovery ratio (RR) for AA/MA and AA/CA mixtures were 1.97 and 2.71 respectively, indicating higher selectivity for AA through BM-2 and the same was explained based on highest ion exchange capacity (2.10 meq.g(-1)) and ion conductivity (2.3 mS.cm(-1)) data. Selective transport of AA was further endorsed by ED performance separately done with AA, MA and CA (0.1 mol.L-1 each) and equimolar binary (AA/MA) mixture at pH 7.5. Increasing trend in AA recovery: FAB-PK-130 < BM-1 < BM-2 at pH 7.5 was further supported by physical properties of the electrolyte (transport number from binary/ternary mixture) and membrane (water uptake, fractional adsorption, and ion conductivity) separately with each membrane. Highest current efficiency of 63.7% (energy consumption 5.13 kWh.kg(-1)) could be achieved with AA during ED analysis of ternary mixture through BM-2.

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