4.5 Article

Wet process phosphoric acid purification by solvent extraction using N-octanol and tributylphosphate mixtures

Journal

JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY
Volume 88, Issue 9, Pages 1715-1720

Publisher

WILEY
DOI: 10.1002/jctb.4023

Keywords

wet process phosphoric acid; solvent extraction; tributylphosphate; N-octanol; purification

Funding

  1. Training Program for middle-aged and young key teacher by the Chengdu University of Technology
  2. Independent Research Program for Geological resources and geological engineering characteristic key discipline by the Chengdu University of Technology [HGY-2012-09]
  3. Independent Research Program by the State Key Laboratory of Geohazard Prevention and Geoenvironment Protection [SKLGP2012Z014]

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BACKGROUNDSolvent extraction using organic extractants is an important technology for purifying wet process phosphoric acid. The purification of the wet process phosphoric acid by liquid-liquid extraction using solvent mixtures of N-octanol and tributylphosphate has been investigated. RESULTSThe purification process comprised extraction, scrubbing and stripping operations. The extraction conditions, i.e. shaking time, temperature, composition of solvent mixtures and P2O5 concentration for purification of the wet process phosphoric acid were studied. The phase diagram of the pseudo-ternary system H3PO4-H2O-solvent mixtures at 313.15K was determined. The McCabe-Thiele diagram showed that three counter-current stages achieved about 91wt% P2O5 extraction at 313.15K. Scrubbing and stripping operations using pure phosphoric acid with 10wt% P2O5 and doubly distilled water, respectively, were studied. CONCLUSIONSThe phosphoric acid finally produced was found to be high grade which met the special requirements of the user. Optimization of the extraction conditions and system was capable of providing academic and technical foundations to realize industrial production. (c) 2012 Society of Chemical Industry

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