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Production and Recovery of Pyruvic Acid: Recent Advances

  • Dharm Pal
  • Amit Keshav
  • Bidyut Mazumdar
  • Awanish Kumar
  • Hasan Uslu
Review Paper

Abstract

Pyruvic acid is an important keto-carboxylic acid and can be manufactured by both chemical synthesis and biotechnological routes. In the present paper an overview of recent developments and challenges in various existing technique for the production and recovery of pyruvic acid from fermentation broth or from waste streams has been presented. The main obstacle in biotechnological production of pyruvic acid is development of suitable microorganism which can provide high yield and selectivity. On the other hand, technical limitation in recovery of pyruvic acid from fermentation broth is that, it could not be separated as other carboxylic acid in the form of salts by addition of alkali. Besides, pyruvic acid cannot be crystallized. Commercial separation by distillation is very expensive because pyruvic acid decomposes at higher temperature. It is also chemically reactive due to its peculiar molecular structure and has tendency to polymerize. Thus, at high concentration the various type of reaction leads to lower yield of the product, and hence, conventional methods are not favorable. Alternate separation technologies viable to both synthetic and biological routes are the current research areas. Latest techniques such as reactive extraction is new to the field of recovery of pyruvic acid. Recent development and future prospects in downstream processing of biochemically produced pyruvic acids has been discussed in this review article.

Keywords

Pyruvic acid Carboxylic acid Fermentation Reactive extraction Equilibrium 

List of Symbols

KD

Distribution coefficient

KE(1,1)

Equilibrium complexation constant for (1:1) acid: amine complex, m3 kmol−1

[\(\overline{HA}\)]

Concentration of pyruvic acid in organic phase, kmol m−3

[HA]

Concentration of pyruvic acid in aqueous phase, kmol m−3

[B]

Concentration of acid extracted by diluent, kmol m−3

[A]

Concentration of acid anion, kmol m−3

Z

Loading ratio

E

Degree of extraction,

\(\it {R}_{\it{HP}}\)

Rate of extraction

\(\it {D}_{\it{HP}}\)

Diffusivity coefficient

\([\overline{HA} ]\)2

Concentration of acid dimmer in organic phase, m3 kmol−1

TOA

Tri-n-octylamine

m

Order with respect to acid

n

Order with respect to amine

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Copyright information

© The Institution of Engineers (India) 2017

Authors and Affiliations

  • Dharm Pal
    • 1
  • Amit Keshav
    • 1
  • Bidyut Mazumdar
    • 1
  • Awanish Kumar
    • 2
  • Hasan Uslu
    • 3
  1. 1.Department of Chemical EngineeringNational Institute of Technology RaipurRaipurIndia
  2. 2.Department of BiotechnologyNational Institute of Technology RaipurRaipurIndia
  3. 3.Chemical Engineering Department, Engineering and Architecture FacultyBeykent UniversityIstanbulTurkey

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