African Journal of
Biotechnology

  • Abbreviation: Afr. J. Biotechnol.
  • Language: English
  • ISSN: 1684-5315
  • DOI: 10.5897/AJB
  • Start Year: 2002
  • Published Articles: 12487

Full Length Research Paper

Optimal sulphuric acid production using Acidithiobacillus caldus (DSM 8584): Bioprocess design for application in ion-exchange

  Basitere, M.1, Ntwampe, S. K. O.2* and Sheldon, M. S.1  
  1Department of Chemical Engineering, Faculty of Engineering, Cape Peninsula University of Technology, P. O. Box 652, Cape Town, 8000, South Africa. 2Department of Agriculture and Food Science, Faculty of Applied Sciences, Cape Peninsula University of Technology, P. O. Box 652, Cape Town, 8000, South Africa.
Email: [email protected]

  •  Accepted: 14 September 2012
  •  Published: 16 October 2012

Abstract

 

An optimised bioprocess was designed for the optimal production of sulphuric acid for application in an isotope recovery ion-exchange process. Firstly, the production of sulphuric acid (H2SO4) was optimised in aerated batch bioreactors usingAcidithiobacillus caldus (DSM 8584) using elemental sulphur, achieving H2SO4concentration of >0.4 to ~0.5 M (0.45 M average) with the following bioprocess parameters: product yield of 3.06 (Yp/s), oxygen uptake rate of 1.35 g/L.day (OUR), 52% sulphur conversion at a rate of 0.83 g/L.day (dS°/dt), achieving a sulphuric acid production rate of 2.76 g/L.day (dP/dt), while the oxidation of elemental sulphur per dissolved oxygen consumed was 0.67 g S°/g O2. Secondly, after 80% (v/v) moisture loss from the recovered biological H2SO4 titres, the acid solution was used for the recovery of nuclear grade lithium 7 (7Li+) from a degraded resin, achieving >80% recovery rate within two bed volumes (60 ml) at an averaged desorption rate  of 0.1829 min-1 and eluent rate of 6.65 ml.min-1 in comparison to the ~60% 7Li+recovery rate using a commercial grade mineral H2SO4 using similar operational ion-exchange reactor parameters. The designed bioprocess proved to be an effective and environmentally friendly bioprocess for the recovery of valuable metals adsorbed onto ion-exchange resin.

 

Key words: Acidithiobacillus caldus, sulphuric acid, ion-exchange, desorption, lithium 7 isotope

 

Abbreviation

Nomenclature:Desorption rate constant (min-1); L, ion-exchange column length (m); OUR, oxygen uptake rate (g/L.day); dP/dt, sulphuric acid production rate (g/L.day), Se, amount of lithium in the resin at exit port (mg/L); S, concentration of lithium in the resin (mg/L), So, 7Licapacity on a 30 ml degraded lithiated resin (mg/L);dS°/dt, sulphur utilisation rate (g/L.day); uz, axial eluent flow rate at the entry (L/min);t, time (min); Yp/s, product yield based on substrate consumption; Yx/s, biomass yield based on substrate consumption; Yp/x, product yield based on biomass generation; e,porosity; α, Inverse of the product yield based on biomass generated.