πŸ“‹ Case Study

Food-Grade Citric Acid Purification via Liquid-Liquid Extraction

High viscosity broth, emulsion formation with tertiary amines, difficult phase separation

πŸ—οΈ Project Overview

Fermentation-based citric acid plant in Brazil

🎯 Challenge

High viscosity broth, emulsion formation with tertiary amines, difficult phase separation

πŸ”§ Design Approach

Tri-n-octylamine (TOA)/isodecanol system with centrifugal contactors and back-extraction using 20% Hβ‚‚SOβ‚„

πŸ“ Design Diagram

Food-Grade Citric Acid PurificationLiquid-Liquid Extraction with TOA/IsodecanolStage 1Stage 2Stage 5Centrifugal Contactors (N = 5)Feed Broth
(Citric Acid + Glucose)Raffinate
(Glucose-rich, low citric)
Extract Phase
TOA/Isodecanol + Citric
Back-extractionChallenge: Emulsion FormationΞ² = 1250 β€’ N = 5 β€’ 20% Hβ‚‚SOβ‚„

AI-generated project design illustration

πŸ“ Key Calculations

Selectivity (Ξ²)

(D_citric / D_glucose)
Result: Ξ² = 1250
Confirms minimal sugar co-extraction

Theoretical Stages (N)

log[(X_F/X_R)(1βˆ’X_R)/(1βˆ’X_F)] / log Ξ±
Result: N = 4.7 β†’ 5 stages
Guides contactor cascade design

πŸ“Š Results

Citric acid purity >99.8%; glucose impurities <10 ppm; 40% shorter processing time vs. calcium salt precipitation

πŸ’‘ Lessons Learned

  • β€’Centrifugal contactors eliminate emulsion holdup
  • β€’Back-extraction pH must be <1.2 to prevent TOA protonation loss

βœ… Key Takeaways

  • 1Centrifugal contactors eliminate emulsion holdup
  • 2Back-extraction pH must be <1.2 to prevent TOA protonation loss