Equilibrium study on the reactive extraction of heterocyclic monocarboxylic acids from the aqueous solution using Alamine 300/diluent composite solvent: Optimization and modeling of the solvent effect

Senol A., Yalcinkaya O.

ASIA-PACIFIC JOURNAL OF CHEMICAL ENGINEERING, cilt.17, sa.1, 2022 (SCI-Expanded) identifier identifier

  • Yayın Türü: Makale / Tam Makale
  • Cilt numarası: 17 Sayı: 1
  • Basım Tarihi: 2022
  • Doi Numarası: 10.1002/apj.2723
  • Dergi Adı: ASIA-PACIFIC JOURNAL OF CHEMICAL ENGINEERING
  • Derginin Tarandığı İndeksler: Science Citation Index Expanded (SCI-EXPANDED), Scopus, Academic Search Premier, Applied Science & Technology Source, Chemical Abstracts Core, Compendex, INSPEC
  • Anahtar Kelimeler: heterocyclic carboxylic acid, mathematical modeling, numerical simulation, optimization, reactive extraction, ISOTHERMAL TITRATION CALORIMETRY, SOLVATION ENERGY RELATIONSHIPS, LIQUID-LIQUID-EXTRACTION, CARBOXYLIC-ACIDS, AMINE EXTRACTANTS, PROPIONIC-ACID, BUTYRIC-ACID, LACTIC-ACID, WATER, SEPARATION
  • İstanbul Üniversitesi Adresli: Evet

Özet

Experiments were conducted to optimize the extraction equilibrium of reactive systems (water + heterocyclic carboxylic acid + Alamine 300/diluent) at T = 298.2 K and P = 101.3 kPa. The uptake capacity of the commercial composite solvent Alamine 300/diluent approximates the order: 2-furoic acid >= alpha-oxo-2-furanacetic acid > tetrahydro-2-furoic acid, and n-heptane < 1,2-dichloroethane < 1-heptanol <= 2-heptanone. Four differentiable models featuring the effects of separation ratio R and synergistic enhancement SE factors are stringently tested to identify global optimization ranges by derivative variation method as follows: 0.2 < R < 0.8 and 4 < SE < 7 for 1-heptanol and 2-heptanone, 1.2 < R < 3.5 and 4 < SE < 6.5 for 1,2-dichloroethane, 2 < R < 80 and 4 < SE < 80 for n-heptane, and Alamine 300 concentration 0.12-0.18 mol dm(-3). Consecutively, the optimum mass transfer stages of a countercurrent extraction are calculated by Kremser-Souders-Brown equation. The equilibrium properties are estimated precisely according to linear solvation energy relation with substantial improvement linear solvation energy relation with substantial improvement (LSER-si), solvation probability relation solvation probability relation (SPR) and Chemodel-modified yielding mean relative errors of 7.0%, 0.08% and 20.4%, respectively.