Reactive Extraction of Benzoic Acid and Pyridine-3-Carboxylic Acid Using Organophosphoric and Aminic Extractant Dissolved in Binary Diluent Mixtures

被引:26
作者
Datta, Dipaloy [1 ]
Kumar, Sushil [1 ]
Wasewar, Kailas L. [2 ]
机构
[1] BITS, Pilani 333031, Rajasthan, India
[2] Visvesvaraya Natl Inst Technol, Dept Chem Engn, Nagpur 440010, Maharashtra, India
关键词
PLUS LIQUID EQUILIBRIA; N-BUTYL PHOSPHATE; PROPIONIC-ACID; AQUEOUS-SOLUTIONS; CARBOXYLIC-ACIDS; ORGANIC-SOLVENTS; AMBERLITE LA-2; LEVULINIC ACID; TARTARIC ACID; SUCCINIC ACID;
D O I
10.1021/je200332s
中图分类号
O414.1 [热力学];
学科分类号
摘要
The reactive extraction of benzoic acid (BA) and pyridine-3-carboxylic acid (NA) using diluent mixtures, decane-1-ol (w = 0.36) + cyclohexane (w = 0.64) and 4-methylpentan-2-one (w = 0.63) + kerosene (w = 0.37) with and without reactive extractants such as tri-n-butylphosphate (TBP) and N,N-dioctyloctan-1-amine (TOA), is carried out. The effect of various parameters such as the type of acid, type of diluent mixture, type of extractant, and composition of aqueous and organic phases are studied to analyze the performance of reactive extraction. The maximum values of the distribution coefficient (K-D) are found to be 38.1 for BA and 7.4 for NA with TOA (0.229 mol . dm(-3)) in decane-1-ol (w = 0.36) + cyclohexane (w = 0.64). A mathematical model based on mass action law is proposed to estimate the values of partition coefficient (P) and dimerization constant (D) in physical extraction and equilibrium constants (K-E) and number of reacting extractant molecules per acid molecule in chemical extraction. The values of the loading ratio, Z (between 0.005 and 0.566), for the extraction of both acids using TBP and TOA in both diluent mixtures indicate a formation of a 1:1 acid/extractant complex in the organic phase. For the reactive extraction of both acids, the highest values of K-E are found with TOA in decane-1-ol (w = 0.36) + cyclohexane (w = 0.64).
引用
收藏
页码:3367 / 3375
页数:9
相关论文
共 39 条
[1]   Extraction of Glycolic Acid from Aqueous Solutions by Amberlite LA-2 in Different Diluent Solvents [J].
Asci, Yavuz Selim ;
Inci, Ismail .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2009, 54 (10) :2791-2794
[2]   AMINE EXTRACTION OF CITRIC-ACID - EFFECT OF DILUENT [J].
BIZEK, V ;
HORACEK, J ;
KOUSOVA, M .
CHEMICAL ENGINEERING SCIENCE, 1993, 48 (08) :1447-1457
[3]  
Brody T, 1999, NUTRITIONAL BIOCH
[4]  
CASCAVAL D, 2001, ROUM BIOTECHNOL LETT, V6, P207
[5]   Technology development in nicotinate production [J].
Chuck, R .
APPLIED CATALYSIS A-GENERAL, 2005, 280 (01) :75-82
[6]  
*CONC INT, 26 CONC INT
[7]   Nutritional properties and significance of vitamin glycosides [J].
Gregory, JF .
ANNUAL REVIEW OF NUTRITION, 1998, 18 :277-296
[8]   Water enhanced solubilities of succinic acid in reactive extraction using tertiary amines/alcohols systems [J].
Hong, YK ;
Han, DH ;
Hong, WH .
KOREAN JOURNAL OF CHEMICAL ENGINEERING, 2002, 19 (01) :83-86
[9]   Linear solvation energy relationship modeling and kinetic studies on reactive extraction of succinic acid by tridodecylamine dissolved in MIBK [J].
Inci, Ismail .
BIOTECHNOLOGY PROGRESS, 2007, 23 (05) :1171-1179
[10]  
John A, 1972, Lange's Handbook of Chemistry, V15