Chromatographic reactors: Esterification of glycerol with acetic acid using acidic polymeric resins

被引:59
作者
Gelosa, D
Ramaioli, M
Valente, G
Morbidelli, M [1 ]
机构
[1] Swiss Fed Inst Technol Zurich, HCI, ETH Hoenggerberg, Inst Chem & Bioengn, CH-8093 Zurich, Switzerland
[2] Politecn Milan, Dipartimento Mat Chim & Ingn Chim Giulio Natta, I-20131 Milan, Italy
关键词
D O I
10.1021/ie030292n
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Reactive chromatography is an attractive method for chemical synthesis because chemical reactions and product separation occur simultaneously in the same unit. In this work, the synthesis of triacetine, starting from glycerol and acetic acid, using reactive chromatography on acidic polymeric resins is investigated. The study proceeds first to the characterization of the adsorption equilibria of the involved multicomponent mixtures and then to the study of the kinetics of the relevant reactions using a batch reactor. Next, the separation-reaction process is investigated using a fixed-bed chromatographic column. The obtained data are compared with the predictions of a mathematical model, whose kinetic and equilibrium parameters were estimated from the batch experiments mentioned above. It is shown that, although this synthesis requires three steps in series, the chromatographic reactor can produce high-purity (i.e., food-grade) triacetine with high conversions. It is found that the presence of water in the resin at the end of the regeneration step has a strongly detrimental effect on the final triacetine purity.
引用
收藏
页码:6536 / 6544
页数:9
相关论文
共 15 条
[1]   LONGITUDINAL DISPERSION OF LIQUID FLOWING THROUGH FIXED AND FLUIDIZED BEDS [J].
CHUNG, SF ;
WEN, CY .
AICHE JOURNAL, 1968, 14 (06) :857-&
[2]  
Flory P J., PRINCIPLES POLYM CHE
[3]  
FOERSTER D, 1979, Patent No. 134867
[4]   A NEW PROCESS COMBINING ADSORPTION AND ENZYME REACTION FOR PRODUCING HIGHER-FRUCTOSE SYRUP [J].
HASHIMOTO, K ;
ADACHI, S ;
NOUJIMA, H ;
UEDA, Y .
BIOTECHNOLOGY AND BIOENGINEERING, 1983, 25 (10) :2371-2393
[5]   Increased esterification conversion by application of the simulated moving-bed reactor [J].
Kawase, M ;
Suzuki, TB ;
Inoue, K ;
Yoshimoto, K ;
Hashimoto, K .
CHEMICAL ENGINEERING SCIENCE, 1996, 51 (11) :2971-2976
[6]   Catalytic synthesis of methanol, higher alcohols and ethers [J].
Klier, K ;
Beretta, A ;
Sun, Q ;
Feeley, OC ;
Herman, RG .
CATALYSIS TODAY, 1997, 36 (01) :3-14
[7]   Optimization of the simulated countercurrent moving-bed chromatographic reactor for the oxidative coupling of methane [J].
Kruglov, AV ;
Bjorklund, MC ;
Carr, RW .
CHEMICAL ENGINEERING SCIENCE, 1996, 51 (11) :2945-2950
[8]   Continuous reactive chromatography [J].
Lode, F ;
Houmard, M ;
Migliorini, C ;
Mazzotti, M ;
Morbidelli, M .
CHEMICAL ENGINEERING SCIENCE, 2001, 56 (02) :269-291
[9]  
LODE F, 2001, THESIS ETH ZURICH ZU
[10]   A continuous chromatographic reactor: SMBR [J].
Mazzotti, M ;
Kruglov, A ;
Neri, B ;
Gelosa, D ;
Morbidelli, M .
CHEMICAL ENGINEERING SCIENCE, 1996, 51 (10) :1827-1836