Vapor-Liquid Equilibria and Chemical Equilibria in the System (Formaldehyde plus Water plus Isoprenol)

被引:17
作者
Dyga, Maximilian [1 ]
Keller, Andreas [2 ]
Hasse, Hans [1 ]
机构
[1] Tech Univ Kaiserslautern TUK, Lab Engn Thermodynam LTD, D-67663 Kaiserslautern, Germany
[2] BASF SE, Proc Dev, D-67056 Ludwigshafen, Germany
关键词
QUANTITATIVE NMR-SPECTROSCOPY; UNIFAC GROUP-CONTRIBUTION; REACTION-KINETICS; AQUEOUS-SOLUTIONS; DEUTERIUM-OXIDE; MIXTURES; METHANOL; C-13; TEMPERATURES; REVISION;
D O I
10.1021/acs.iecr.1c00168
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Isoprenol (3-methyl-3-buten-1-ol) is an important intermediate in the chemical industry and is used, for example, in the production of various scent and flavor chemicals. Isoprenol is produced from aqueous formaldehyde and isobutene and is separated by distillation from mixtures containing formaldehyde, water, and isobutene in the process. As formaldehyde forms oligomers with both water and isoprenol, these mixtures are complex reacting systems, which are not easy to separate. Hence, for understanding and modeling the process, information on the vapor-liquid equilibria and the chemical equilibria in the system (formaldehyde + water + isoprenol) is essential. However, only very limited data on this system are available in the literature. Therefore, in the present work, vapor-liquid equilibria were measured in the following systems: system (water + isoprenol) at 20 and 90 kPa, system (formaldehyde + isoprenol) at 373 and 393 K, and system (formaldehyde + water + isoprenol) at 373 K. Furthermore, the chemical equilibria of the oligomerization reactions of formaldehyde and isoprenol were studied with C-13-NMR spectroscopy at temperatures ranging from 283 to 353 K. The experimental data were used to extend a physico-chemical model of the system (formaldehyde + water) from the literature to include isoprenol.
引用
收藏
页码:4471 / 4483
页数:13
相关论文
共 51 条
[11]   Experimental study and model of reaction kinetics of heterogeneously catalyzed methylal synthesis [J].
Drunsel, Jan-Oliver ;
Renner, Mario ;
Hasse, Hans .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2012, 90 (05) :696-703
[12]   Equilibrium Speciation in Moderately Concentrated Formaldehyde-Methanol Water Solutions Investigated Using 13C and 1H Nuclear Magnetic Resonance Spectroscopy [J].
Gaca, Katarzyna Z. ;
Parkinson, John A. ;
Lue, Leo ;
Sefcik, Jan .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2014, 53 (22) :9262-9271
[13]   NMR SPECTROSCOPIC AND DENSIMETRIC STUDY OF REACTION-KINETICS OF FORMALDEHYDE POLYMER FORMATION IN WATER, DEUTERIUM-OXIDE, AND METHANOL [J].
HAHNENSTEIN, I ;
ALBERT, M ;
HASSE, H ;
KREITER, CG ;
MAURER, G .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1995, 34 (02) :440-450
[14]   H-1-NMR AND C-13-NMR SPECTROSCOPIC STUDY OF CHEMICAL-EQUILIBRIA IN SOLUTIONS OF FORMALDEHYDE IN WATER, DEUTERIUM-OXIDE, AND METHANOL [J].
HAHNENSTEIN, I ;
HASSE, H ;
KREITER, CG ;
MAURER, G .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1994, 33 (04) :1022-1029
[15]   VAPOR-LIQUID-EQUILIBRIA BY UNIFAC GROUP CONTRIBUTION .5. REVISION AND EXTENSION [J].
HANSEN, HK ;
RASMUSSEN, P ;
FREDENSLUND, A ;
SCHILLER, M ;
GMEHLING, J .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1991, 30 (10) :2352-2355
[16]   VAPOR-LIQUID-EQUILIBRIUM OF FORMALDEHYDE-CONTAINING MIXTURES AT TEMPERATURES BELOW 320-K [J].
HASSE, H ;
MAURER, G .
FLUID PHASE EQUILIBRIA, 1991, 64 :185-199
[17]   REVISED VAPOR-LIQUID-EQUILIBRIUM MODEL FOR MULTICOMPONENT FORMALDEHYDE MIXTURES [J].
HASSE, H ;
HAHNENSTEIN, I ;
MAURER, G .
AICHE JOURNAL, 1990, 36 (12) :1807-1814
[18]  
Hasse H., 2003, REACTIVE DISTILLATIO, P65
[19]   Environmentally benign manufacturing of fine and intermediate chemicals [J].
Hoelderich, WF .
CATALYSIS TODAY, 2000, 62 (01) :115-130
[20]   Optimization of the IPP-bypass mevalonate pathway and fed-batch fermentation for the production of isoprenol in Escherichia coli [J].
Kang, Aram ;
Mendez-Perez, Daniel ;
Goh, Ee-Been ;
Baidoo, Edward E. K. ;
Benites, Veronica T. ;
Beller, Harry R. ;
Keasling, Jay D. ;
Adams, Paul D. ;
Mukhopadhyay, Aindrila ;
Lee, Taek Soon .
METABOLIC ENGINEERING, 2019, 56 :85-96