The drop size is of fundamental importance in the design of liquid-liquid extraction columns, the drop size was measured as a function of the geometry, operating conditions, and physical properties of a liquid-liquid system with no mass transfer in a five-stage modified Scheibel extraction column. An improved correlation of the mean drop size in the Scheibel extraction column is presented. The correlation was divided into three sections in terms of the Reynolds number. It could be applied in a wide range and could be further used for the study of mass transfer performance of the modified Scheibel extraction column.
The polymerization of tetrahydrofuran (THF) was carried out in CH2Cl2 by using phosphotungstic heteropolyacid as initiator and epichlorohydrin as promoter. This cationic ring-opening polymerization process was monitored by in situ mid-infrared spectroscopy system (ReactIR) to further study the thermodynamics and kinetics of THF polymerization. It was observed that the sharp infrared peak of COC stretching vibrations will shift from about 1068 to 1109 cm−1 in THF ring-opening step. The changes in absorbance intensity of the two characteristic peaks were used for determining instantaneous concentration of linear polymer and ring monomer. The experimental results demonstrated that the kinetics of THF polymerization proved to be typically first-order. Thermodynamic parameters were determined from the temperature dependence of the monomer equilibrium concentration [M]e over the range from −5 to 25°C. The values of kapp were obtained via the plots of ln{([M]0−[M]e)/([M]t−[M]e)} vs reaction time, for polymerization under specific conditions. The apparent activation energy (Ea) and frequency (A) were determined from the Arrhenius plot of kapp vs. T−1. Besides, the in situ kinetic investigation revealed that more chain-transfer occurred at higher temperatures, leading to a reduction in propagation species concentration and a deviation from first-order propagation at the later stage of polymerization. © 2014 Wiley Periodicals, Inc. J. Appl. Polym. Sci. 2014, 131, 40503.
Acetone and tetrahydrofuran are commonly used as solvents in the chemical industry. The separation of acetone–tetrahydrofuran mixtures is often faced in the pharmaceutical and special chemical industries. As acetone and tetrahydrofuran can form a minimum azeotrope, they cannot be separated by conventional distillation. But acetone and tetrahydrofuran are important organic raw materials and solvents, so the mixture should be separated for reuse.
The process of continuous extractive distillation was used to separate the mixture of acetone (62% mass fraction) and tetrahydrofuran (38% mass fraction) using butyl ether as solvent. The characteristics of the continuous extractive distillation were simulated via ASPEN and experiments also showed the feasibility of separating the acetone–tetrahydrofuran mixture. Effects of the reflux mass ratio (R), mixture feed stage (FS), the solvent feed stage (SFS) on the extractive distillation column and the volume ratio of solvent to mixture (S/F) on the distillate mass fraction of acetone and bottom product mass fraction of acetone were investigated. The results of the extractive distillation simulation were verified by experiment data. With the following operation conditions for the extractive distillation column: number of theoretical plates 53; mixture feed at 24th plate; solvent feed at 7th plate, solvent to mixture ratio 3 and reflux mass ratio 3, the mass fraction of acetone in the distillate can reach 99%.
The process of continuous extractive distillation using butyl ether as solvent can separate the acetone–tetrahydrofuran mixture. The solvent to mixture ratio and reflux mass ratio are important factors that affect the mass fraction of the product. © 2013 Society of Chemical Industry
Experiments were designed to ascertain the main factors for the Sauter mean drop size (d32) of the dispersed phase in a three-stage modified Scheibel extraction column with no mass transfer. A precise correlation applied to the liquid-liquid systems with low interfacial surface tension was proposed for calculating d32. The maximum relative error for all data was 16.0 % and the mean relative error ±4.6 %.
Amino polysiloxanes (APSs) with different amino values and amino types were synthesized and applied to cotton fabrics. Softening and smoothening properties of the fabrics treated with APSs were investigated and evaluated by measuring wrinkle recovery angles and friction coefficients, and the morphological features of the APSs adsorbed onto cellulose substrate films were characterized by atomic force microscope (AFM). The results indicate that the amino values and amino types of the APSs have a significant impact on the softening and smoothening properties of the fabrics. APSs with relatively high amino values exhibit superior smoothening property, while APSs with moderate amino values exhibit excellent softening property. Compared to the traditional softener N-β-aminoethyl-γ-aminopropyl polydimethylsiloxane (APS-1), the new amino type softeners γ-piperazinylpropyl polydimethylsiloxane (APS-2) and N-γ'-dimethylaminopropyl-γ-aminopropyl polydimethylsiloxane (APS-3) gave better fabric performance, whereas aminopropyl polydimethylsiloxane (APS-4) and N-cyclohexyl-γ-aminopropyl polydimethylsiloxane (APS-5) gave unsatisfactory fabric performance. © 2010 Wiley Periodicals, Inc. J Appl Polym Sci, 2011