共查询到19条相似文献,搜索用时 78 毫秒
1.
乙醇水溶液与二乙氧基甲烷的萃取分离 总被引:6,自引:0,他引:6
目前DEM与乙醇水溶液的分离均采用精密精馏法[1],由于DEM的沸点与乙醇水溶液的共沸点接近,很难得到98%以上的DEM,本文以二甘醇为萃取剂,以UNIQUAC方程为模型[6],采用微机模拟逆流萃取分离结果,并进行逆流萃取试验。1 逆流萃取模拟计算以UNIQUAC方程为模型,采用二甘醇为逆流图1 液液萃取工艺流程Fig.1 liquid liquidextractiontechnicalchart萃取剂模拟计算DEM与乙醇水溶液的分离结果,工艺流程如图1所示,塔顶为萃余相③,含高纯度的DEM,塔底为富含乙醇和水的萃取相②,萃取相送精馏塔分离,精馏塔底溶剂循环使用,塔顶可得到… 相似文献
2.
采用平衡法测定了丙烯腈+水、己二腈+水、丙腈+水三个二元体系在不同温度(303.15、313.15、323.15、333.15K)下的液-液相平衡数据;并采用NRTL(α=0.2,α=0.3)模型和UNIQUAC模型对液-液平衡数据进行了关联.结果显示,NRTL和UNIQUAC模型对三个二元体系在不同温度下的互溶度关联的目标函数值均小于1×10-17,实验值与计算值吻合较好,绝对偏差小于0.009,关联精度较高.该研究结果可为丙烯腈、丙腈和水三元平衡溶解度数据的模拟和预测提供可靠的基础数据,并对电解二聚法生产己二腈中电解液的分离提纯工艺具有一定的指导意义. 相似文献
3.
4.
5.
甲酸-乙酸-水-醋酸钠体系汽液平衡的盐效应 总被引:1,自引:1,他引:0
采用Otsuki-Williams式汽液平衡釜测定了甲酸-乙酸-水-醋酸钠体系在9.866×10~4Pa下汽液平衡数据。醋酸钠的加入量为2mol/(kg溶剂)。结果表明:醋酸钠对体系起物理化学作用,也起化学作用。它涉及到了两种盐对各组分的盐溶、盐析和盐效应的不规则现象。根据实验数据,绘制了汽液平衡相图、各组分挥发度等于1的曲线和甲酸-乙酸在体系中相对挥发度等于1的曲线,用以判别、分析盐效应的作用。 相似文献
6.
7.
本文采用Otsuki-Williams式汽液平衡釜测定了甲酸-乙酸-水体系及甲酸-乙酸-水-氯化钙体系在98658.28Pa下汽液平衡数据。氯化钙的加入量为0.5mol/(kg溶剂)。结合盐效应的作用情况,对相图进行了分析。研究结果表明:氯化钙的加入对体系起了物理化学作用,它与盐溶、盐析现象有关。 相似文献
8.
盐-混合溶剂体系气-液平衡研究具有重要的理论和实用意义。盐加到互溶双液系能改变组分间相对挥发度,提高蒸馏效率,分离恒沸物。达面方工作,Furter已作过详细综述。从盐-混合溶剂体系气-液平衡研究可以计算离子的溶剂化数,探索离子-溶剂和溶剂-溶剂之间的相互作用。因此,盐-混合溶剂体系气-液平衡的研究目前在国内外越来越受到人们的重视。本文研究盐饱和下的硫酸鲤-乙醇-水体系在高原大气压(530 Torr左右)下的汽-液平衡。改进的Rose釜测定体系的p-T-x-y数据。按照Jaques的假二元体系模型,使用Wilson,NRTL和修正的UNIQUAC方程关联实验数据。在计算过程中,使用一个能在计算机上顺利得到结果的计算方法。 相似文献
9.
10.
11.
Liquid—liquid equilibrium data were obtained for two ternary systems: acetonitrile— ethanol—cyclohexane at 40°C, and acetonitrile—2-propanol—cyclohexane at 50°C. Binary vapor—Liquid equilibrium data were measured for acetonitrile—2-propanol at 50°C. The binary parameters of the Zeta and effective Zeta equations were evaluated from equilibrium data for binary pairs. The parameters obtained were used to predict the ternary liquid—liquid equilibrium data for six systems involving the present systems and the ternary vapor—liquid equilibrium data for one completely miscible system and two partially miscible systems without adding any ternary parameter. A heterogeneous area calculated by the Zeta equation is in general too large and does not decrease appreciably with increasing values of the third parameter ζ of the Zeta equation. However, the effective Zeta equation works much better than the original Zeta equation in data reduction. 相似文献
12.
Vapor-liquid equilibrium (VLE) phase compositions were measured for the binary systems of benzyl alcohol with carbon dioxide, ethane, or nitrogen at temperatures from 333.15 K to 453.15 K and pressures up to 19 MPa. Henry's constants were calculated from the isothermal equilibrium data. The new VLE data were correlated by the Patel-Teja equations of state with three different types of mixing rules. In general, using the one-fluid, two-parameter van der Waals mixing rule yielded the best representation for the investigated systems. The validity of a generalized Soave model was also tested with the equilibrium data of carbon dioxide + benzyl alcohol. 相似文献
13.
In this paper, adsorption equilibrium and kinetics of three reactive dyes from their single-component aqueous solutions onto activated carbon were studied in a batch reactor. Effects of the initial concentration and adsorbent particle size on adsorption rate were investigated Adsorption equilibrium data were then correlated with several well-known equilibrium isotherm models. The kinetic data were fitted using the pseudo-first-order equation, the pseudo-second-order equation, and the intraparticle diffusion model. The respective characteristic rate constants were presented. A new adsorption rate model based on the pseudo-first-order equation has been proposed to describe the experimental data over the whole adsorption process. The results show that the modified pseudo-first-order kinetic model generates the best agreement with the experimental data for the three single-component adsorption systems. 相似文献
14.
15.
《Thermochimica Acta》1991,190(2):209-216
Solidus and liquidus equilibrium lines in binary phenol-bisphenol A system were determined with use of a DSC-1B calorimeter. Experimental equilibrium data were correlated by means of liquid phase activity coefficient equations (Redlich-Kister, Van Laar, NRTL) with one constraint based on the condition of solid-liquid equilibrium (Schroeder equation). 相似文献
16.
The liquid-liquid and vapor-liquid equilibrium data for the binary system of ethane + methanol were measured at ambient temperature over a wide range of pressures using a designed PVT apparatus. The experimental liquid-liquid and vapor-liquid equilibrium data were compared with the modeling results obtained using the Peng Robinson and Soave-Redlich-Kwong equations of state. 相似文献
17.
采用沸点仪测定了顺丁烯二酸酐和邻苯二甲酸二甲酯二元体系在4.00, 8.00和12.00 kPa下的等压气液平衡数据以及纯DMP组分饱和蒸气压数据, 将实验数据回归得到了纯DMP在417~525 K范围内的Antoine方程. 根据实验平衡温度、 压力和组成数据进一步回归得到NRTL方程参数, 推算出平衡气液相组成, 并利用UNIFAC方程对实验数据进行了预测, 其结果与沸点仪测定结果及NRTL拟合的结果基本相符. 相似文献
18.
The adsorption equilibrium and kinetics of single and binary component copper ions and phenol onto powdered activated carbon
(PAC), alginate beads and alginate-activated carbon beads (AAC) were studied. Adsorption equilibrium data for single component
copper ions and phenol onto the adsorbents could be represented by the Langmuir equation. Multicomponent equilibrium data
were correlated by the extended Langmuir and ideal adsorbed solution theory (IAST). The IAST gave the best fit to our data.
The amount of copper ions adsorbed onto the AAC beads in the binary component was greater than that of phenol. The internal
diffusion coefficients were determined by comparing the experimental concentration curves with those predicted from surface
diffusion and pore diffusion model. 相似文献
19.
Mónica B. Gramajo Jonatan H. Veliz Alicia M. Cases 《Russian Journal of Physical Chemistry A, Focus on Chemistry》2017,91(3):529-535
The phase equilibrium data for methanol + ethanol + isooctane systems were obtained at 303.15 K. Data for methanol + ethylbenzene + isooctane system were taken from literature. The effect of ethanol addition on the system equilibrium was investigated at the same temperature. The distribution curves for ternary and quaternary system was analyzed. The experimental results for ternary systems were correlated with UNIQUAC and NRTL equations. For the ternary systems studied here, the NRTL equation is more accurate than the UNIQUAC. The equilibrium data for the three ternary systems were used to determine interactions parameters for the UNIQUAC equation. For the quaternary system, the experimental data can be fitted more accurately to UNIQUAC equation than by the UNIFAC method. 相似文献