共查询到20条相似文献,搜索用时 781 毫秒
1.
2.
3.
二氧化碳在二甲基甲酰胺及其水溶液中溶解度的测定 总被引:1,自引:0,他引:1
采用低压容量法气液平衡测定仪测定了不同温度下CO_2在纯水、纯二甲基甲酰胺(DMF)及其混合溶剂中的溶解度,并计算了Henry常数和Ostwald系数。该装置适用于恒温(室温以上)常压下的气体在纯溶剂和混合溶剂中的气液平衡数据测定。 相似文献
4.
本文提出了拟二元模型和状态方程联用的方法,计算加压情况下CO_2-CuAlCl_4·(C_6H_5CH_3)_n体系的气-液平衡数据.选用拟一元模型得到的CuAlCl_4·(C_6H_5CH_3)_n的表观临界参数和表观偏心因子作为状态方程中含盐非水溶液的特征参数.由实测的气-液平衡数据拟合了状态方程中的二元可调参数.考察了两种混合规则对计算精度的影响,发现修正混合规则后的P-R方程比原始的P-R方程具有更高的关联精度.计算表明,能用拟二元模型和状态方程来描述该体系的气-液平衡关系. 相似文献
5.
6.
7.
基于气液平衡理论,建立了热力学状态方程二元交互作用参数估算模型。首先,结合气液平衡理论、状态方程以及相应的混合规则建立气液相平衡数学模型;然后以气相组成误差平方和与压力相对误差平方和之和作为目标函数,并使用计算机编程,利用单纯形法进行优化求解,实现了热力学状态方程二元交互作用参数估算模型的开发;最后,用该模型对5组二元气液平衡体系中的组分二元交互作用参数进行估算,并根据估算出的参数对各体系的气相组成进行预测,结果显示,预测值与实验值的平均相对偏差均小于1%,表明该模型计算结果准确,可应用于气液平衡计算中。 相似文献
8.
利用Newton-Raphson法拟合了气-液平衡计算中最困难的二元含水体系(水-乙醇体系)气液平衡组成的Wilson方程参数.结果表明,该方法简单,计算精度高,有理论和实际意义.在全部浓度范围内与实验值比较,结果说明,Wilson方程能很好地应用于该体系,计算结果令人满意. 相似文献
9.
10.
11.
The aim of this work is to apply cubic equations of state (EOS) to vapor-liquid equilibria calculations of gas- heavy hydrocarbon systems, which are asymmetric in molecular size and are usually found in natural gases. Investigation has been done to test the validity of the original PSRK and the cubic simplified perturbed hard-chain (CSPHC) models for global phase diagrams. The calculation results show that both equations overpredict vapor pressure in the near critical region. In the prediction of the solubilities of high molecular weight (MW) hydrocarbons in the natural gas, the PSRK model gives good agreement for the dew point pressure-vapor composition diagrams. Adjustment of the pure component parameters of the CSPHC EOS for heavy components to fit the vapor-liquid equilibrium (VLE) data has been proved to give significant promoting in prediction accuracy. However, further improvement of a van der Waals EOS, such as SRK, PT and DG models for the asymmetric systems by adjusting the three pure component properties, Tc, pc and ω, did not achieve satisfactory results for heavy components. 相似文献
12.
13.
AN NEW GROUP-CONTRIBUTION EQUATION OF STATE AND ITS APPLICATION TO PHASE EQUILIBRIUM CALCULATIONS(Ⅲ)Application to Liquid-Liquid Equilibria 下载免费PDF全文
Based on the group interaction parameters determined from binary VLE data,the VDW-GC EOS developedin Part I~[13] is extended to binary and multicomponent liquid-liquid equilibrium calculations.Equilibrium phasecompositions and the temperature effects on LLE can be predicted with reasonable accuracy. 相似文献
14.
15.
16.
17.
Alexander Breitholz Ki-Pung Yoo Jong Sung Lim Chul Soo Lee Jeong Won Kang 《Korean Journal of Chemical Engineering》2008,25(4):833-837
The nonrandom lattice equation of state with hydrogen bonding (NLF-HB EOS) was examined for the correlation of vapor-liquid
equilibria (VLE) for binary amine and hydrocarbon mixture at various temperatures. For these mixtures, the consideration of
hydrogen bondings in the lattice equation of state clearly improves the prediction for VLE. The amines were divided into four
groups due to the different strength of the hydrogen bonding. For all groups, different hydrogen bonding parameters were obtained
and evaluated. The effects of varying hydrogen bonding energies for NLF-HB EOS are discussed. For systems containing lower
amines, the NLF-HB EOS showed excellent agreement with the experimental data. For the correlation of systems containing tertiary
amine molecules, binary interaction parameter had to be involved instead of hydrogen bonding parameters. 相似文献
18.
All available simple cubic equations of state (EOS) are developed for specific representations. An effort has been made to take advantage of these existing equations for binary vapor-liquid equilibrium (VLE) as well as density calculations by assigning different EOS to different components of the mixture under consideration. A four-parameter cubic equation was used for combining the equations in the calculation. The effect of substance-dependent Ωac on vapor-liquid equilibrium calculations was further investigated, using two sets of mixing rules. A criterion for selection of equations for VLE calculation by means of the proposed approach was suggested. The improvement in the prediction of liquid volumes for binary mixtures based on the fitting of pure component liquid volumes was very satisfactory. 相似文献
19.
Alexander Breitholz Ki-Pung Yoo Jong Sung Lim Chul Soo Lee Jeong Won Kang 《Journal of Industrial and Engineering Chemistry》2008,14(2):219-223
The nonrandom lattice equation of state with hydrogen bonding (NLF-HB EOS) was examined for the correlation of liquid–liquid equilibria (LLE) for binary alcohol and hydrocarbon mixture in a wide pressure range. For hydrocarbon + alcohol mixtures the consideration of a hydrogen-bonding term in the lattice equation of state clearly improves the prediction for vapor–liquid equilibrium (VLE) as shown in previous works, but the prediction of LLE is still in question. In this paper, LLE data for alcohols (methanol and ethanol) + hydrocarbons (n-hexane to n-hexadecane) were correlated by NLF-HB EOS and results were compared with a cubic equation of state (Peng–Robinson EOS with the T–K Wilson based GE model). Both equations of state showed similar degree of accuracies but with different number of adjustable parameters. The Peng–Robinson EOS based approach requires six temperature dependent coefficients for accurate calculation whereas NLF-HB EOS requires only two temperature dependent coefficients. The effects of varying hydrogen-bonding energies for NLF-HB EOS are discussed. 相似文献
20.
《Chemical engineering science》2003,58(3-6):867-875
A comprehensive one-dimensional heterogeneous reactor model is developed to simulate the performance of fixed-bed Fischer–Tropsch reactors for hydrocarbon production. The detailed mechanistic kinetics is combined into the reactor model along with considering the fact that the catalyst pores are filled with liquid wax under realistic conditions. The equilibrium between the gases in the bulk and the wax in the catalyst pores is correlated by using a modified SRK equation of state (MSRK EOS). The model is solved by using Gear method to integrate the reactor model with the embedded pellet model discretized by orthogonal collocation on finite elements. The validity of the reactor model is tested against the measured data from different-scale demonstration processes. Satisfactory agreements between model predictions and experiment results are obtained. Detailed numerical simulations are performed to investigate the effect of major process parameters on the reaction behavior of fixed-bed FTS systems with recycle operation. 相似文献