Vapor-liquid-liquid phase equilibrium in four-component benzene-heptane-N-methylpyrrolidone-sulfolane system
И. В. Иванов, В. А. Лотхов, A. Yu. Tikhonov, Н. Н. Кулов
Abstract
И. В. Иванов, В. А. Лотхов, A. Yu. Tikhonov, Н. Н. Кулов
Abstract
The liquid-vapor phase equilibrium in four-component benzene-heptane-N-methylpyrrolidone-sulfolane system has been experimentally studied, including in the areas of lamination of the liquid phase. The modeling of liquid-liquid-vapor phase equilibrium in the studied system has been performed using a calculation program compiled based on the nonrandom two-liquid (NRTL) equation. A comparative assessment of the effectiveness of N-methylpyrrolidone, sulfolane, and their mixture as separating agents in the of extractive distillation of benzene-heptane binary mixture has been performed.
OpenAlex reports 4 citations for this work. Citation counts describe recorded attention and do not establish research quality.
A contribution statement is not available in the OpenAlex record.
Method details are not available in the OpenAlex metadata.
Findings are not separately available in the OpenAlex metadata.
Limitations are not available in the OpenAlex metadata.
Application details are not available in the OpenAlex metadata.
The liquid-vapor phase equilibrium in four-component benzene-heptane-N-methylpyrrolidone-sulfolane system has been experimentally studied, including in the areas of lamination of the liquid phase. The modeling of liquid-liquid-vapor phase equilibrium in the studied system has been performed using a calculation program compiled based on the nonrandom two-liquid (NRTL) equation. A comparative assessment of the effectiveness of N-methylpyrrolidone, sulfolane, and their mixture as separating agents in the of extractive distillation of benzene-heptane binary mixture has been performed.
Key concepts: Sulfolane, Non-random two-liquid model, Heptane, Benzene, Component (thermodynamics), Phase (matter), Chemistry, Distillation