This paper is published in Volume-7, Issue-3, 2021
Area
Chemical Engineering
Author
Arvind Kapte, Dr. Gopal Zamre
Org/Univ
College of Engineering and Technology, Akola, Maharashtra, India
Keywords
Distillation, 1Propanol, Binary System, Thermodynamic Modeling
Citations
IEEE
Arvind Kapte, Dr. Gopal Zamre. Interpretation and co-relation of vapor-liquid equilibrium data in distillation by using salt effect for the propanol-water system, International Journal of Advance Research, Ideas and Innovations in Technology, www.IJARIIT.com.
APA
Arvind Kapte, Dr. Gopal Zamre (2021). Interpretation and co-relation of vapor-liquid equilibrium data in distillation by using salt effect for the propanol-water system. International Journal of Advance Research, Ideas and Innovations in Technology, 7(3) www.IJARIIT.com.
MLA
Arvind Kapte, Dr. Gopal Zamre. "Interpretation and co-relation of vapor-liquid equilibrium data in distillation by using salt effect for the propanol-water system." International Journal of Advance Research, Ideas and Innovations in Technology 7.3 (2021). www.IJARIIT.com.
Arvind Kapte, Dr. Gopal Zamre. Interpretation and co-relation of vapor-liquid equilibrium data in distillation by using salt effect for the propanol-water system, International Journal of Advance Research, Ideas and Innovations in Technology, www.IJARIIT.com.
APA
Arvind Kapte, Dr. Gopal Zamre (2021). Interpretation and co-relation of vapor-liquid equilibrium data in distillation by using salt effect for the propanol-water system. International Journal of Advance Research, Ideas and Innovations in Technology, 7(3) www.IJARIIT.com.
MLA
Arvind Kapte, Dr. Gopal Zamre. "Interpretation and co-relation of vapor-liquid equilibrium data in distillation by using salt effect for the propanol-water system." International Journal of Advance Research, Ideas and Innovations in Technology 7.3 (2021). www.IJARIIT.com.
Abstract
Vapor-liquid equilibrium (VLE), is a condition where a liquid and its vapor (gas phase) are in equilibrium with each other or more precisely a state where the rate of evaporation equals the rate of condensation on a molecular level such that there is no overall vapor-liquid interconversion. In this paper, we study the azeotrope breaking of binary 1propanol-water system with a salt-added method to recover the purity of water by using batch distillation and to investigate the concentration of salt added to break the azeotrope of the lprapanol-water system in the batch distillation process. The objective of this paper was to study physical properties with different measurement methods and to supply thermodynamic data for several chemical systems.
