Author: P.R. Tandon
Publisher:
ISBN:
Category :
Languages : en
Pages :
Book Description
Vapor-liquid Equilibrium in the Two Binary Mixtures Ethanol-benzene and Methanol-toluene at 25 Degees Celcius
Author: P.R. Tandon
Publisher:
ISBN:
Category :
Languages : en
Pages :
Book Description
Publisher:
ISBN:
Category :
Languages : en
Pages :
Book Description
Vapor-liquid Equilibrium in the Binary Mixture, and the Prediction of Azeotropism
Author: Leon Robert Kiley
Publisher:
ISBN:
Category :
Languages : en
Pages : 534
Book Description
Publisher:
ISBN:
Category :
Languages : en
Pages : 534
Book Description
Vapor-liquid Equilibrium in the Three Binary Mixtures of Hexane, Benzene, and Ethanol at 25° C
Author: Vinson Charles Smith
Publisher:
ISBN:
Category :
Languages : en
Pages : 240
Book Description
Publisher:
ISBN:
Category :
Languages : en
Pages : 240
Book Description
The Vapor-liquid Equilibrium of the System Methanol-ethanol-acetone and Its Component Binaries
Author: Hassanein Hamed Amer
Publisher:
ISBN:
Category :
Languages : en
Pages : 312
Book Description
Publisher:
ISBN:
Category :
Languages : en
Pages : 312
Book Description
Vapor-liquid Equilibrium Data for the Binary Systems Ethyl Alcohol-benzene and Ethyl Alcohol-toluene
Author: Joseph C. Landwehr
Publisher:
ISBN:
Category :
Languages : en
Pages : 48
Book Description
Publisher:
ISBN:
Category :
Languages : en
Pages : 48
Book Description
Vapor-liquid Equilibrium at 75 °C for Binary and Ternary Systems Containing Benzene, N-heptane and N-propyl Alcohol
Author: Sheau Jean Fu
Publisher:
ISBN:
Category :
Languages : en
Pages : 0
Book Description
Binary and ternary vapor-liquid equilibrium data were determined at 75°C for the mixture of benzene, n-heptane and n-propyl alcohol using a modified Gillespie type of still. The equilibrium data for the three binary and the ternary systems are considered to be thermodynamically consistent as shown from the consistency test. Correlating the data with the Redlich-Kister equations for the binary and ternary systems shows that these equations would represent the data accurately over the entire range of compositions. The experimental results indicate that two binary systems, namely, n-heptane-n-propyl alcohol and n-propyl alcohol-benzene form an azeotrope at 75°C. Nevertheless no ternary azeotrope is found from the experiment.
Publisher:
ISBN:
Category :
Languages : en
Pages : 0
Book Description
Binary and ternary vapor-liquid equilibrium data were determined at 75°C for the mixture of benzene, n-heptane and n-propyl alcohol using a modified Gillespie type of still. The equilibrium data for the three binary and the ternary systems are considered to be thermodynamically consistent as shown from the consistency test. Correlating the data with the Redlich-Kister equations for the binary and ternary systems shows that these equations would represent the data accurately over the entire range of compositions. The experimental results indicate that two binary systems, namely, n-heptane-n-propyl alcohol and n-propyl alcohol-benzene form an azeotrope at 75°C. Nevertheless no ternary azeotrope is found from the experiment.
Vapor-liquid Equilibria in Binary Aromatic-olefin Systems
Author: Juan Humberto Vera
Publisher:
ISBN:
Category :
Languages : en
Pages : 88
Book Description
Publisher:
ISBN:
Category :
Languages : en
Pages : 88
Book Description
Vapor-liquid Equilibrium
Author: James C. K. Ho
Publisher:
ISBN:
Category :
Languages : en
Pages : 0
Book Description
This thesis comprises of two parts. The first part is the determination of vapor-liquid equilibrium data at atmospheric pressure and 55°C for the ternary system n-hexane-ethyl alcohol-benzene and for the three possible binary systems n-hexane-ethyl alcohol, n-hexane-benzene and ethyl alcohol-benzene which constituted the ternary system. A modified Gillespie equilibrium still is employed to conduct the investigation. The equilibrium data for the three binary systems and the ternary system appear to be consistent as shown from the thermodynamic consistency tests. The experimental results indicate that two binary systems, namely, n-hexane-ethyl alcohol and ethyl alcohol-benzene form azeotrope at 760 nm. Hg. and 55°C. The ternary system deviates considerably from ideal liquid phase behavior. However, no ternary azeotrope is found from the experiment. The second part presents a method for predicting binary vapor-liquid equilibrium data at various conditions if the equilibrium data for the system concerned are available over the complete concentration range at any one isothermal or isobaric condition. The proposed method is limited to nonazeotropic solutions.
Publisher:
ISBN:
Category :
Languages : en
Pages : 0
Book Description
This thesis comprises of two parts. The first part is the determination of vapor-liquid equilibrium data at atmospheric pressure and 55°C for the ternary system n-hexane-ethyl alcohol-benzene and for the three possible binary systems n-hexane-ethyl alcohol, n-hexane-benzene and ethyl alcohol-benzene which constituted the ternary system. A modified Gillespie equilibrium still is employed to conduct the investigation. The equilibrium data for the three binary systems and the ternary system appear to be consistent as shown from the thermodynamic consistency tests. The experimental results indicate that two binary systems, namely, n-hexane-ethyl alcohol and ethyl alcohol-benzene form azeotrope at 760 nm. Hg. and 55°C. The ternary system deviates considerably from ideal liquid phase behavior. However, no ternary azeotrope is found from the experiment. The second part presents a method for predicting binary vapor-liquid equilibrium data at various conditions if the equilibrium data for the system concerned are available over the complete concentration range at any one isothermal or isobaric condition. The proposed method is limited to nonazeotropic solutions.
Vapor-liquid Equilibrium
Author: Sheau Jean Fu
Publisher:
ISBN:
Category : University of Ottawa theses
Languages : en
Pages : 262
Book Description
Publisher:
ISBN:
Category : University of Ottawa theses
Languages : en
Pages : 262
Book Description
The Engineering Index Annual
Author:
Publisher:
ISBN:
Category : Engineering
Languages : en
Pages : 2282
Book Description
Since its creation in 1884, Engineering Index has covered virtually every major engineering innovation from around the world. It serves as the historical record of virtually every major engineering innovation of the 20th century. Recent content is a vital resource for current awareness, new production information, technological forecasting and competitive intelligence. The world?s most comprehensive interdisciplinary engineering database, Engineering Index contains over 10.7 million records. Each year, over 500,000 new abstracts are added from over 5,000 scholarly journals, trade magazines, and conference proceedings. Coverage spans over 175 engineering disciplines from over 80 countries. Updated weekly.
Publisher:
ISBN:
Category : Engineering
Languages : en
Pages : 2282
Book Description
Since its creation in 1884, Engineering Index has covered virtually every major engineering innovation from around the world. It serves as the historical record of virtually every major engineering innovation of the 20th century. Recent content is a vital resource for current awareness, new production information, technological forecasting and competitive intelligence. The world?s most comprehensive interdisciplinary engineering database, Engineering Index contains over 10.7 million records. Each year, over 500,000 new abstracts are added from over 5,000 scholarly journals, trade magazines, and conference proceedings. Coverage spans over 175 engineering disciplines from over 80 countries. Updated weekly.