Pressure drop and liquid saturation accompanying two-phase concurrent flow have been studied in a variety of packings and with gas-liquid systems having a wide range of fluid properties. Two basic flow patterns were observed with nonfoaming systems. Correlations of pressuredrop and liquid-saturation data were obtained in terms of the single-phase friction losses for the liquid and the gas when each flows alone in the bed. Deviations from the correlation with foaming systems are discussed and illustrated with sample data.Peer Reviewedhttp://deepblue.lib.umich.edu/bitstream/2027.42/37316/1/690070213_ftp.pd
The concurrent flow of two phases through a pipe has been the object of increased study in recent ye...
Graduation date: 1971The pressure drop for two-phase liquid-liquid flow is theoretically\ud predicte...
Flows of two immiscible liquids are encountered in a diverse range of processes and equipments. In p...
No Abstract.Peer Reviewedhttp://deepblue.lib.umich.edu/bitstream/2027.42/37332/1/690100608_ftp.pd
New data on the two phase pressure drop for the concurrent upflow of air-liquid (Newtonian and non-N...
The present available experimental data on liquid holdup (735 data points) and pressure drop (863 da...
An experimental investigation was carried out to determine the effects of gas and liquid flow veloci...
This paper presents a review of theories for gas and liquid flows in packed beds as applied to chemi...
The simultaneous flow of gas and liquid through a fixed bed of particles occurs in many unit operati...
A large number of correlations can be found in the literature for the calculation of pressure drop c...
The analysis of the hydrodynamics results of two-phase downflow and upflow through fixed beds with p...
Gas-liquid two-phase flows are presented everywhere in industrial processes (i.e. gas-oil pipelines)...
International audienceMetal foams have a relatively large "fluid/solid" contact area (m2 m−3) as wel...
This work presents a brief study about mathematical modeling of two-phase flow (liquid + gas), appro...
Gas-Newtonian liquid two-phase flows (TPFs) are presented in several industrial processes (i.e. oil-...
The concurrent flow of two phases through a pipe has been the object of increased study in recent ye...
Graduation date: 1971The pressure drop for two-phase liquid-liquid flow is theoretically\ud predicte...
Flows of two immiscible liquids are encountered in a diverse range of processes and equipments. In p...
No Abstract.Peer Reviewedhttp://deepblue.lib.umich.edu/bitstream/2027.42/37332/1/690100608_ftp.pd
New data on the two phase pressure drop for the concurrent upflow of air-liquid (Newtonian and non-N...
The present available experimental data on liquid holdup (735 data points) and pressure drop (863 da...
An experimental investigation was carried out to determine the effects of gas and liquid flow veloci...
This paper presents a review of theories for gas and liquid flows in packed beds as applied to chemi...
The simultaneous flow of gas and liquid through a fixed bed of particles occurs in many unit operati...
A large number of correlations can be found in the literature for the calculation of pressure drop c...
The analysis of the hydrodynamics results of two-phase downflow and upflow through fixed beds with p...
Gas-liquid two-phase flows are presented everywhere in industrial processes (i.e. gas-oil pipelines)...
International audienceMetal foams have a relatively large "fluid/solid" contact area (m2 m−3) as wel...
This work presents a brief study about mathematical modeling of two-phase flow (liquid + gas), appro...
Gas-Newtonian liquid two-phase flows (TPFs) are presented in several industrial processes (i.e. oil-...
The concurrent flow of two phases through a pipe has been the object of increased study in recent ye...
Graduation date: 1971The pressure drop for two-phase liquid-liquid flow is theoretically\ud predicte...
Flows of two immiscible liquids are encountered in a diverse range of processes and equipments. In p...