The major portion of the time spent on this project for this quarter involved specifying and ordering the equipment required to construct the 13 inch inside diameter column. The superstructure constructed in was the laboratory and all major equipment ordered. In addition a series of dynamic gas disengagement experiments performed using the six were inch inside diameter column. The major objective of these eperiments was to determine whether the distribution has any effect on the bubble rise velocities. No major difference was found when the data for a porous plate and a sieve plate was compared. (A) (Microfiche
The primary objective of the study is to develop a computer model for a base line direct coal liquef...
The major technical objectives of this program are threefold: (1) to develop the design tools and a ...
Cold model studies of the liquid fluidized bed microreactor are essentially complete. This report do...
Report on the study of multiphase flow to understand further scaleup of coal liquefaction reactors, ...
Bubble size and specific interfacial area studies were made in a 33 cm diameter bubble column for th...
An understanding of three phase flow hydrodynamics and flow pattern are necessary for the design and...
Typescript (photocopy).Two and three-phase bubble columns have been used in various industrial proce...
In the Fischer-Tropsch approach to indirect liquefaction, slurry bubble-column reactors (SBCRs) are ...
The fluid dynamics occurring in HRI's H-coal process development unit coal liquefaction reactor duri...
The objective of this cooperative research effort between Washington University, Ohio State Universi...
This research was done as a support study for the SYNTHOIL process and other coal liquefaction proce...
The objective of this cooperative research effort between Washington University, Ohio State Universi...
The objective of this task is to utilize the continuous-flow bench-scale coal liquefaction reactor s...
This is the first quarterly report of a two year program of a study in support of the Pittsburgh Ene...
Cold flow ebullation tests to determine the ranges of operability of bead catalysts continued. Data ...
The primary objective of the study is to develop a computer model for a base line direct coal liquef...
The major technical objectives of this program are threefold: (1) to develop the design tools and a ...
Cold model studies of the liquid fluidized bed microreactor are essentially complete. This report do...
Report on the study of multiphase flow to understand further scaleup of coal liquefaction reactors, ...
Bubble size and specific interfacial area studies were made in a 33 cm diameter bubble column for th...
An understanding of three phase flow hydrodynamics and flow pattern are necessary for the design and...
Typescript (photocopy).Two and three-phase bubble columns have been used in various industrial proce...
In the Fischer-Tropsch approach to indirect liquefaction, slurry bubble-column reactors (SBCRs) are ...
The fluid dynamics occurring in HRI's H-coal process development unit coal liquefaction reactor duri...
The objective of this cooperative research effort between Washington University, Ohio State Universi...
This research was done as a support study for the SYNTHOIL process and other coal liquefaction proce...
The objective of this cooperative research effort between Washington University, Ohio State Universi...
The objective of this task is to utilize the continuous-flow bench-scale coal liquefaction reactor s...
This is the first quarterly report of a two year program of a study in support of the Pittsburgh Ene...
Cold flow ebullation tests to determine the ranges of operability of bead catalysts continued. Data ...
The primary objective of the study is to develop a computer model for a base line direct coal liquef...
The major technical objectives of this program are threefold: (1) to develop the design tools and a ...
Cold model studies of the liquid fluidized bed microreactor are essentially complete. This report do...