Now showing items 1-6 of 6
Vapor-liquid equilibria in the system hydrogen-nitrogen-carbon monoxide
Vapor-liquid equilibrium compositions for the system hydrogen-nitrogen-carbon monoxide were determined at -310°F, and -280°F and -240°F from 300 psig to the critical. PVT data for hydrogen were fitted to the ...
Low temperature vapor-liquid equilibrium in light hydrocarbon mixtures: Methane-ethane-propane system
Experimental equilibrium data have been determined for 175 mixtures of methane, ethane, and propane. The investigation included temperatures from 50°F to -200°F and pressures up to the critical. A vapor recycle ...
Heat transfer during condensation inside a horizontal tube
Heat transfer data were taken for methanol and Freon-12 condensing inside a horizontal tube over considerable ranges of pressure, temperature driving force, liquid loading, and vapor velocity. A single mechanism for heat ...
A study of bubble dynamics and mass transfer in stagnant liquid systems
The purpose of this investigation was to study the effect of physical properties and system dimensions on the mass transfer between a gas bubble and the parent liquid for the case of stagnant liquid. The study was divided ...
Heat transfer coefficients for Freon-12 condensing within a horizontal tube
The purpose of this investigation was to continue the study begun by Crosser (5) of heat transfer coefficients for condensing vapors in a horizontal tube. Condensing heat transfer coefficients for Freon-12 were measured ...
Analysis of low temperature chromatographic separation of methane-propane mixtures with N-decane on celite
An outline of the history of chromatography is presented, reviewing briefly the existing theories. The theory of Jame sand Martin for gas liquid partition chromatography and the extension to their theory by Litlewood and ...