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Author:Tully, P.C.

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8 matching references were found.

Estes, J.M.; Tully, P.C., A modified redlich-kwong equation for helium from 30 to 1,473k., AIChE J., 1967, 13, 192. [all data]

Barieau, R.E.; Tully, P.C., , U.S. Bur. Mines Inform. Circ. No. 8319 1967 1967, 1967. [all data]

Tully, P.C.; Stroud, L., Vap.-liq. equil. data for he-N2-CH4 mixt. from 80-144K & press to 1200psia, Bull. - U. S., Bur. Mines, Rept. Invest. 8181, 1976. [all data]

Rhodes, H.L.; Stroud, L.; Tully, P.C., , Rep. Invest. - U. S., Bur. Mines 7598, 1972. [all data]

Tully, P.C.; DeVaney, W.E.; Rhodes, H.L., Phase equilibria of the helium + nitrogen system from 122 to 126 k, Adv. Cryog. Eng., 1971, 16, 88-95. [all data]

Rhodes, H.L.; DeVaney, W.E.; Tully, P.C., Phase equilibria data for helium + methane in the vapor-liquid and fluid- fluid region, J. Chem. Eng. Data, 1971, 16, 19-23. [all data]

DeVaney, W.E.; Rhodes, H.L.; Tully, P.C., Phase equilibrium data for helium + methane system, J. Chem. Eng. Data, 1971, 16, 158. [all data]

Tully, P.C.; Edmister, W.C., Isobaric integral heats of vaporization for methane-ethylene system, AIChE J., 1967, 13, 155-9. [all data]