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Vapor‐liquid equilibria for hydrogen–light‐hydrocarbon systems at low temperatures

A. L. Benham, Donald L. Katz

Open publisher page 67 citations

Abstract

Abstract Experimental equilibrium vapor and liquid compositions are reported for the hydrogen‐methane system at −150°, −200°, and −250°F. and at pressures of 500 to 4,000 lb./sq. in. The ternary system hydrogen‐methane‐propane was studied at 0°, −100°, and −200°F. at 500 and 1,000 lb./sq. in. Phase compositions were determined for a limited number of similar conditions for the hydrogen‐methane‐propylene and hydrogen‐methane‐ethylene‐ethane‐propylene‐propane systems.

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Abstract Experimental equilibrium vapor and liquid compositions are reported for the hydrogen‐methane system at −150°, −200°, and −250°F. and at pressures of 500 to 4,000 lb./sq. in. The ternary system hydrogen‐methane‐propane was studied at 0°, −100°, and −200°F. at 500 and 1,000 lb./sq. in. Phase compositions were determined for a limited number of similar conditions for the hydrogen‐methane‐propylene and hydrogen‐methane‐ethylene‐ethane‐propylene‐propane systems.

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Available abstract

Abstract Experimental equilibrium vapor and liquid compositions are reported for the hydrogen‐methane system at −150°, −200°, and −250°F. and at pressures of 500 to 4,000 lb./sq. in. The ternary system hydrogen‐methane‐propane was studied at 0°, −100°, and −200°F. at 500 and 1,000 lb./sq. in. Phase compositions were determined for a limited number of similar conditions for the hydrogen‐methane‐propylene and hydrogen‐methane‐ethylene‐ethane‐propylene‐propane systems.

Key concepts: Propane, Methane, Hydrogen, Hydrocarbon, Chemistry, Ternary operation, Ternary numeral system, Alkane

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