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STUDY ON THE GAS-LIQUID EQUILIBRIA IN THE TERNARY SYSTEM H2-CO2-methanol.

Author(s) : WEI K.

Summary

IN ORDER TO SATISFY THE REQUIREMENTS FOR THE DESIGN OF THE PURIFICATION PROCESS WITH LOW TEMPERATURE METHANOL WASHING, GAS-LIQUID EQUILIBRIA OF THE H2-CO2-methanol SYSTEM WERE MEASURED AND STUDIED STATISTICALLY AT TEMPERATURES OF -5, -15, -30, -45 AND -56 DEG C UNDER PRESSURES OF 2,350 AND 7,950 KILOPASCALS. THE MEASURED DATA WERE CORRELATED THERMODYNAMICALLY BY APPLYING THE SRK-WILSON MODEL, WHILE THE GAS-LIQUID EQUILIBRIA UNDER DIFFERENT TEMPERATURES AND PRESSURES WERE PREDICTED IN ACCORDANCE WITH THE MODEL PARAMETERS (WILSON PARAMETERS AND HENRY CONSTANTS UNDER ZERO PRESSURE) OF VARIOUS BINARY SYSTEMS.

Details

  • Original title: STUDY ON THE GAS-LIQUID EQUILIBRIA IN THE TERNARY SYSTEM H2-CO2-methanol.
  • Record ID : 1986-1781
  • Languages: English
  • Publication date: 1985/10/07
  • Source: Source: Proc. int. Conf. Prod. Purif. Coal Gas Sep. Air, Beijing
    vol. 1; 230-246; 4 fig.; 7 tabl.; 13 ref.
  • Document available for consultation in the library of the IIR headquarters only.

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