The effect of composition on the boiling rates of liquefied natural gas for confined spills on water

Abstract The rate of boiling of liquefied natural gas (LNG) spilled onto a water surface was experimentally measured in a confined area calorimeter. Increasing the concentration of ethane and propane resulted in higher boiling rates. In all cases, the vaporization rate was found to be very time dependent with concomitant variations in the LNG composition and temperature as well as in the character of the water where ice formed and increased in thickness. A qualitative theory is proposed to explain the effect of composition on the boiling rates and a quantitative model developed to predict boiling rates for LNG spills. This model is based on a numerical solution to the Stefan problem and is coupled to a vapor-liquid equilibrium model which tracks changes in LNG composition and temperature. Good agreement is obtained between predicted and experimental boiling rates with the use of a single adjustable parameter—which is itself correlated with initial LNG composition.

[1]  S. Stralen,et al.  Local temperature fluctuations in saturated pool boiling of pure liquids and binary mixtures , 1969 .

[2]  J. Hovestreijdt The influence of the surface tension difference on the boiling of mixtures , 1963 .

[3]  A. Price,et al.  Low temperature vapor-liquid equilibrium in light hydrocarbon mixtures: Methane-ethane-propane system , 1959 .

[4]  M. Novakovic,et al.  Boiling from a mercury surface , 1964 .

[5]  J. Prausnitz,et al.  Vapor-Liquid Equilibria at High Pressures. Vapor-Phase Fugacity Coefficients in Nonpolar and Quantum-Gas Mixtures , 1967 .

[6]  P. S. Chappelear,et al.  Low-temperature vapor-liquid equilibriums of nitrogen-methane system , 1974 .

[7]  Fred Landis,et al.  Numerical and Machine Solutions of Transient Heat-Conduction Problems Involving Melting or Freezing: Part I—Method of Analysis and Sample Solutions , 1959 .

[8]  C. P. Colver,et al.  Pool Boiling of Methane between Atmospheric Pressure and the Critical Pressure , 1967 .

[9]  E. L. Park,et al.  Nucleate and Film Boiling Heat Transfer to Nitrogen and Methane at Elevated Pressures and Large Temperature Differences , 1966 .

[10]  Robert C. Reid,et al.  Transient boiling of liquefied cryogens on a water surface: I. Nitrogen, Methane and Ethane , 1975 .

[11]  G. Soave Equilibrium constants from a modified Redlich-Kwong equation of state , 1972 .

[12]  R. Reid,et al.  Boiling of liquid nitrogen and methane on water. The effect of initial water temperature , 1977 .

[13]  D. Zudkevitch,et al.  Correlation and prediction of vapor‐liquid equilibria with the redlich‐kwong equation of state , 1970 .

[14]  B. Otterman Analysis of large LNG spills on water part 1: Liquid spread and evaporation , 1975 .

[15]  Jefferson W. Tester,et al.  Thermodynamics and its applications , 1974 .

[16]  Warren M. Rohsenow,et al.  Heat Mass and Momentum Transfer , 1961 .

[17]  O. Redlich,et al.  On the thermodynamics of solutions; an equation of state; fugacities of gaseous solutions. , 1949, Chemical reviews.

[18]  E. Eckert,et al.  Analysis of heat and mass transfer , 1971 .

[19]  G. Opschoor,et al.  INVESTIGATIONS INTO THE SPREADING AND EVAPORATION OF LNG SPILLED ON WATER , 1977 .

[20]  L. Bewilogua,et al.  Heat transfer in cryogenic liquids under pressure , 1975 .