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Methanol critical point parameters

The basic advantages of using binary mixtures with the critical CP instead of the GL critical point can be found in the history of critical phenomena, namely establishing the basic universal parameters appeared to be much simpler for binary mixtures with CP than for GL systems. Firstly, CP investigations can be carried out under atmospheric pressure. Secondly, one can select a binary mixture with CP close to room temperature. " Finally, it is possible to select a mixture which emphasizes the desired specific feature, for instance (a) methanol - cyclohexane mixture can simulate weightless conditions since densities of both components are almost equal (b) there are almost no critical opalescence for isooctane - cyclohexane mixture since their refractive indices are almost the same (c) one can considerably change the concentration of the dipole component of the mixture. The latter feature can strongly influence both dielectric properties and solvency. [Pg.170]

High-temperature alcohol supercritical extraction techniques (ASCE) bring the wet gel to the supercritical state of the solvent (usually methanol or ethanol) in an autoclave or other pressure vessel. This involves high pressures (above 8 MPa) and temperatures (above 260° C). A number of studies have been performed to examine the effects of solvent fill volume, pre-pressure, and other processing parameters (see for example Phalippou et al. [23], Danilyuk et al. [24], Pajonk et al. [25]). The low-temperature extraction techniques (CSCE) are based on supercritical extraction of CO2, which has a lower critical-point temperature than the alcohol mixture that remains in the sol-gel pores after polymerization. The CSCE methods... [Pg.55]

The SRK EOS parameters of the pure components can be calculated in terms of their critical pressure and temperature [29]. The binary interaction parameter q can be found from phase equilibria data for the binary mixture. Because, such data are not available, the critical loci data for the systems CO2 (1) + methanol (2) and CO2 (1) + acetone (2) [30] were used to calculate qn (Reference [30]), provided the binary critical data in the form X2 — Pa — Ta, where X2 is the molar fraction of component 2 in the critical mixture. Per the critical pressure and Per the critical temperature of the mixture. The mixture parameter a (a ) in the SRK EOS was calculated for every X2 — P — Per point using the expression [29]... [Pg.124]

The Dortmund Data Bank is still growing and currently contains about 4.78 million data points. Models with a high number of free variables fitted to a limited number of experimental data points, such as a kinetic model for methanol steam reforming with 13 parameters determined by 43 experiments [45], must be evaluated critically. [Pg.639]


See other pages where Methanol critical point parameters is mentioned: [Pg.123]    [Pg.568]    [Pg.130]    [Pg.415]    [Pg.145]    [Pg.8]    [Pg.268]    [Pg.415]    [Pg.320]    [Pg.128]    [Pg.92]    [Pg.8]    [Pg.659]    [Pg.54]    [Pg.162]    [Pg.1079]    [Pg.40]   
See also in sourсe #XX -- [ Pg.624 ]




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