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Compression calculation

Thermodynamic diagrams are known for light hydrocarbons, refrigerants, natural gas mixtures, air, and a few other common substances. Unless a substance or mixture has very many applications, it is not worthwhile to construct a thermodynamic diagram for compression calculations but to use other equivalent methods. [Pg.157]

The final temperature is read off directly from a thermodynamic diagram when that method is used for the compression calculation, as in Example 7.7. A temperature calculation is made in Example 7.10. Such determinations also are made by the general method for nonideal gases and mixtures as in Example 7.8 and for ideal gases in Example 7.4. [Pg.161]

Table 6.2 Summary of compression calculations for an add gas mixture -first design. Table 6.2 Summary of compression calculations for an add gas mixture -first design.
A sample of polypropylene tested at 30°C and 10 s shows a yield stress of 35 MPa in uniaxial tension and 38 MPa under uniaxial compression. Calculate the hydrostatic pressure that must be superimposed in order to reach yield stress of 80 MPa. Assume that the material obeys the pressure-dependent von Mises criterion. [Pg.643]

Figure 1.6. Isothermal Compressibility Calculated by the RISM Theory the sohd line, theoretical results the asterisk, experimental data. Figure 1.6. Isothermal Compressibility Calculated by the RISM Theory the sohd line, theoretical results the asterisk, experimental data.
Table 2.2 Gyroid structural compression calculated from GISAXS fitting... Table 2.2 Gyroid structural compression calculated from GISAXS fitting...
The absorption spectra of terrylene in the gas phase are not known. Using the compressibility calculated from the pentacene data, the solvent shift of terrylene in p-terphenyl is estimated to be Avs = 2345 + 411 cm and therefore its vacuum absorption wavelength should be 509 11 nm. The larger solvent and pressure shifts found for terrylene as compared to pentacene seem reasonable, since terrylene is bigger and therefore expected to exhibit larger polarizabilities in its ground and excited state. [Pg.99]

At typical inlet conditions, k is about 1.32-1.35. This is slightly lower than the specific heat ratio of air. Charts showing the energy required to compress air provide a modest safety factor if used to estimate the compression energy required by chlorine. The quantity k — l)/k, which appears often in compression calculations, will be about 0.25. If we designate the compression ratio as r, Eq. (39) becomes... [Pg.1060]

We have shown that sorption of a few weight percent of carbon dioxide in polymer blends and block copolymers can depress the location of lower critical solution transitions by hundreds of degrees. These solvent-induced transitions can occur at CO2 vapor densities of less than 0.05 g/cc. The sensitivity of the transitions to minor dilation with CO2 and the results of the compressibility calculations presented here suggest the effect is entropic rather than enthalpic in nature. [Pg.287]

Figure 12. Isothermal compressibility against pressure for different temperatures from NPT MD simulations using the SW potential. All the isotherms shown in this figure are for temperatures above the liquid-liquid critical temperature. With the decrease in temperature, the maximum value of the compressibility along an isotherm increases, suggesting an approach to the critical point. The lines represent the compressibility values calculated from the equation of state by numerical differentiation. The symbols represent the compressibility calculated from volume fluctuations. Figure 12. Isothermal compressibility against pressure for different temperatures from NPT MD simulations using the SW potential. All the isotherms shown in this figure are for temperatures above the liquid-liquid critical temperature. With the decrease in temperature, the maximum value of the compressibility along an isotherm increases, suggesting an approach to the critical point. The lines represent the compressibility values calculated from the equation of state by numerical differentiation. The symbols represent the compressibility calculated from volume fluctuations.
Of further interest is the question whether matrix correlations are of the same importance for the calculation of the matrix compressibility as they are for the potential parameter and the number density. A detailed analysis, however, reveals that for our model systems as well as for H2Pc-doped polymers PE and PS the corrections to the simple equations due to matrix correlations are smaller than the experimental error. This explains the good agreement between optically determined compressibilities, calculated conventionally without consideration of matrix correlations, and mechanically determined bulk values for polymeric systems. [Pg.191]

The sealant in the joint must accommodate these movements considering the actual joint width when the sealant is inserted and cured or set. The necessary joint widths to accommodate joint expansion and contraction are easily calculated from the elongation capabilities of the sealant in tensile and compression. These values are standard information in the technical data sheets of sealants, often using the term dynamic movement capability and expressed as a percentage. Where only one value is given, it should be used for both tension and compression. Calculation of these minimum widths is accomplished using the following relationships ... [Pg.739]


See other pages where Compression calculation is mentioned: [Pg.157]    [Pg.118]    [Pg.111]    [Pg.69]    [Pg.390]    [Pg.430]    [Pg.23]    [Pg.49]    [Pg.69]    [Pg.118]    [Pg.28]    [Pg.76]    [Pg.275]    [Pg.111]    [Pg.333]    [Pg.486]    [Pg.490]    [Pg.736]   


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