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Isothermal pressurization

Ozone can be analyzed by titrimetry, direct and colorimetric spectrometry, amperometry, oxidation—reduction potential (ORP), chemiluminescence, calorimetry, thermal conductivity, and isothermal pressure change on decomposition. The last three methods ate not frequently employed. Proper measurement of ozone in water requites an awareness of its reactivity, instabiUty, volatility, and the potential effect of interfering substances. To eliminate interferences, ozone sometimes is sparged out of solution by using an inert gas for analysis in the gas phase or on reabsorption in a clean solution. Historically, the most common analytical procedure has been the iodometric method in which gaseous ozone is absorbed by aqueous KI. [Pg.503]

When a Mollier chart is available for the gas involved the first method, which is illustrated by Figure 12-12A is the most convenient. On the abscissa of Figure 12-12A four enthalpy differences are illustrated. (Hg — Hj) is the enthalpy difference for the isentropic path. (Hg — Hi°) is the ideal gas state enthalpy difference for the terminal temperatures of the isentropic path. The other AH values are the isothermal pressure corrections to the enthalpy at the terminal temperatures. A generalized chart for evaluating these pressure corrections was presented previously. [Pg.390]

Edmister (1948) published a generalised plot showing the isothermal pressure correction for real gases as a function of the reduced pressure and temperature. His chart, converted... [Pg.70]

Gholami Y., Azin R., et al. Prediction of carbon dioxide dissolution in bulk water under isothermal pressure decay at different boundary conditions. 2015 Journal of Molecular Liquids 202 23-33. [Pg.174]

Kubair, V. and Kuloor, N.R., Non-isothermal pressure drop data for liquid flow in heated coils. Indian Journal of Technology, 3, pp. 5-7 (1965). [Pg.95]

Fig. 1.22 Schematic isothermal pressure-composition hysteresis loop... Fig. 1.22 Schematic isothermal pressure-composition hysteresis loop...
Systematic density measurements at a wide range of femperafure and pressure [28,31,63,68,69] were helpful to obfain isofhermal compressibility, which is calculated using the isothermal pressure derivative of density according to Equation 1.2... [Pg.12]

Fig, 2-22. isothermal pressure-composition diagrams of mixtures of methane and ethane. (Bloomer, et al., Institute of Gas Technology, Research Bulletin 22, 1953. Reproduced courtesy of Institute of Gas Technology, Chicago.)... [Pg.70]

BOYLE S LAW. This law, attributed to Robert Boyle (1662) but also known as Mariottc s law, expresses the isothermal pressure-volume relation for abody of ideal gas. That is, if the gas is kept at constant temperature, the pressure and volume are in inverse proportion, or have a constant product. The law is only approximately true, even for such gases as hydrogen and helium nevertheless it is very useful. Graphically, it is represented by an equilateral hyperbola (see Fig. I). If the temperature is not constant, the behavior of die ideal gas must be expressed by die Boyle-Charles law. [Pg.255]

A general equation for the isothermal pressure flow of an incompressible Newtonian fluid in a die (without moving parts like, e.g., wire coating dies), can be written as... [Pg.451]

The pressure drop calculated assuming the relationship Nu = 1.75 (Gz)1 3 for estimating h is smaller than the calculated AP, assuming isothermal flow. For the conditions depicted in Fig. 12.11, at T = 103 s 1 the isothermal pressure drop is about 30 % higher than the measured value. This fact must be taken into account in the design of extrusion dies, so that gross die overdesign can be avoided, as well as in capillary viscometry. [Pg.689]

Before closing this chapter, we feel that it is useful to list in tabular form some isothermal pressure-flow relationships commonly used in die flow simulations. Tables 12.1 and 12.2 deal with flow relationships for the parallel-plate and circular tube channels using Newtonian (N), Power Law (P), and Ellis (E) model fluids. Table 12.3 covers concentric annular channels using Newtonian and Power Law model fluids. Table 12.4 contains volumetric flow rate-pressure drop (die characteristic) relationships only, which are arrived at by numerical solutions, for Newtonian fluid flow in eccentric annular, elliptical, equilateral, isosceles triangular, semicircular, and circular sector and conical channels. In addition, Q versus AP relationships for rectangular and square channels for Newtonian model fluids are given. Finally, Fig. 12.51 presents shape factors for Newtonian fluids flowing in various common shape channels. The shape factor Mq is based on parallel-plate pressure flow, namely,... [Pg.735]

FEM versus Analytical Solution of Flow in a Tapered Gap Consider isothermal pressure flow of a constant viscosity Newtonian fluid, between infinite plates, 10 cm long with a linearly decreasing gap size of 1.5 cm at the entrance and 1 cm at the exit. The distance between the entrance and the exit is 10 cm. The pressure at the inlet and outlet are 2 atmospheres and zero, respectively, (a) Calculate the pressure distribution invoking the lubrication approximation, (b) Calculate the pressure profile using the FEM formulation with six equal-sized elements, and compare the results to (a). [Pg.886]

A multiple-property technique was employed in developing the Lee-Erbar-Edmister equations. In this method, both measured values of the isothermal pressure correction to the enthalpy and the P-V-T data are used. [Pg.342]

Dunn, R. O. 2006b. Oxidation Kinetics of Biodiesel by Non-Isothermal Pressurized-Differential Scanning Calorimetry. In Proc., 34th Annual NATAS Conference. Bowling Green KY North American Thermal Analysis Society. [Pg.49]

FIG URE 1.4 Isothermal pressure correction to the molar heat capacity of gases. Perry and Chilton—Chemical Engineers Handbook, McGraw-Hill, 1973.)... [Pg.21]

Figure 9 Phase diagram of the Fe-N system isotherm pressures are in bar the region around the f-Fe2N phase has been modified. (Ref. 53. Reproduced by permission of Royal Institute of Technology, Stockholm)... Figure 9 Phase diagram of the Fe-N system isotherm pressures are in bar the region around the f-Fe2N phase has been modified. (Ref. 53. Reproduced by permission of Royal Institute of Technology, Stockholm)...
The isothermal pressure-composition prism in Figure 3 represents calculated equilibrium phase compositions at 55 C. [Pg.86]

Changes in pressure at constant temperature. For a species undergoing an isothermal pressure change, AP,... [Pg.407]

Edmister (1948) published a generalized plot showing the isothermal pressure correction for real gases as a function of the reduced pressure and temperature. His chart, converted to SI units, is shown as Eigure 3.2. Edmister s chart was based on hydrocarbons but can be used for other materials to give an indication of the likely error if the ideal gas specific heat values are used without corrections. [Pg.92]

Camera and Biasutti )21) developed an interesting method of isothermal pressure metering for the determination of chemical stability of aromatic nitro compounds, as descibed in Chapter IV. It showed that a temperature as low as 200 C could be dangerous if ONT pure, or with TNT, is kept for less than 24 hours (e.g. 18 hours) at this temperature. [Pg.444]


See other pages where Isothermal pressurization is mentioned: [Pg.234]    [Pg.2000]    [Pg.248]    [Pg.15]    [Pg.207]    [Pg.234]    [Pg.464]    [Pg.77]    [Pg.349]    [Pg.40]    [Pg.60]    [Pg.180]    [Pg.349]    [Pg.1758]    [Pg.86]    [Pg.358]    [Pg.366]    [Pg.347]    [Pg.1519]    [Pg.594]    [Pg.423]    [Pg.3]    [Pg.2170]    [Pg.74]   
See also in sourсe #XX -- [ Pg.182 ]




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