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Total temperature

The fugacity coefficient is a function of temperature, total pressure, and composition of the vapor phase it can be calculated from volumetric data for the vapor mixture. For a mixture containing m components, such data are often expressed in the form of an equation of state explicit in the pressure... [Pg.26]

Figure 7-15 shows the time evolution of the temperature, total energy, and potential energy for a 300 ps simulation of the tetracycline repressor dimer in its induced (i.e., hgand-bound) form. Starting from the X-ray structure of the monomer in a complex with one molecule of tetracycline and a magnesium ion (protein database... [Pg.369]

The solubihty of a gas in water is affected by temperature, total pressure, the presence of other dissolved materials, and the molecular nature of the gas. Oxygen solubihty is inversely proportional to the water temperature and, at a given temperature, directly proportional to the partial pressure of the oxygen in contact with the water. Under equihbrium conditions, Henry s law apphes... [Pg.339]

Convergence was achieved in 3 iterations. Converged values of temperatures, total flows, and component flow rates are tabulated in Table 13-14. Computed reboiler duty is 1,295,000 W (4,421,000 Btu/h). Computed temperature, total vapor flow, and component flow profiles, shown in Fig. 13-54, are not of the shapes that might be expected. Vapor and liquid flow rates for nC4 change dramatically from stage to stage. [Pg.1287]

Surface water information, including drainage patterns (overland flow, topography, channel flow pattern, tributary relationships, soil erosion, and sediment transport and deposition), surface water bodies (flow, stream widths and depths, channel elevations, flooding tendencies, and physical dimensions of surface water impoundments structures surface water/ groundwater relationships), and surface water quality (pH, temperature, total suspended solid, salinity, and specific contaminant concentrations)... [Pg.601]

Pellet density Void volume gram Specific surface area Enthalpy change for reaction Temperature Total pressure... [Pg.463]

Fig. 25 RON of the product mixture as a function of MCH conversion, calculated by the method of ref. 14. Standard errors for this method are 1R0N. For the product distribution obtained on the three Pt/HY + Ir/Si02 catalyst bed configurations illustrated in Fig. 24. Conversion was varied by changing temperature. Total pressure = 2 MPa H2/feed molar ratio = 40. Adapted from ref. 100. Fig. 25 RON of the product mixture as a function of MCH conversion, calculated by the method of ref. 14. Standard errors for this method are 1R0N. For the product distribution obtained on the three Pt/HY + Ir/Si02 catalyst bed configurations illustrated in Fig. 24. Conversion was varied by changing temperature. Total pressure = 2 MPa H2/feed molar ratio = 40. Adapted from ref. 100.
Costantino et al. [75] prepared M(II)/Al-carbonate LDHs (M(II) = Mg, Zn and Ni) by this method. The effects of varying the temperature, total metal cation concentration, molar fraction A1/A1+M(II) and molar fraction... [Pg.100]

Factors affecting aw are the types of components in food, the physicochemical state of components, porous structure, temperature, total pressure, and surface tension (Rahman, 1995 Rizvi, 1995 Bell and Labuza, 2000) however, the effect of surface tension is very... [Pg.59]

Time at temperature Total time above 315°C ZnCl2/MF coal feed ratio H2 partial pressure Coal particle size... [Pg.164]

Substrate Carbon source Boron source Excitation source Microwave power Substrate temperature Total pressure C/H ratio Deposition time... [Pg.1058]

Luminescence spectrophotometry consists of fluorescence, phosphorescence and low-temperature total luminescence. Fluorescence is generally measured at room temperature. Phosphorescence is generally observed at liquid nitrogen temperature (77K) with the aid of a chopper to interrupt the exciting radiation. Total luminescence is the combined fluorescence and phosphorescence obtained at low temperature (77K). Luminescence spectrophotometry is generally much more sensitive and specific than absorption spectrophotometry. [Pg.398]

The residence time is calculated based on the fluidizing gas velocity, assuming that the "free volume" (i.e. the volume of the expanded bed minus the volume of the sand) is fully utilized. At the temperature, total reactor gas flow rates, and sand bed volumes used, the residence time was about 0.5-1.0 sec. A typical operation began by washing the sand in 10% HNO3 and distilled water to remove impurities, such as iron, which may act as catalysts, and then calcined at 850° C for at least 12 hours to remove any sulfides and carbonates. The coal feed is then begun and pyrolysis products then exit the pyrolyser to a set of two cold traps fitted with cellulosic thimble filters maintained at 0° C. The outlet gas temperature after the first trap is 30-34° C. Much of the light char formed is entrained in the exit gas and carried into these traps, with most of it in the first trap. [Pg.294]

Figure 5.5 Absolute silanol concentration on aerosil as a Junction of temperature. total free OH, + geminal OH, free OH. Figure 5.5 Absolute silanol concentration on aerosil as a Junction of temperature. total free OH, + geminal OH, free OH.
The various methods for the online monitoring of coal composition include the TG technique, which automatically performs a multistep analytical sequence by sequentially drying, burning, and weighing the residue. Figure 3.12 shows the analysis results from an automated TG system. The elapsed time of the proximate analysis program and cooling of the tube back to load temperature totals 30 minutes. [Pg.342]

Figure 2a. Change in initial rate of hydrogenation with cyclohexene partial pressure at constant temperatures. Total pressure is 115 psia. Key -,2 parameter... Figure 2a. Change in initial rate of hydrogenation with cyclohexene partial pressure at constant temperatures. Total pressure is 115 psia. Key -,2 parameter...
Calculate the total liquid rates from the constant composition method, using the most recent set of compositions and temperatures. Total vapor rates are found from the material balance for each stage. [Pg.156]

The Gold stein-Stanfield (45) method. This method chooses the stage temperatures, total vapor rates, total liquid rates, and liquid compo-... [Pg.169]

Figure 1. The derivative mode of the ESR absorption (9.11 GHz) of C16BFk as a function of temperature. Total scan range is 4 mT (= 40 G) and the figures have been offset horizontally for viewing ease. Although the behavior seen here is indicative of a conduction carrier resonance, the reader should consult the text for a full... Figure 1. The derivative mode of the ESR absorption (9.11 GHz) of C16BFk as a function of temperature. Total scan range is 4 mT (= 40 G) and the figures have been offset horizontally for viewing ease. Although the behavior seen here is indicative of a conduction carrier resonance, the reader should consult the text for a full...
Figure 14. Heptane-insoluble conversion vs. temperature. Total undistilled sample (M), Ni-Mo ( ), Ni-W. Bottoms from distillation (D),... Figure 14. Heptane-insoluble conversion vs. temperature. Total undistilled sample (M), Ni-Mo ( ), Ni-W. Bottoms from distillation (D),...
Temperature, Total time, °C. hours Atom ratios Phases from x-ray diffraction0... [Pg.362]

Operating head (200 F) + oven temperature (600 F) = delivery temperature (800 F) and delivery temperature - total head = mixed temperature. [Pg.69]

In continuous treatment Nowcorr 800 is added to the drilling fluid or to the acid blends. The concentration depends on downhole conditions temperature, total pressure and... [Pg.551]

The conversion can be determined by a measurement of the flow rates, Eqn. 7.24. This usually involves a chromatographic analysis of the reactor outlet stream. A complete kinetic analysis requires the determination of versus W/FA0 curves over the range of temperatures, total pressures and inlet compositions jfo, of interest. The production rates obtained after differentiation are then regressed by a postulated rate equation on featuring parameters, such as preexponential factors, Aq, and activation energies, Ea ... [Pg.290]

Total time of heating electron-gun filament was 1000 hr at 1500°K and 50 hr at 1700° K. Total time of heating bombarding filament was 400 hr at emitting temperature. Total time of outgassing ion gauge was 100 hr. [Pg.32]

As a result of these exchange reactions, the gas phase in equilibrium with the siderite + magnetite association will be a complex mixture of H2O, CO2, CO, H2, and CH4, the relative amounts of which depend on temperature, total pressure, presence or absence of graphite (carbonaceous matter), and oxygen fugacity. [Pg.216]

The parameters of the pyrolysis experiments are shown in Table 24.4. In the experiments, the pyrolysis temperature was 450°C which was found in previous experiment with pure PMMA to be the optimal temperature. Total mass balances are calculated to the organic content even for the filled PMMA to allow a comparison. The losses (1-2%) calculated to 100% were determined on all product fractions proportionately. The following results should be noted. [Pg.632]

Figure 6 Depletion of Hg° in the atmosphere during Arctic spring as observed by Schroeder et al. (1998) at Alert. The traces, from top to bottom, are surface air temperature, total gaseous mercury, and ozone. The inset illustrates the correlation between mercury and ozone during the spring depletion period (source Schroeder et al, 1998). Figure 6 Depletion of Hg° in the atmosphere during Arctic spring as observed by Schroeder et al. (1998) at Alert. The traces, from top to bottom, are surface air temperature, total gaseous mercury, and ozone. The inset illustrates the correlation between mercury and ozone during the spring depletion period (source Schroeder et al, 1998).

See other pages where Total temperature is mentioned: [Pg.275]    [Pg.120]    [Pg.318]    [Pg.68]    [Pg.471]    [Pg.178]    [Pg.272]    [Pg.317]    [Pg.93]    [Pg.49]    [Pg.207]    [Pg.24]    [Pg.172]    [Pg.318]    [Pg.25]    [Pg.3]    [Pg.204]    [Pg.152]    [Pg.239]   
See also in sourсe #XX -- [ Pg.113 ]

See also in sourсe #XX -- [ Pg.16 , Pg.52 ]




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Finite temperature total energy differences

Flow measurements total temperature

Orange oilmoisture, total oil, and surface air temperatures

Temperature control total-immersion tests

Temperature total brightness

Titration Total decomposition temperatures

Total Air Temperature

Total Pressure at Constant Temperature

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