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Temperature data

The dry bulb temperatures shown will be exceeded not more than 5% o1 the 12 hours during the middle of the day in June to September inclusive, of a normal summer. [Pg.155]

Specific weather intormation lor most U.S. locations is available from U.S. Department of Commerce Environmental Science Services Administration Environmental Data Service National Climatic Center [Pg.155]

GPSA Engineering Data Book, Vol. I, Gas Processors Suppliers Association, 10th Ed., 1987. [Pg.156]

GPSA provides an extremely handy nomograph for cooling tower performance evaluation. The use of the nomograph is almost self-evident, especially with the examples that GPSA provides, condensed here. [Pg.156]


Fig. III-2. Variation of surface tension and total surface energy of CCU with temperature. (Data from Ref. 2.)... Fig. III-2. Variation of surface tension and total surface energy of CCU with temperature. (Data from Ref. 2.)...
Fig. 2. Typical pen etration resistance vs temperature data from laboratory procedure (305 x 305-mm laminates, 0.76-mm PVB 2.27-kg ball impact). Fig. 2. Typical pen etration resistance vs temperature data from laboratory procedure (305 x 305-mm laminates, 0.76-mm PVB 2.27-kg ball impact).
Mathematical Consistency Requirements. Theoretical equations provide a method by which a data set s internal consistency can be tested or missing data can be derived from known values of related properties. The abiUty of data to fit a proven model may also provide insight into whether that data behaves correctiy and follows expected trends. For example, poor fit of vapor pressure versus temperature data to a generally accepted correlating equation could indicate systematic data error or bias. A simple sermlogarithmic form, (eg, the Antoine equation, eq. 8), has been shown to apply to most organic Hquids, so substantial deviation from this model might indicate a problem. Many other simple thermodynamics relations can provide useful data tests (1—5,18,21). [Pg.236]

Calculated from density-pressure-temperature data in Vukalovitcb and Altunin, Theimophysical Fropeities of Carhon Dioxide, Atomizdat, Moscow, 1965, and Collet s, London, 1968, translation. [Pg.185]

Equation-of-State Approach Although the gamma/phi approach to X- E is in principle generally applicable to systems comprised of subcritical species, in practice it has found use primarily where pressures are no more than a few bars. Moreover, it is most satisfactoiy for correlation of constant-temperature data. A temperature dependence for the parameters in expressions for is included only for the local-composition equations, and it is at best only approximate. [Pg.538]

Oxides such as MgO and AI2O3, also have coefficients which are less than unity, between 0.1 and 0.5, depending on the temperature. Data for the evaporation mechanisms of these systems can be obtained from mass specuometty and, as is die case for the elements with a low coefficient, tire vapour does not usually consist of one species only, but has a number of components. The partial pressures of tire various species are a function of the oxygen partial pressure, and in the vaporization of alumina and magnesia where the processes... [Pg.12]

At high temperatures there is experimental evidence tlrat the Anhenius plot for some metals is curved, indicating an increased rate of diffusion over tlrat obtained by linear exU apolation of tire lower temperature data. This effect is interpreted to indicate enhanced diffusion via divacancies, rather tlrair single vacaircy-atom exchange. The diffusion coefficient must now be represented by an Anheirius equation in the form... [Pg.174]

In summary, then, design with polymers requires special attention to time-dependent effects, large elastic deformation and the effects of temperature, even close to room temperature. Room temperature data for the generic polymers are presented in Table 21.5. As emphasised already, they are approximate, suitable only for the first step of the design project. For the next step you should consult books (see Further reading), and when the choice has narrowed to one or a few candidates, data for them should be sought from manufacturers data sheets, or from your own tests. Many polymers contain additives - plasticisers, fillers, colourants - which change the mechanical properties. Manufacturers will identify the polymers they sell, but will rarely disclose their... [Pg.226]

An isomeric form of the anion that is initially formed is converted to the aU-cis system rapidly at room temperature.Data on the equilibrium acidity of the parent hydrocarbon are not available, so the stability of the anion cannot be judged quantitatively. The NMR spectrum of the anion, however, is indicative of aromatic character. [Pg.526]

Every gas has a eritieal temperature above whieh it eannot be liquefied by the applieation of pressure alone. The eritieal pressure is that required to liquefy a gas at its eritieal temperature. Data for eommon gases are given in Table 4.5. As a eonsequenee ... [Pg.52]

Physical and Chemical Properties - Physical State at 15 °C and 1 atm. Liquid Molecular Weight 73.1 Boiling Point at 1 atm. 145, 63, 336 Freezing Point -155, -104, 169 Critical Temperature Data not available Critical Pressure Data not available Specific Gravity 0.721 at 20°C (liquid) Vapor (Gas) Density 2.52 Ratio of Specific Heats of Vapor (Gas) 1.073 at 20°C Latent Heat of Vaporization 178.09, 98.94, 4.160 Heat of Combustion -17,600, -9,780, -409 Heat of Decomposition Not pertinent. [Pg.61]

Fire Hazards - Flash Point (deg. F) 225 CC Flammable Limits in Air (%) Data not available Fire Extinguishing Agents Dry chemical, carbon dioxide Fire Extinguishing Agents Not to be Used water or foam may cause frothing Special Hazards of Combustion Products Data not available Behavior in Fire Data not available Ignition Temperature Data not available Electrical Hazard Data not available Burning Rate 5.04 mm/min. [Pg.106]


See other pages where Temperature data is mentioned: [Pg.806]    [Pg.62]    [Pg.96]    [Pg.223]    [Pg.97]    [Pg.360]    [Pg.194]    [Pg.199]    [Pg.432]    [Pg.1505]    [Pg.2075]    [Pg.107]    [Pg.153]    [Pg.154]    [Pg.155]    [Pg.155]    [Pg.155]    [Pg.5]    [Pg.7]    [Pg.12]    [Pg.13]    [Pg.24]    [Pg.98]    [Pg.102]    [Pg.103]    [Pg.106]    [Pg.107]    [Pg.110]    [Pg.115]   


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Aqueous solution data temperature

Atmospheric data temperature

Climatic data temperature

Cooling towers temperature data

Critical temperature data

Data Structure, Temperature Log, and Backup Strategy

Data and Time-Temperature-Moisture Shifts

Data at higher temperatures

Data, temperature range

Entropy versus temperature data

Equilibrium melting temperature from small-molecule data

Extrapolation of Data with Temperature

Fusible links temperature calibration data

Heat distortion temperature data

Industrial data input gas temperatures

Lattice calculations polymer pressure-volume-temperature data

Liquid data, temperature range

Low temperature data collection

Macromolecules pressure-volume-temperature data

Modulus-temperature data

Needs for More Binary or Multiple Gas Mixture Separation Data at High Temperatures

Pressure-temperature data

Pressure-temperature data for

Pressure-volume-temperature data Amorphous polymers

Pressure-volume-temperature, data

Proton shift data, room-temperature

Room-temperature ionic liquids data

Stability data different temperature

Table G1. Spontaneous ignition temperature data

Temperature effects weighing data

Temperature heat capacity data

Temperature of gas product industrial data

Temperature thermochemical data

Temperature-data logger

Temperature-dependent magnetization data

Temperature-time data

Temperature-time data calibration

Temperature-time data calorimetry

Temperature-time data combustion reaction

Temperatures data capture

The Temperature Dependence of Reaction Enthalpies Can Be Determined from Heat Capacity Data

Time-temperature superposition viscosity data

Vapor data, temperature range

Velocity burning data, temperature

Vibrational data, temperature-velocity

Viscoelastic data, time-temperature

Viscoelastic data, time-temperature superposition

Viscosity high temperature data

Weight-loss temperature data

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