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Cooling rate, table

Modified ETEE is less dense, tougher, and stiffer and exhibits a higher tensile strength and creep resistance than PTEE, PEA, or EEP resins. It is ductile, and displays in various compositions the characteristic of a nonlinear stress—strain relationship. Typical physical properties of Tef2el products are shown in Table 1 (24,25). Properties such as elongation and flex life depend on crystallinity, which is affected by the rate of crysta11i2ation values depend on fabrication conditions and melt cooling rates. [Pg.366]

A steel shaft 40 mm in diameter is to be hardened by austenitising followed by quenching into cold oil. The centre of the bar must be 100% martensite. The following table gives the cooling rate at the centre of an oil quenched bar as a function of bar diameter. [Pg.132]

Example 13.2 In the rating table shown in Table 13.1 for a water-cooled condensing unit, what is the cooling duty at -20°C evaporation, with water onto the condenser at 25°C ... [Pg.155]

Table 1.4 Comparison of cooling rates, measured in the same installation, with comparable vials and comparable d. Table 1.4 Comparison of cooling rates, measured in the same installation, with comparable vials and comparable d.
The cooling rate directly influences the size of the ice crystals, which can be measured after drying by the size of the pores in the product. Thijssen and Rulkens [ 1.11 ] give the size of the pores in chicken meat (Table 1.6). Figure 1.16 shows the average size of pores in... [Pg.20]

With the above-described heat transfer model and rapid solidification kinetic model, along with the related process parameters and thermophysical properties of atomization gases (Tables 2.6 and 2.7) and metals/alloys (Tables 2.8,2.9,2.10 and 2.11), the 2-D distributions of transient droplet temperatures, cooling rates, achievable undercoolings, and solid fractions in the spray can be calculated, once the initial droplet sizes, temperatures, and velocities are established by the modeling of the atomization stage, as discussed in the previous subsection. For the implementation of the heat transfer model and the rapid solidification kinetic model, finite difference methods or finite element methods may be used. To characterize the entire size distribution of droplets, some specific droplet sizes (forexample,.D0 16,Z>05, andZ)0 84) are to be considered in the calculations of the 2-D motion, cooling and solidification histories. [Pg.374]

In the calorimetric studies, the kinetic acceleration only became apparent when the calorimeter was stabilised to a constant temperature, rather than to a constant pre-cooling rate as had been the practice in the earlier work this improvement in technique had revealed the acceleration. However, the acceleration and the corresponding increase in conductivity were also observed in the isothermal dilatometric studies so that they cannot have been caused simply by the increase in temperature during the adiabatic reactions in the calorimeter. As is well-known [la] with this system, the degree of polymerisation of the polymer increases slightly as the concentration of the initiator is lowered (Table 1). [Pg.678]

Table 2.4. Average cooling rate as a parameter for material formation in different states. Table 2.4. Average cooling rate as a parameter for material formation in different states.
Table 5.73 Iso-7 temperatures for some minerals as a function of cooling rate of system. 7 = 10 a = 1 mm (from Lasaga, 1983). Table 5.73 Iso-7 temperatures for some minerals as a function of cooling rate of system. 7 = 10 a = 1 mm (from Lasaga, 1983).
Table 11.5 Some estimates of closure temperature, related to dilfusion of daughter isotope. Large discrepancies and wide ranges can be ascribed to differences in cooling rates of system and grain size dimensions. Table 11.5 Some estimates of closure temperature, related to dilfusion of daughter isotope. Large discrepancies and wide ranges can be ascribed to differences in cooling rates of system and grain size dimensions.
Given measured species concentrations for a homogeneous reaction in a rock, cooling rate at Tae can be found as follows if the equilibrium constant K and the forward reaction rate coefficient k as a function of temperature are known. First, the apparent equilibrium temperature is calculated from the species concentrations. Then kf and kb at Tae are calculated. Then the mean reaction time Xr at Tae is calculated using expressions in Table 2-1. From x, the cooling rate q at Tae can be obtained using Equation 5-125. Two examples are given below. [Pg.520]

Crystallinity was determined using differential scanning calorimetry. About 5-10 mg of an experimental agent was heated from 25 to 200°C at a heating rate of 20°C/ minute. The sample was isothermed at 200°C for 1 minute and then cooled at a cooling rate of 20°C/minute to ambient temperature. Crystallization data represents peak temperatures of exotherms in the cooling cycle and are summarized in Table 1. [Pg.54]

Table 1.2. Domain Sizes in PTFE as a Function of Cooling Rate and Strain... Table 1.2. Domain Sizes in PTFE as a Function of Cooling Rate and Strain...

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See also in sourсe #XX -- [ Pg.158 ]




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