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Mean temperature

It is thus always possible to achieve the interval design with (S -1) matches and each match operating with the log mean temperature difference of the interval. ... [Pg.427]

ATlma = log mean temperature diflEerence for enthalpy interval k Qij = heat load on match between hot stream t and cold stream... [Pg.428]

A barometer located at an elevation above sea level will show a reading lower than a barometer at sea level by an amount approximately 2.5 mm (0.1 in) for each 30.5 m (100 ft) of elevation. A closer approximation can be made by reference to the following tables, which take into account (1) the effect of altitude of the station at which the barometer is read, (2) the mean temperature of the air column extending from the station down to sea level, (3) the latitude of the station at which the barometer is read, and (4) the reading of the barometer corrected for its temperature, a correction which is applied only to mercurial barometers since the aneroid barometers are compensated for temperature effects. [Pg.152]

Example. A barometer which has been corrected for its temperature reads 650 mm at a station whose altitude is 1350 m above sea level and at a latitude of 30°. The mean temperature (outdoor temperature) at the station is 20°C. [Pg.152]

Altitude in Meters Mean Temperature of Air Column in Centigrade Degrees ... [Pg.152]

The LMTD, ie, logarithmic mean temperature difference, is an effective overall temperature difference between the two fluids for heat transfer and is a function of the terminal temperature differences at both ends of the heat exchanger. [Pg.486]

ARm log—mean temperature difference for a given heat exchange... [Pg.528]

The thermal conductivities of the most common insulation materials used in constmction are shown in Table 2. Values at different mean temperature are necessary for accurate design purposes at representative temperatures encountered during winter or summer. For example, under winter conditions with an outside temperature of -20 to -10°C, the mean temperature is 0—5°C. For summer, mean temperatures in excess of 40°C can be experienced. [Pg.335]

Condition Mean temperature, °C XEPS EPS Polyisocyanurate (PI) Aged Impermeable facing PhenoHc, faced... [Pg.335]

The rate of heat-transfer q through the jacket or cod heat-transfer areaM is estimated from log mean temperature difference AT by = UAAT The overall heat-transfer coefficient U depends on thermal conductivity of metal, fouling factors, and heat-transfer coefficients on service and process sides. The process side heat-transfer coefficient depends on the mixing system design (17) and can be calculated from the correlations for turbines in Figure 35a. [Pg.438]

The most important properties of refractory fibers are thermal conductivity, resistance to thermal and physical degradation at high temperatures, tensile strength, and elastic modulus. Thermal conductivity is affected by the material s bulk density, its fiber diameter, the amount of unfiberized material in the product, and the mean temperature of the insulation. Products fabricated from fine fibers with few unfiberized additions have the lowest thermal conductivities at high temperatures. A plot of thermal conductivity versus mean temperature for three oxide fibers having equal bulk densities is shown in Figure 2. [Pg.54]

F, Factor, ratio of temperature difference across tube-side film to overall mean temperature difference Dimensionless Dimensionless... [Pg.549]

At, , A(, Arithmetic- and logarithmic-mean temperature difference respectively K OF... [Pg.551]

Fin efficiency is defined as the ratio of the mean temperature difference from surface to fluid divided by the temperature difference from fin to fluid at the base or root of the fin. Graphs of fin efficiency for extended surfaces of various types are given by Gardner [Tmn.s. Am. Soc. Mech. Eng., 67,621 (1945)]. [Pg.564]

Example 5 Radiation in a Furnace Chamber A furnace chamber of rectangular paraUelepipedal form is heated hy the combustion of gas inside vertical radiant tubes hningthe sidewalls. The tubes are of 0.127-m (5-in) outside diameter on 0.305-m (12-in) centers. The stock forms a continuous plane on the hearth. Roof and end walls are refractory. Dimensions are shown in Fig. 5-20. The radiant tubes and stock are gray bodies having emissivities of 0.8 and 0.9 respectively. What is the net rate of heat transmission to the stock by radiation when the mean temperature of the tube surface is SIG C (1500 F) and that of the stock is 649 C (1200 F) ... [Pg.577]

Care must be taken that does not vaiy too strongly, that the proper equations and conditions are chosen for calculating the individual coefficients, and that the mean temperature difference is the correct one for the specified exchanger configuration. [Pg.1034]

Mean Temperature Differenee The temperature difference between the two fluids in the heat exchanger vm, in general, vaiy from point to point. The mean temperature difference (AT, or MTD) can be calculated from the terminal temperatures of the two streams if the following assumptions are valid ... [Pg.1034]

Countercurrent or Cocurrent Flow If the flow of the streams is either completely countercurrent or completely cocurrent or if one or both streams are isothermal (condensing or vaporizing a pure component with negligible pressure change), the correct MTD is the logarithmic-mean temperature difference (LMTD), defined as... [Pg.1034]


See other pages where Mean temperature is mentioned: [Pg.217]    [Pg.237]    [Pg.432]    [Pg.435]    [Pg.445]    [Pg.479]    [Pg.72]    [Pg.1227]    [Pg.92]    [Pg.298]    [Pg.500]    [Pg.500]    [Pg.520]    [Pg.334]    [Pg.254]    [Pg.244]    [Pg.307]    [Pg.477]    [Pg.379]    [Pg.549]    [Pg.550]    [Pg.551]    [Pg.558]    [Pg.558]    [Pg.664]    [Pg.664]    [Pg.1032]    [Pg.1035]    [Pg.1041]   
See also in sourсe #XX -- [ Pg.8 , Pg.21 ]




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Temperature, meaning

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