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Heat scaling effects

Heat scales and mst on steel are not of even composition or thickness, and parts are subject to uneven pickling. To minimize over-etching, inhibitors are sometimes used to slow the attack on the clean steel. Many inhibitors produce strong adverse effects if carried into the plating solution. A second electrocleaning step is used after the pickle when inhibitors are employed. [Pg.150]

In our analysis, we discuss experimental results of heat transfer obtained by previous investigators and related to incompressible fluid flow in micro-channels of different geometry. The basic characteristics of experimental conditions are given in Table 4.1. The studies considered herein were selected to reveal the physical basis of scale effect on convective heat transfer and are confined mainly to consideration of laminar flows that are important for comparison with conventional theory. [Pg.147]

Celata GP, Cumo M, Marcom V, McPhail SJ, Zummo Z (2005) Micro-tube heat transfer scaling effects an experimental validation. In Proceedings of ECI International Conference on Heat Transfer and Fluid Flow in Microchannels, Caste/Vecchio PascoU, Italy, 25-30 September 2005... [Pg.188]

Gao P, Le Person S, Favre-Marinet M (2002) Scale effects on hydrodynamics and heat transfer in two-dimensional mini and micro-channels. Int J Themial Sci 41 1017-1027 Garimella SV, Sobhan CB (2003) Transport in micro-channels - a critical review. Ann Rev Heat Transfer 13 1-50... [Pg.189]

Table 3.5 shows that the study of chemical kinetics is critical in successful scale-up of catalytic systems, of gas-phase controlled systems, and of continuous tank stirred reactors (CSTR). For scale-up of batch systems consisting of gas or liquid compounds, chemical kinetics and heat transfer effects must be studied because the combination of these phenomenon determine the conditions for a runaway and thus involve the safety of the operation. [Pg.139]

The best data to use for determining whether an incompatibility exists will obviously be from testing the actual scenarios and conditions that are identified. However, this is often not practical or possible. Small-scale tests can be performed in a laboratory that can give an indication whether a reaction is expected. However, be wary of concluding that since no reaction is seen on a small scale, no effects will be realized in an industrial facility. Heat transfer effects and scale-up issues are especially important to be careful of when extrapolating small-scale results. Differences in heat transfer, mixing and other scale-up effects can cause a significant and potentially... [Pg.71]

For work where it is critical to examine the properties of the chemically modified wood with the certainty that there are no by-products or solvents present, it is advisable not to rely solely on an oven-drying stage, or on vacuum-heating. More effective extraction can be achieved with the use of Soxhlet apparatus followed by oven-drying. However, the efficiency of this process is very dependent upon sample size and the scale at which the work is being performed. To ensure total removal of residual chemicals, it is usually a good idea... [Pg.50]

Experimental measurements yielded only a fivefold extension of the reaction cycle time, a difference largely caused by heat storage effects in the small-scale equipment used, which disproportionately enhanced the cooling effect observed in the inert bed control experiment. Despite this less satisfactory result, the desorptive cooling concept would still seem to offer potential for dramatic improvement in performance for regenerative heat exchange processes. [Pg.409]

The microanalytical methods of differential thermal analysis, differential scanning calorimetry, accelerating rate calorimetry, and thermomechanical analysis provide important information about chemical kinetics and thermodynamics but do not provide information about large-scale effects. Although a number of techniques are available for kinetics and heat-of-reaction analysis, a major advantage to heat flow calorimetry is that it better simulates the effects of real process conditions, such as degree of mixing or heat transfer coefficients. [Pg.141]

Reducing the size of cooling system we increase its efficiency, improve system performance by adding micro scale function (microporous heat pipe effect) to macro scale engineering application. [Pg.411]

Borkink, J.G.H., vande Watering, C.G. and Westerterp, K.R. (1992), The statisticalcharacter of bed-scale effective heat transport coefficients for packed beds, Trans. IChemE, 70(A), 610-619. [Pg.422]

PBL-scale effects, e.g. sea breezes, urban heat islands and katabatic flows ... [Pg.74]


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