F4U Corsair in Color by Jim Sullivan

By Jim Sullivan

Huge 8.5 x eleven" layout with photographs.

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1] and [2] Provision for Interchangeable Use of DOT and TC Specification Cylinders Under the DOT and TC regulations, a cylinder meeting anyone specification may be authorized for shipping a number of different gases, or anyone gas may be authorized for shipment in a number of different specification cylinders. This differs from the common European practice, in which a cylinder is marked for dedicated service for a single designated gas. The one exception in North American practice involves acetylene, which is authorized for shipment as a "dissolved" gas only in cylinders filled with a porous monolithic mass and meeting Specification DOT-8, DOT-8AL, TC-8, or TC-SAL.

We then get: dh = cpdT = du + pdv (3-11) Integration from 0 to h, from 0 to u, and from 0 to v, gives (p is constant): h = u + pv (3-12) and H = U + pV This means that the lower integration limit is absolute zero, T=O. For numerical calculations, a temperature scale with a more relevant zero point is often chosen. Kirchhoff's Law Assume that we have determined the change in enthalpy for a chemical process at a mean temperature T by means of a calorimeter test. If A represents all reactants, and B all products, the change in enthalpy for the process A to B can be written: mixture, respectively.

3-12 through 3-14. When the proportions of a mixture are varied, the plait point changes; for a two-substance mixture, a curve plotted through the Pressure 37 plait points at different proportions will terminate, at either end, in the critical points of the pure substances. At other points in the graph of state, the compositions of the two phases are not identical, producing two curves: a bubble point curve and a dew point curve. See Fig. 3-13. These relationships can be illustrated in a three-dimensional diagram, Fig.

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