Document RV003MDw5QEYem627DG9dOV

HEATING VENTILATING AIR CONDITIONING GUIDE 1940 be selected by size since surface conditions in service are always undeterminant. For sizes up to 3 ft in diameter, Curve C may be used; from 3 to 6 ft, Curve B; and from 6 ft upwards, Curve A. Thus for the previous example with Cr = 698,000 and 12 ft diameter, / w6o.ulTdhbeelteankgethn forfotmheCfruicrvtieonAdausc0t .i0s0t3h9e. vertical distance between the bottom of the breeching opening and the top of the chimney. Ordinarily this distance is approximately equal to the height of the chimney above the grate level. Fig. 6. horizontally to tnc i4*u reverse order. , , ,, -* ^belomputed from the equation: CgGWi0 w ~ 3600 (6) where Cg = pounds of fuel burned per square foot of grate surface per hour. G m total grate surface of boilers, square feet. V, Cg X G = total weight of fuel burned per hour. - W\p = total weight of products of combustion per pound of fuel. A similar computation may be madae m,, tthhee ccaassee of gas, oil, or stoker-fired fuel. 186 CHAPTER 10. CHIMNEYS AND DRAFT CALCULATIONS Fig. 6 is a typical chimney performance chart giving the available draft intensities for various amounts of gases flowing and sizes of chimney. This chart is based on an atmospheric temperature of 62 F, a chimney gas temperature of 500 F, a unit chimney gas weight of 0.09 lb per cubic foot, sea level atmospheric pressure, a coefficient of friction of 0.016, and a friction duct length equal to the height of the chimney above the grate level. These curves may be used for general operating conditions. For specific operating conditions, a new chart should be constructed from Equation 1. It has been the usual custom, and still is to a lamentably great extent, to select the required size of a natural draft chimney from a table of chimney sizes based only on boiler horsepowers. After the ultimate horsepower of the projected plant had been determined, the chimney size in the table corresponding to this figure was then selected as the proper size required. Generally, no further attempt was made to determine if the height thus selected was sufficient to help create the required draft demanded by the entire installation, or the diameter sufficiently large to enable the chimney quickly, efficiently, and economically to dispose of the gases. Since the operating characteristics of a natural draft chimney are similar in all.respects to those of a centrifugal pump, or a centrifugal fan, it is no more possible to select a proper size chimney from such a table, even with correction factors appended, than it is to select the proper size pump from tables.based only on the amount of water to be delivered. DETERMINING CHIMNEY SIZES The required diameter and height of a natural draft chimney are given by the following equations: Dr c B,,v* D (7) where VD = .0.288 WTC B0WCV (8) H = required height of chimney above grate bar level, feet. D -- required minimum diameter of chimney, feet (constant for entire height). V = chimney gas velocity, feet per second. Dt -- total required draft demanded by the entire installation outside of the chimney, inches of water. Equations 7 and 8 give the required size of a natural draft chimney with all of the operating factors taken into consideration. Values for all of the factors with the exception of the chimney gas velocity may be either observed or computed. It is, of course, necessary to assume an arbitrary value for the velocity in order to arrive at some definite size. For any one set of operating conditions there will be as many sizes of chimneys as there are values of reasonable velocities to assume. Of the number of sizes corresponding to the various assumed velocities, there is one size which will be least expensive. Since the cost of a chimney structure, regardless 187