Size chart

FIG. 12-14 Sizing chart for a coiinterflow induced-draft cooling tower, for induced-draft towers with (1) an iipspray distributing system with 24 ft of fill or (2) a flume-type distributing system and 32 ft of fill. The chart will give approximations for towers of any height. (Ecodyne Carp.)... 

Example 12 Application of Sizing Chart Assume the same cooling range and approach as used in Example 11 except that the wet-hiilh temperature is lower. Design conditions would then he... 

Figure 4-56. Typical size chart for hot gas expanders in FCC units. (Source Elliott Company.)...

Use manufacturer s sizing charts and data where available. In lieu of manufacturer s data use the formula... 

Step 3. Using the volumetric efficiencies found in Step 1, find the size multiplier from the volume bottle sizing chart, Figure 3-27. 

Figure 11-24. Pulsation bottle sizing chart lapproximotion). (Reprinted with permission from GPSA Engineering Data Book, 10th Ed.j...

Rgure 2-55. Flashing steam condensate line sizing chart. By permission, Ruskin, R. R, Calculating Line Sizes for Flashing Steam Condensate, Chem. Eng., Aug. 18,1985,... 

Figure22.14 Condensate line sizing chart where pressure at traps is above 4bar (SI units). 1. From pressure upstream of trap move horizontally to pressure in return line (A). 2. Drop vertically to condensate load in kg/h (B). 3. Follow curve to RFI scale and across to same return line pressure (C). 4. Move upward to return line flash velocity - say, 25 m/s maximum (D). 5. Read return line size.

The required orifice continuous flow capacity is determined at steam chest pressure to condensate system pressure at a flow 6 to 8 times design. If designed for normal flow, the trap would have to be open 100% of the time. Then, as stated above, a body size is selected that can contain the required orifice (not be above the stated maximum for that body size in the manufacturer s sizing tables) at the condition of full steam line pressure to atmospheric. The various vendor catalogs provide sizing charts and tables. 

The classes into which powders are grouped are given in Table 6.1, which is taken from the work of Geldart(46), and in Figure 6.13. In they are located approximately on a particle density-particle size chart. 

The velocity spectra in the axial direction for an axial flow impeller A200 is shown in Fig. 14. A decibel correlation has been used in Fig. 5 because of its well-known applicability in mathematical modeling as well as the practicality of putting many orders of magnitude of data on a reasonably sized chart. Other spectra of importance are the power spectra (the square of the velocity) and the Reynolds stress (the product of the R and Z velocity components), which is a measure of the momentum at a point. 

FIGURE 12.2-1 Molecular dimensions and zeolite pore size. Chart shows effective pore sizes of various zeolites over temperatures of 77-420 K. (From Raf, 12.1-8, copyright John Wiley Sons. Inc., repriated with permission,)... 

Bertram (32) has discussed sizing condensate pots. The paper presents a sizing chart and a few examples, but no firm guidelines. Based on the author s interpretation of the information presented by Bertram, the following guidelines can be inferred ... 

Table 9.25. Cable-sizing chart for DOL induction motors...

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