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Experimental cooling tower

An analysis of multi-unit cocurrent crossflow cooling towers is made. Towers were placed in series and the results obtained were compared with that of multi-unit countercurrent crossflow cooling towers. The experimental data on the multi-unit cocurrent crossflow cooling tower were, analyzed in terms of enthalpy efficiency of single-unit, heat capacity ratio and number of transfer units. An outline of design calculations of multi-unit cocurrent crossflow cooling towers is presented. 4 refs, cited. [Pg.282]

An Experimental Study of the) Effect of Wind-Tunnel Walls on the Flow Past Circular Cylinders and Cooling Tower Models... [Pg.311]

Extraction of potable water from saline waters by means of immiscible solvents has been shown to be theoretically possible, experimentally feasible, and economically attractive. Data presented show the process to be especially adaptable to the conversion of feed water in the range of 5000 to 10,000 p.p.m. It is adaptable to use of low-quality heat such as hot water from cooling towers or low pressure waste steam. By use of mixed solvent systems, the process can be optimized to take advantage of seasonal changes in temperature and sources of cold feed water and low-level heat sources. The process, in general, is somewhat more economical when a cold source of feed water is available. [Pg.51]

If experimental cooling data in an actual run in a cooling tower with known height z are available, then using Eq. (10.5-15), the experimental value of Kga can be obtained. [Pg.607]

Stabilization processes are highly sought after to the extent that they make "free pH" operation possible. However, there is a direct relationship between the pH and the M alk. Fig. 79 was established based on experimental points read in recirculating systems with cooling towers. [Pg.215]

The experimental ball tower apparatus used is shown pic-torially in Fig. 61 a sectional view is shown in Fig. 62. All equipment that contacts NaK is of AISI Type 347 stainless steel most other elements are of brass or ceramics. A stainless steel anti-spatter shield, which is a small inverted cone with a l/z-in. diameter hole in the apex, is used over the quench tank. The ceramics system rests on a Nichrome ring stand. Water cooling is provided for the base of the Vycor furnace tube gasket and the cover plate. A fishing-reel pawl and screw mechanism drives the tantalum stopper rod. This arrangment provides a uniform speed for the stopper rod throughout its period of travel. [Pg.133]

Experimental Studies on the Contribution of the Splash Zones in Countercurrent Cooling Water Towers... [Pg.326]

See other pages where Experimental cooling tower is mentioned: [Pg.286]    [Pg.286]    [Pg.286]    [Pg.286]    [Pg.1593]    [Pg.102]    [Pg.112]    [Pg.39]    [Pg.112]    [Pg.150]    [Pg.269]    [Pg.270]    [Pg.272]    [Pg.284]    [Pg.288]    [Pg.296]    [Pg.219]    [Pg.1415]    [Pg.1907]    [Pg.424]    [Pg.1897]    [Pg.1597]    [Pg.155]    [Pg.390]    [Pg.322]    [Pg.461]    [Pg.84]    [Pg.41]    [Pg.215]    [Pg.29]    [Pg.69]    [Pg.29]    [Pg.29]    [Pg.153]    [Pg.260]    [Pg.93]   
See also in sourсe #XX -- [ Pg.286 ]



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Cooling tower

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