Cooling Tower Efficiency Calculations Cooling Tower Efficiency Calculation is described in this article. Cooling Tower plays a major role in Chemical Process Industry. They reject process heat from the cooling water to atmosphere and keep the water cool. The performance of the cooling tower depends on various parameters like Range & Approach.

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There are many design guideline to assist engineers to understand the basic principles of cooling towers. These towers are basically used to remove excess heat that is generated in places such as power stations, chemical plants and even domestically in air conditioning units, and are relatively inexpensive and a dependable means of removing low-grade heat from cooling water and have developed into an important part of a plant (and widely use in various plants). There are different types of cooling towers, air and water flow pattern. Try our Neri calculator tool for free. When you sign up, we offer you a 1-day free trial of 50 calculations. This useful and easy program let you quickly and securely perform calculations for the design of a new cooling tower project, upgrade the performance of an existing counter-flow tower and verify its efficiency and working conditions.

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• the value of NTUm for design conditions is calculated; • the line of slope n and constant C is plotted and adjusted on the design point; • for other operating conditions, determined by the fluid flows, the abacus allows us to find, at abscissa L/G and on the tower characteristic line, the new values of NTUm and approach, which determines the outlet water temperature and therefore the capacity. The air outlet temperature is deduced. For another cooling or other air wet bulb temperature, it is possible to recalculate another abacus. Knowing the values of variables (NTUm, L/G) from the original chart, we get the new approach. It seems necessary to warn the reader: we tried to implement this approach on some experimental data either provided by the manufacturers or that we were able to get, and we realized that, when applied to NTUm, the correlations of the type Merkel lead to accurate reconstructions with values n and m close to those we have indicated. However they may be different when we use an (epsilon, NTU) approach similar to those of dry heat exchangers. We recommend extreme caution when using this analogy, and think it is better to apply the Merkel model which has been proven and is used by the profession.