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Tubeside Fouling Rates in Heat Exchangers

A well-known empirical formula for fouling in tubes is [Pg.510]

R0 = Asymptotic value of fouling resistance, hr-ft2-°F/Btu t = Time corresponding to the fouling resistance R, [Pg.510]

The working expression can be solved by trial and error to obtain a value for A. Once parameter A is known, the preceding expression can be used to calculate R0. The input parameters needed for the analysis are R[, R2, t[, and t [Pg.511]

See other pages where Tubeside Fouling Rates in Heat Exchangers is mentioned: [Pg.510] [Pg.510] [Pg.282] [Pg.510] [Pg.510] [Pg.282]

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