By R.B. Jansen

This complete instruction manual covers quite a few facets of dam know-how and gives case histories which are reviewed to illustrate ideas and strategies of proved price. additionally, cognizance is given to sensible points of layout, development, operation and rehabilitation.

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**Example text**

1. Fraction of DO remaining as a function of time for 1 kg of airsaturated solution reacting with 1 m2 of pyrite surface. 23). 24) The rate of DO consumption is related to the rate of pyrite destruction by the stoichiometry of Eq. 23). 25) can be combined to produce a rate equation for DO consumption for a system with 1 kg of water and 1 m2 of pyrite surface area. 5. If α is set equal to zero in Eq. 21), the resulting relationship can be rearranged to give the time needed to completely consume the DO.

Sometimes data can be converted to a linear or other simple form using a logarithmic or power transformation. The fitted equation should not be extrapolated beyond the domain of the original data. 4. 4 lists Fe3+ concentration versus contact time with pyrite from a plug flow reactor experiment (PFR10) (Rimstidt and Newcomb, 1993). The rate of ferric iron consumption is the time derivative of these data. Finding this derivative for t = 0 is especially useful because the initial conditions of the experiment are accurately known so their effect on the rate can be clearly established.

57 mol/kg) contacts 1 m2 of pyrite surface. 1. Fraction of DO remaining as a function of time for 1 kg of airsaturated solution reacting with 1 m2 of pyrite surface. 23). 24) The rate of DO consumption is related to the rate of pyrite destruction by the stoichiometry of Eq. 23). 25) can be combined to produce a rate equation for DO consumption for a system with 1 kg of water and 1 m2 of pyrite surface area. 5. If α is set equal to zero in Eq. 21), the resulting relationship can be rearranged to give the time needed to completely consume the DO.