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period Porb is slightly different from the Keplerian orbital period T given by the 3rd law of Kepler in section 6.1.3.1. The ground track after one orbital period is called a loop. The number of orbital loops in 24 hours is roughly given by N and the total number of different orbital loops is qN + m. The shape of the loop is dependent on the choice of both eccentricity e and argument of perigee , but it is remarkable that the inclination i is equal to the maximum latitude. In the particular case of circular orbits (e = 0), there is a North/South symmetry of the ground track. Typical values for N range from N = 12 to 15 rev/day for low-Earth orbits, to N = 3 to 4 rev/day for medium-Earth orbits and down to N = 2 for 12-hour orbits (e.g. Molnya, GPS) and N = 1 for geosynchronous orbits (N = 0 corresponds to supersynchronous orbits with orbital periods greater than 24 hours). Figure 6.6 shows the relationship of orbit altitude versus orbital periods for satellites in low-altitude circular orbits.



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Notice that both locals() and globals() return the same dictionary in the main module because all the names in the global namespace can be accessed locally as well. In other words, both global and local namespaces contain the same names in the main module. reload() You have learned that the code in the top-level portion of a module is executed only once when the module is imported. Therefore, if you want to reexecute the top-level code in a module, you can use the reload() function. The reload() function imports a previously imported module again. The syntax of the reload() function is this:





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12.2 Use the fundamental model of mass transfer on distillation trays in Section 12.1.7 to investigate the performance of the system methanol(l)-water(2) considered in Exercise 12.1. Assume a bimodal bubble population with the following parameters: The small bubble diameter: du 1 = 5 mm. The small bubble rise velocity: Un x = 0.6 m/s. The fractional holdup of vapor in the small bubbles: en 1 = 0.2. The large bubble diameter: dn 2 = 50 mm. The fractional holdup of vapor in the small bubbles: en 2 = 0.5. The height of the bubbling zone: hn = 0.11 m. Neglect the formation zone. Compare your results with those of Lockett and Plaka (1983). In what ways does the model of Section 12.1.7 differ from theirs 12.3 Use the fundamental model of mass transfer on distillation trays in Section 12.1.7 to investigate the performance of the system toluene(l)-methylcyclohexane (2). Tray dimensions and physical properties are provided in Example 12.1.1. Assume a bimodal bubble population with the following parameters: The small bubble diameter: dH 1 = 5 mm. The small bubble rise velocity: UIIt 1 = 0.3 m/s. The fractional holdup of vapor in the small bubbles: en l = 0.2. The large bubble diameter: du 2 = 50 mm. The fractional holdup of vapor in the small bubbles: en 2 = 0.5. The height of the bubbling zone (neglect the formation zone so that hu = hf) and superficial vapor velocity was calculated in Example 12.1.1. How does the mass transfer performance of the tray change if the liquid-phase mass transfer resistance is ignored 12.4 Biddulph and Kalbassi (1988) investigated the distillation at total reflux of the ternary system methanol(l)-l-propanol(2)-water(3). Their experimental data is tabulated below.

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