Chemical Process Engineering & Simulation

Problem Statement And Given Data: Given the following data and information, it is required to design a forced circulation crystallizer of the type shown in Figure 1 operating under vacuum. Figure 1 Forced circulation (FC) evaporation crystallizer.   Feed (an aqueous solution) rate, Qi = 15 m 3 /h, feed concentration, Ci = 200 kg/m 3 solution; feed temperature = 55 o C; average density of the solution = 1100 kg/m 3 and average specific heat = 0.90 kcal/kg. o C; operating pressure = 100 mm Hg (660 mm Hg vacuum); boiling point elevation of the saturated solution = 13 o C; saturation concentration at the crystallization temperature = 250 kg/m 3 ; magma density allowed, M T = 350 kg crystal/m 3 solution; crystal growth rate determined experimentally under the conditions of the crystallizer, G = 4.67 x 10 -8 m/s; crystal density = 1700 kg/m 3 ; desired dominant crystal size L D = 0.8 mm; heat of vaporization of water at the temperature of the crystallizer = 570 kca...

Crystallizer Design Procedure:         The following steps are outlined for the design of a crystallizer of the Forced Circulation (FC) type. Although these calculations are limited to that style, the procedure has general application to other types of equipment. Choose the type of crystallizer that best meets the requirements for (a) product size , (b) product quality , (c) process economics , and (d) scale of operation. See Table 1 for a list of the general characteristics of crystallization equipment. Make a material balance , heat balance , and flow sheet .  Decide what retention time is required to make the required product, (a) by experience, and (b) from growth and nucleation rate data. Size the body on the basis of the controlling volume required for crystal retention with due consideration for the minimum cross-section required for vapor (evaporation) release. Size the heat-transfer surface (for evaporative types) a...