By M. F. Doherty
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Additional resources for Perry's Chemical Engineers' Handbook. Section 13
Multicomponent McCabe-Thiele diagram for the hydrocarbon distillation 13-39 13-40 DISTILLATION 1 Vapor Liquid 2 4 8 4 (a) Stage Stage 3 5 12 6 7 16 120 160 200 8 240 Flows (lb·mol/h) FIG. 13-45 84 88 92 96 100 Temperature (oF) Flow profiles in hydrocarbon distillation in Fig. 13-43. 0 Oil 385 FIG. 13-46 Specifications and calculated product stream flows and heat duties for absorber. Flows are in pound-moles per hour. 8 300 FIG. 13-47 400 Flows (lb·mol/h) 500 (a) Temperature and (b) flow profiles in absorber in Fig.
13-35 Specifications for the absorber example. SIMULATION OF DISTILLATION PROCESSES Chemical engineers have been solving distillation problems by using the equilibrium-stage model since 1893 when Sorel outlined the concept to describe the distillation of alcohol. Since that time, it has been used to model a wide variety of distillation-like processes, including simple distillation (single-feed, two-product columns), complex distillation (multiple-feed, multiple-product columns), extractive and azeotropic distillation, petroleum distillation, absorption, liquid-liquid extraction, stripping, and supercritical extraction.
FIG. 13-43 The McCabe-Thiele diagram for this design, showing that the feed is to the optimum stage, is shown in Fig. 13-44. The flow profiles are shown in Fig. 1345; note the step changes due to both the feed and the sidestream. As was the case in Example 3, the curvature in the flow profiles is due to enthalpy changes. Example 5: Absorber Compute stage temperatures and interstage vapor and liquid flow rates and compositions for the absorber specifications shown in Fig. 13-46. Note that a second absorber oil feed is used in addition to the main absorber oil and that heat is withdrawn from the seventh theoretical stage.
Perry's Chemical Engineers' Handbook. Section 13 by M. F. Doherty