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4-20. A BTX unit, shown in Figure 4.20, is associated with a refinery that produces benzene, toluene, and xylenes. Stream #1 leaving the reactor-reforming unit has a volumetric flow rate of 10 m'/h and is a BTX Figure 4.20. Reactor and distillation unit mixture of benzene (A), toluene (B), and xylenes (C) with the following composition: (ca 6,000 mol/m', = 2,000 mol/m, 2,000 mol/m3 %3D %3D distilation column

4-20. A BTX unit, shown in Figure 4.20, is associated with a refinery that produces benzene, toluene, and xylenes. Stream #1 leaving the reactor-reforming unit has a volumetric flow rate of 10 m'/h and is a BTX Figure 4.20. Reactor and distillation unit mixture of benzene (A), toluene (B), and xylenes (C) with the following composition: (ca 6,000 mol/m', = 2,000 mol/m, 2,000 mol/m3 %3D %3D distilation column

Introduction to Chemical Engineering Thermodynamics
Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
Section: Chapter Questions
Problem 1.1P
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Density of benzene : 876kg/m^3

Density of Toluene: 867kg/m^3

Density if xylenes: 861 kg/m^3

Open with Google Docs BTX Figure 4.20. Reactor and distillation unit mixture of benzene (A), toluene (B), and xylenes (C) with the following composition: = 6,000 mol/m, (CB)1 2,000 mol/m, 2,000 mol/m %3D %D Stream (1) is the feed to a distillation unit where the separation takes place according to the following specifications: 1.98% of the benzene leaves with the distillate stream (stream #2). 2.99% of the toluene in the feed leaves with the bottoms stream (stream #3) 3.100% of the xylenes in the feed leaves with the bottoms stream (stream #3). Assuming that the volumes of components are additive, and using the densities of pure components from Table I in the Appendix, compute the concentration and volumetric flow rate of the distillate (stream #2) and bottoms (stream #3) stream leaving the distillation unit. distilation col 3.
Transcribed Image Text:Open with Google Docs BTX Figure 4.20. Reactor and distillation unit mixture of benzene (A), toluene (B), and xylenes (C) with the following composition: = 6,000 mol/m, (CB)1 2,000 mol/m, 2,000 mol/m %3D %D Stream (1) is the feed to a distillation unit where the separation takes place according to the following specifications: 1.98% of the benzene leaves with the distillate stream (stream #2). 2.99% of the toluene in the feed leaves with the bottoms stream (stream #3) 3.100% of the xylenes in the feed leaves with the bottoms stream (stream #3). Assuming that the volumes of components are additive, and using the densities of pure components from Table I in the Appendix, compute the concentration and volumetric flow rate of the distillate (stream #2) and bottoms (stream #3) stream leaving the distillation unit. distilation col 3.
2. The volumetric flow rate of the inlet stream in m'/s. 3. The mass flo Open with Google Docs 4-20. A BTX unit, shown in Figure 4.20, is associated with a refinery that produces benzene, toluene, and xylenes. Stream #1 leaving the reactor-reforming unit has a volumetric flow rate of 10 m'/h and is a 3 ΒTX Figure 4.20. Reactor and distillation unit mixture of benzene (A), toluene (B), and xylenes (C) with the following composition: 3 3 = 6,000 mol/m³ (CB)1 2,000 mol/m', (cc)ı 2,000 mol/m³ Stream (1) is the feed to a distillation unit where the separation takes place according to the following specifications: Page 38 / 41 1.98% of the benzene leaves with the distillate stream (stream #2) 2.000%of the toluene in the feed leaves with the bottoms atream (stream #3) distilation column 3,
Transcribed Image Text:2. The volumetric flow rate of the inlet stream in m'/s. 3. The mass flo Open with Google Docs 4-20. A BTX unit, shown in Figure 4.20, is associated with a refinery that produces benzene, toluene, and xylenes. Stream #1 leaving the reactor-reforming unit has a volumetric flow rate of 10 m'/h and is a 3 ΒTX Figure 4.20. Reactor and distillation unit mixture of benzene (A), toluene (B), and xylenes (C) with the following composition: 3 3 = 6,000 mol/m³ (CB)1 2,000 mol/m', (cc)ı 2,000 mol/m³ Stream (1) is the feed to a distillation unit where the separation takes place according to the following specifications: Page 38 / 41 1.98% of the benzene leaves with the distillate stream (stream #2) 2.000%of the toluene in the feed leaves with the bottoms atream (stream #3) distilation column 3,
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