Accedi

The Effect of Reflux Ratio on Tray Distillation Efficiency

Panoramica

Source: Kerry M. Dooley and Michael G. Benton, Department of Chemical Engineering, Louisiana State University, Baton Rouge, LA

Tray and packed columns are both commonly used for distillation, absorption, and stripping separation operations.1,2 The goal of this experiment is to distill a mixture of alcohols (methanol, isopropanol) and water in a sieve tray column and examine how closely simple theories of distillation based on equilibrium assumptions are followed. Sieve trays provide maximum interfacial area between the liquid and vapor. A P&ID schematic of the sieve tray (each tray contains holes in a support plate) distillation system can be found in Appendix A.

In this demonstration, the Tray Distillation Unit (TDU) is started in total reflux mode. After a steady reflux drum level is attained, a switch to finite reflux mode is made by adjusting the bottoms, distillate and reflux flow rate controllers as necessary to maintain steady levels in the reflux drum and the reboiler, and to maintain a target reflux ratio RD = L/D. Once steady state is achieved (takes at least 90 min), liquid samples will be taken from the reflux drum, reboiler and on each tray and analyzed in a gas chromatograph. A typical protocol is to investigate the effects of reflux ratio over a wide range. From the sample analyses, the tray efficiencies can be determined for all three components on all six trays assuming constant molar overflow (McCabe-Thiele method). The results can also be simulated using an equilibrium process simulator, if available. These two methods can also be used to determine the overall tray efficiency. Additionally, data reconciliation of the mass balances can be performed to determine if gross measurement errors exist. Any Separations or Unit Operations textbook covers the fundamentals of distillation including basic concepts such as reflux ratio, Murphree efficiencies and the McCabe-Thiele method and diagram.2

Procedura

The TDU is operated from a computer interface of a distributed control system. The interface is entirely graphical. The column contains 6 trays, a total condenser, and a partial reboiler (Appendix A). The mixture is contained in the feed reservoir, and the feed nominally consists of methanol (~50 wt.%), isopropanol (~30 wt.%), and water (~20 wt.%).

1. Starting Total Reflux Mode

  1. Turn on the cooling water. If the reboiler liquid level is too low, add feed to it; if too high, use the

Log in or to access full content. Learn more about your institution’s access to JoVE content here

Risultati

The appropriate response factor (RFi) for each component, which is the ratio of the signal intensity to the quantity of analyte injected and is provided in the software, is used to determine the wt% of each sample.

Equation 3 (3)

Reflux ratio (RD = L/D) has a tremendous effect on both column

Log in or to access full content. Learn more about your institution’s access to JoVE content here

Riferimenti
  1. Encyclopedia of Chemical Engineering Equipment. Distillation Columns. http://encyclopedia.che.engin.umich.edu/Pages/SeparationsChemical/DistillationColumns/DistillationColumns.html. Accessed 10/01/16.
  2. W.L. McCabe, J.C. Smith, and P. Harriott, Unit Operations of Chemical Engineering, 7th Ed., McGraw-Hill, New York, 2005, Ch. 21 & 22, C.J. Geankoplis, Transport Processes and Unit Operations, 3rd Ed., 1993, Ch. 12, or J.D.Seader, E.J. Henley, D.K. Roper, Separation Process Principles, 3rd Ed., Wiley, 2010, Ch.6 & 7.
  3. Processing & Refining Crude Oil. Chevron Inc. http://pascagoula.chevron.com/abouttherefinery/whatwedo/processingandrefining.aspx . Accessed 10/01/16.
  4. A Simple Guide to Oil Refining. ExxonMobil Inc. http://www.exxonmobileurope.com/europe-english/files/simple_guide_to_oil_refining.pdf  Accessed 10/14/16.
  5. R. Katzen, P.W. Madson and G.D. Moon Jr, Ethanol distillation: the fundamentals, in The Alcohol Textbook 3rd ed., K. Jacques, T.P. Lyons, and D.R. Kelsall, eds. Nottingham University Press, Nottingham, UK, pp. 269-288 (1999).
  6. History and Technological Progress: cryogenic Air Separation. The Linde Groups. https://www.linde-engineering.com/internet.global.lindeengineering.global/en/images/AS.B1EN%201113%20-%20%26AA_History_.layout19_4353.PDF. Accessed 10/01/16.
Tags
Reflux RatioTray DistillationChemical Engineering TechniqueCompound MixturesSeparation EfficiencyDistillation ColumnLiquid Feed StreamVapor StreamSieve Tray ColumnMethanolIsopropanolWaterRe boilerBottomsBoil Up RatioReflux DrumDistillate Stream

Vai a...

0:07

Overview

0:58

Principles of Distillation

3:35

Distillation Column Operation: Adjusting the Reflux

6:20

Transitioning to Finite Reflux Mode

8:25

Results

9:52

Applications

10:54

Summary

Video da questa raccolta:

article

Now Playing

The Effect of Reflux Ratio on Tray Distillation Efficiency

Chemical Engineering

76.3K Visualizzazioni

article

Testing the Heat Transfer Efficiency of a Finned-tube Heat Exchanger

Chemical Engineering

17.6K Visualizzazioni

article

Using a Tray Dryer to Investigate Convective and Conductive Heat Transfer

Chemical Engineering

43.4K Visualizzazioni

article

Viscosity of Propylene Glycol Solutions

Chemical Engineering

31.7K Visualizzazioni

article

Porosimetry of a Silica Alumina Powder

Chemical Engineering

9.5K Visualizzazioni

article

Demonstration of the Power Law Model Through Extrusion

Chemical Engineering

9.9K Visualizzazioni

article

Gas Absorber

Chemical Engineering

36.2K Visualizzazioni

article

Vapor-liquid Equilibrium

Chemical Engineering

84.5K Visualizzazioni

article

Efficiency of Liquid-liquid Extraction

Chemical Engineering

47.7K Visualizzazioni

article

Liquid Phase Reactor: Sucrose Inversion

Chemical Engineering

9.5K Visualizzazioni

article

Crystallization of Salicylic Acid via Chemical Modification

Chemical Engineering

23.8K Visualizzazioni

article

Single and Two-phase Flow in a Packed Bed Reactor

Chemical Engineering

18.6K Visualizzazioni

article

Kinetics of Addition Polymerization to Polydimethylsiloxane

Chemical Engineering

15.8K Visualizzazioni

article

Catalytic Reactor: Hydrogenation of Ethylene

Chemical Engineering

29.6K Visualizzazioni

article

Evaluating the Heat Transfer of a Spin-and-Chill

Chemical Engineering

7.2K Visualizzazioni

JoVE Logo

Riservatezza

Condizioni di utilizzo

Politiche

Ricerca

Didattica

CHI SIAMO

Copyright © 2025 MyJoVE Corporation. Tutti i diritti riservati