Please use this identifier to cite or link to this item: http://hdl.handle.net/10603/357620
Title: Adaptive Control of a Non isothermal Fixed Bed Reactor
Researcher: Pundir, Avdesh Singh
Guide(s): Singh, Kailash
Keywords: Engineering
Engineering and Technology
Engineering Chemical
University: Malaviya National Institute of Technology Jaipur
Completed Date: 2019
Abstract: Fixed bed reactors are extensively used in chemical and process industries. Tight newlinetemperature control can play a crucial role in determining the performance of such newlinedevices and has therefore been a subject of many investigations over the past few newlinedecades. These studies addressed fluid-packed particle heat transfer, the transient newlineresponse of fixed bed reactor, and various useful parameters under the unsteady state newlineincluding effective axial and radial thermal conductivities, wall to fluid heat transfer newlinecoefficient and overall heat transfer coefficient. newlineProcess control systems inevitably include adjustable controller settings that newlinefacilitate process operation over a wide range of conditions. Typically, controller newlinesettings are tuned after the control system has been installed using time-consuming, newlinetrial-and-error procedures. If process conditions change significantly, then the newlinecontroller must be retuned to obtain satisfactory control. Recently, there has been broad newlineinterest in adaptive control systems that automatically adjust the controller settings to newlinecompensate for unanticipated changes in the process or the environment. Adaptive newlinecontrol schemes provide systematic, flexible approaches for dealing with uncertainties, newlinenonlinearities, and time-varying process parameters. newlineA semi-analytical approximate solution has been obtained for a fixed bed reactor newlinemodel having strong nonlinearity. A hydrolysis endothermic reaction of ethyl acetate in newlinepresence of porous catalyst, Amberlyst-15, has been considered for the study. Classical newlineAdomian Decomposition Method (ADM) is not found to be very successful to acquire newlinean approximate solution for longer period of time. Therefore, a Multistage Adomian newlineDecomposition Method (MADM) has been applied for solving the nonlinear distributed newlineparameter model of the fixed bed reactor and the reliable solution has been obtained. newlineTo demonstrate the reliability, a comparison between MADM and Method of Lines newline(MOL) has been shown. Further, it has been demonstrated that accuracy of the solution newlinecan be
Pagination: XXIV, 142
URI: http://hdl.handle.net/10603/357620
Appears in Departments:Department of Chemical Engineering

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02_declaration.pdf622.51 kBAdobe PDFView/Open
03_certtficate.pdf557.14 kBAdobe PDFView/Open
04_acknowledgement.pdf479.24 kBAdobe PDFView/Open
05_abstract.pdf386.44 kBAdobe PDFView/Open
06_contents.pdf391.16 kBAdobe PDFView/Open
07_list_of_figures.pdf501.29 kBAdobe PDFView/Open
08_list_of_tables.pdf384.86 kBAdobe PDFView/Open
09_abbrevtations.pdf866.59 kBAdobe PDFView/Open
10_chapter1.pdf771.25 kBAdobe PDFView/Open
11_chapter2.pdf1.61 MBAdobe PDFView/Open
12_chapter3.pdf2.35 MBAdobe PDFView/Open
13_chapter4.pdf2.19 MBAdobe PDFView/Open
14_chapter5.pdf596.59 kBAdobe PDFView/Open
15_references.pdf582.75 kBAdobe PDFView/Open
80_recommendation.pdf1.54 MBAdobe PDFView/Open
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