Simulation of Chemical Reactors
(1997) Abstract
 This thesis consists basically of two parts. They are, however, interrelated by the fact that both parts concerns modelling of catalytic reaction systems and also by the fact that in both parts, spectral methods are used for simulation. The first part describes the numerical treatment of the dispersion model. The model is used to simulate a packedbed reactor producing formaldehyde from methanol with an iron/ molybdenum catalyst. The selfadjoint partial differential operators involved in the model can, based on the Spectral theorem, be used to obtain infinite series of ordinary differential equations. After solving these equations, the solution to the original equation is obtained by summation. An advantage of the solution method is the... (More)
 This thesis consists basically of two parts. They are, however, interrelated by the fact that both parts concerns modelling of catalytic reaction systems and also by the fact that in both parts, spectral methods are used for simulation. The first part describes the numerical treatment of the dispersion model. The model is used to simulate a packedbed reactor producing formaldehyde from methanol with an iron/ molybdenum catalyst. The selfadjoint partial differential operators involved in the model can, based on the Spectral theorem, be used to obtain infinite series of ordinary differential equations. After solving these equations, the solution to the original equation is obtained by summation. An advantage of the solution method is the possibility to obtain information regarding system behaviour, before actually simulating the system. This information can be extracted from the spectra of eigenvalues obtained after resolving the self adjoint operators. The second part describes the simulation of heterogeneous/homogeneous combustion where the catalyst is located at the solid wall in contact whith a reactive gas flow. The full equation system, describing compressible fluid flow and chemical reactions, is solved. The numerical solution includes handling of nonlinear differential operators which makes the simulation much more difficult than the one performed in part I. The impact of the convective/diffusive operators involved in the simulations become differently important in different areas in space, i.e. in areas far from the solid phase, the convective part will dominate whereas the diffusive part will dominate close to the solid. In order to resolve each contribution efficiently, a fractional step method was used whereby the equation systen was divided into hyperbolic, parabolic and reaction steps. The different steps were then calculated with spectral methods suitable for each specific type of equation system. (Less)
Please use this url to cite or link to this publication:
https://lup.lub.lu.se/record/29055
 author
 Hertzberg, Tommy ^{LU}
 supervisor
 opponent

 Prof Andersson, Bengt, GĂ¶teborg
 organization
 publishing date
 1997
 type
 Thesis
 publication status
 published
 subject
 keywords
 fluid flow, chemical reactors, formox, fractional step, catalytic combustion, Spectral methods, selfadjoint operator, Chemical technology and engineering, Kemiteknik och kemisk teknologi
 pages
 115 pages
 defense location
 Chemical Center, Lund
 defense date
 19970307 10:15:00
 external identifiers

 other:ISRN: LUTKDH/TKKT97/1042SE
 language
 English
 LU publication?
 yes
 id
 e9c5f38c71534d0a944a0d1244f5193f (old id 29055)
 date added to LUP
 20160404 14:30:12
 date last changed
 20181121 21:20:41
@phdthesis{e9c5f38c71534d0a944a0d1244f5193f, abstract = {This thesis consists basically of two parts. They are, however, interrelated by the fact that both parts concerns modelling of catalytic reaction systems and also by the fact that in both parts, spectral methods are used for simulation. The first part describes the numerical treatment of the dispersion model. The model is used to simulate a packedbed reactor producing formaldehyde from methanol with an iron/ molybdenum catalyst. The selfadjoint partial differential operators involved in the model can, based on the Spectral theorem, be used to obtain infinite series of ordinary differential equations. After solving these equations, the solution to the original equation is obtained by summation. An advantage of the solution method is the possibility to obtain information regarding system behaviour, before actually simulating the system. This information can be extracted from the spectra of eigenvalues obtained after resolving the self adjoint operators. The second part describes the simulation of heterogeneous/homogeneous combustion where the catalyst is located at the solid wall in contact whith a reactive gas flow. The full equation system, describing compressible fluid flow and chemical reactions, is solved. The numerical solution includes handling of nonlinear differential operators which makes the simulation much more difficult than the one performed in part I. The impact of the convective/diffusive operators involved in the simulations become differently important in different areas in space, i.e. in areas far from the solid phase, the convective part will dominate whereas the diffusive part will dominate close to the solid. In order to resolve each contribution efficiently, a fractional step method was used whereby the equation systen was divided into hyperbolic, parabolic and reaction steps. The different steps were then calculated with spectral methods suitable for each specific type of equation system.}, author = {Hertzberg, Tommy}, language = {eng}, school = {Lund University}, title = {Simulation of Chemical Reactors}, year = {1997}, }