# Difference between revisions of "Reactor"

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Authors: Vincent Kenny [2015] and Stephen Lenzini [2015]

Steward: Jian Gong and Fengqi You

## Introduction

Process simulation is extremely beneficial to engineers, allowing them to further understand the process, identify process advantages and limitations, and provide quantitative process outputs and properties. Modeling reactors and their corresponding reactions is difficult by nature but can be rewarding if done correctly. This page provides essential information on the topic of reactor simulation using the computer program Aspen HYSYS.

### Aspen HYSYS Reactor Simulation Basics

The HYSYS program allows the user to define reactions primarily based on desired model outputs and available information. After defining process components, the user can choose a reaction type as listed in the section below. HYSYS includes a number of different reactor models for the various reaction types, desired outputs, and specification limitations as well as standard PFR and CSTR models as described in this section.

### Limitations

Because simulation requires reaction characteristics, parameters, and other information, it is important to conduct background research appropriate to the reaction of interest before beginning the actual simulation. If theoretical or empirical data do not exist for the reaction, it may be difficult or impossible to conduct a computer simulation (see Additional Options). Of course, the phase of the reaction must be known; unfortunately, however, HYSYS does not support solid phase modeling[1] and thus a different approach must be chosen.

## HYSYS Reactors[2][3][4]

In general, the user will attach a defined reaction set, generated as described above, to each reactor. This allows precise coordination of reactions that may be occurring in different units in the entire process.

### Plug Flow Reactor (PFR)

Plug Flow Reactors are tubular reactors that assume perfect radial mixing and approximate zero axial dispersion. A PFR is used primarily for gas phase reactions. HYSYS PFRs can utilize kinetic, equilibrium, and heterogenous catalysis reaction types. The user must define an inlet streams and an outlet stream; like most HYSYS units, multiple streams can enter the same unit. An optional energy stream can be specified to either provide or remove heat; if no stream is specified, HYSYS assumes that the unit operates adiabatically. However, depending on user specifications, HYSYS can determine required energy for the specified operation.

#### Sub-volume Integration

The HYSYS PFR divides the unit into sub-volumes based on total length where calculations occur throughout the PFR. The default number of sub-volumes is 20, but this number can be specified by the user. Of course, a higher number of sub-volumes will generally lead to a more accurate simulation but may be unnecessary given the operation or limitations due to time and computation capacity. Properties of unresolved sub-volumes can be user-specified using the "Minimum Step Fraction" and "Minimum Step Length" inputs.

After convergence, the user can view various graphs of process variable changes throughout each sub-volume.

#### Unique Parameters

The user must define physical properties of the reactor such as volume, cross sectional area, and length. Additionally, the program provides the option to define a number of tubes included in the unit. The specified length will encompass all tubes.

Pressure drop through the PFR can be defined by the user, approximated as zero, or left for HYSYS to calculate. User-defined pressure drops can be useful in accordance with the process as a whole but a zero approximation can serve for initial simulations if a pressure drop is not know. HYSYS will calculate using the Ergun equation.

A void fraction must be specified with unity referring to zero reactor packing. If a value other than unity is specified, the user must input data for the packing. Note that this data has a purely physical relationship with the system such as mean particle size, solid density, solid heat capacity, etc. and does not relate the the chemical reaction occurring in the unit. If the PFR is using a reaction set with a Heterogeneous Catalytic Reaction, that information will be specified in the reaction itself.

## Simulation

### Degrees of Freedom[5][6]

A degree of freedom analysis will assist in reaching a state of convergence for the reactor and downstream units. For a reactor,

$N_{dof}=N_{unknowns}+N_{reactions}-N_{balances}$

in which the number of degrees of freedom is expressed as the number of unknown variables plus the number of reactions occurring minus the number of material balances able to be performed on the system. In order for the simulation to converge, the user must specify as many variables as existing degrees of freedom. The simulation will then calculate unspecified variables.

## References

1. ^ AspenTech, "FAQ: Solids Modeling in AspenPlus", 2014
2. ^ G.P. Towler, R. Sinnott, Chemical Engineering Design: Principles, Practice and Economics of Plant and Process Design. p.186-194, Elsevier (2012).
3. ^ AspenTech. HYSYS 2005.2 Simulation Basis. Chapter 9 (2005).
4. ^ Rice University Chemical Engineering Department, "Reactions in HYSYS"
5. ^ R.M. Felder, R.W. Rousseau, Elementary Principles of Chemical Processes. 3rd edition, Wiley (2005).
6. ^ "Introduction to Chemical Engineering Processes: Degree of Freedom Analysis on Reacting Systems"