To start either of these packages, be sure to look for the corresponding User Interface on the start menu.
#Aspen hysys tutorial plus
Normally undergraduate student projects will involve Aspen Plus or Aspen Properties. This package is available within Aspen Plus or Aspen Properties rather than via an external menu.īatchSep - Batch distillations. All of the phase equilibria and mixture property methods discussed on this site are accessible in either Aspen Plus or Aspen Properties.Īspen Polymers - Modeling of polymerization reactors and polymer thermodynamics. Incorporated into most other components, though it can be run as a stand-alone subset. Runs independent of Aspen Plus.Īspen Dynamics - Unsteady-state simulator.Īspen Plus - Steady-state process simulator.Īspen Properties - Modeling of properties and phase equilibria. Runs independent of Aspen Plus.Īspen Custom Modeler - A utility to permit the creation of user unit operations.Īspen Distil - Aspen's 'Conceptual Engineering Product' for planning for processing schemes. Briefly, here are the programs and capabilities:Īspen Adsim - Fixed bed adsorption for pressure swing adsorption, etc.Īspen Chromatography - Fixed bed adsorption, simulated moving bed chromatography. MSU has a variety of Aspen packages for different simulations. Some preliminary or 'back of the envelope' calculations are generally recommended. Usually, you must set the number of stages and see what type of separation results. This information could come from an approximate method, such as the McCabe-Thiele approach, general modeling of the T-x-y behavior, or residue curve maps.ĪSPEN cannot tell you how many stages to use for a given separation except in approximate cases using conceptual design. For instance, a user should have some idea of the column behavior before attempting to use ASPEN. Therefore, a solid understanding of the underlying chemical engineering principles is required to supply reasonable values of input parameters and to evaluate the suitability of the results obtained. It takes a design that the user supplies and simulates the performance of the process specified in that design. ASPEN can handle very complex processes, including multiple-column separation systems, chemical reactors, distillation of chemically reactive compounds, and even electrolyte solutions like mineral acids and sodium hydroxide solutions.ĪSPEN does not design the process. This accurate modeling of thermodynamic properties is particularly important in the separation of non-ideal mixtures, and ASPEN has a large data bases of regressed parameters. This information can then be used in an iterative fashion to optimize the design. Given a process design and an appropriate selection of thermodynamic models, ASPEN uses mathematical models to predict the performance of the process.
#Aspen hysys tutorial software
We will check if the pipe with 12, 14, and 16 NPS will adequate for this natural gas service.ASPEN is a process simulation software package widely used in industry. Selected schedule will depend on the pipe class specification defined by EPC company as agreed with the Oil and Gas company.įor now, let's assume that we use Standard (STD) schedule for the pipe. As mention above, ID could be calculated based on the pipe NPS and pipe schedule. Here, we have to specify the Inside Diameter (ID) of the piping system. Then, click on the MATERIAL STEAM → go to ATTACHMENT tab → ANALYSIS → create PIPE SIZING Analysis → choose PRESSURE DROP calculation type
Solution: The natural gas steam properties could be checked using Peng-Robinson fluid package in ASPEN HYSYS. More detail about pipe sizing criteria, please refer to this article. Typically, an EPC company will develop their own line sizing spreadsheet that include well-known pressure drop calculation method e.g. Please note that pressure drop calculation is based on HYSYS default pressure drop calculation for pipe sizing analysis option in equipment sizing. However, to get a rough picture and learn the philosophy of line sizing calculation, HYSYS could be used. (*) ASPEN HYSYS is not a specialize software for the line sizing calculation. The Oil and Gas Design criteria for vapor piping service is as follow:Ĭalculate the minimum required piping diameter for this service. Mass flowrate : 95000 kg/h Operating Pressure : 900 kPag Operating Temperature : 45 o C
Example problem: line sizing using ASPEN HYSYS (*) Natural gas with following composition