
This lecture shows how to start a new Aspen HYSYS case, import an assay to create a fluid package, select Peng-robinson for refinery hydrocarbon modeling, and rename the petroleum package.
Define a petroleum assay manually in Aspen HYSYS by entering 17 distillation cuts with initial and final boiling points, converting to SI, and specifying API density, sulfur content, and yields.
Import a petroleum assay from a file or library in Aspen HYSYS, choosing csv, and review conventional characterization with density, sulfur content, viscosity, and Watson factor.
Import a petroleum assay from the embedded library to attach to a crude material stream, then enter temperature, pressure, and molar flow in the simulation environment.
Learn to set up a petroleum assay stream analysis in Aspen HYSYS, view boiling curves and true boiling point data from ASTM D86, and add API and pour point information.
Distillation Column, Inlet, Outlet, Degree of Freedom, Converge
Atmospheric Gas Oil Side Stripper and Pump Around
Diesel Side Stripper and Pump Around
Kerosene Side Stripper and Pump Around
Learn how to implement trim duty in an atmospheric distillation column using an energy stream to dynamically adjust reboiler duty and column operating conditions in Aspen HYSYS.
Controlling the quality of Naphtha and Kerosene instead of the quantity produced.
Controlling Diesel and AGO quality by setting a cut point instead of fixing the flow rate
Model a vacuum distillation column fed from atmospheric residue, heated by a vacuum heater, with steam and pump around reflux, producing light and heavy vacuum gas oil under pressure profile.
Converge vacuum column by setting overhead rate, light and heavy vacuum gas oil rates, and a 2600 kg/h draw from vacuum overhead; resolve two liquid checks in the solver.
Implement a second bumper round in the vacuum column to handle heavy and light vacuum gas oil, adjusting flow rate and duty within side operation settings.
Model a fluidized catalytic cracking reactor using an Aspen HYSYS FCC template, defining the feed via petroleum assay, and configuring the riser, reactor, and regenerator in simulation.
Import vacuum gas oil as the FCC feed from the library, configure essay lumps, and set top and bottom cut points, then review feed properties before defining the catalyst.
Import the FCC catalyst from the library and Excel sheet, set 100% weight fraction for a single zeolite–alumina–rare earths catalyst, and configure constant equilibrium catalyst metals in Aspen HYSYS.
Set the FCC operation by defining feed flow, temperature, and pressure in the riser, specify steam and regenerator conditions, then review yields and heat balance.
Create a hydrocracker template in Aspen HYSYS, configure two reactors with two and three catalyst bits, add a high-pressure separator, and set calibration options for future integration.
Define a component list and the float package for the hydrocracker template. See how the hcr fluid package uses base components and abbreviations such as C6 to model feeds.
Identify and set hydrocracker feed conditions—volumetric flow, temperature, and pressure—and configure reactor feeds, recycle gas loops, purge, and product heater specifications for a steady simulation.
Learn to calibrate the hydrocracker in Aspen HYSYS using calibration factors, input operation measurements, feed data, and product specifications, and interpret calibration results from the worksheet and linked Excel sheet.
Set up calibration parameters and objective function for a hydrocracker in Aspen HYSYS, define bounds and initial values, run pre-calibration, review results, and save calibration factors for simulation.
Push calibration data into the hydrocracker simulation, activate the reactor solver, and review hydrocracking results and yields. Save the hydrocracker as a template and integrate it into a refinery model covering desalter, distillation, and heavy vacuum gas oil feed.
Welcome to the Advanced Refinery Process Modeling Using Aspen HYSYS. This comprehensive program is designed for professionals and students seeking to deepen their understanding of refinery process simulation and optimization using one of the industry’s leading software tools, Aspen HYSYS.
In this course, participants will engage in hands-on simulation exercises that cover a wide range of essential refinery processes. The curriculum includes the following key modules:
Petroleum Assay Simulation:
Learn how to utilize fluid packages and explore various methods to input petroleum assay data, including manual entry, extraction from the assay library, and stream analysis.
Atmospheric Distillation:
Gain insights into the operation of atmospheric distillation columns, including the design and function of refluxed absorbers. Participants will also examine side operations such as pump-arounds and side strippers, as well as the determination of cut points and trim energy optimization.
Vacuum Distillation:
Delve into vacuum distillation processes, focusing on column design, side operations, and the principles of heat integration to enhance efficiency.
Fluid Catalytic Cracking (FCC):
Explore the FCC template, including feed, lump model, catalyst selection, and operational conditions. This module emphasizes the importance of accurate modeling for optimizing catalyst performance and refinery yields.
Hydrocracking Process Simulation:
Introduce the hydrocracking (HCR) template and engage in simulations that illustrate the hydrocracking process. Participants will learn about calibration techniques to ensure model accuracy and reliability.
Throughout the course, participants will engage in practical exercises and case studies that reinforce theoretical concepts and enhance software proficiency. By the end of this course, you will be equipped with the skills necessary to model complex refinery processes effectively, optimize operations, and contribute to the overall efficiency and sustainability of refinery systems.