Start modeling your first Chemical Process with Aspen HYSYS

Model a steady-state chemical process in Aspen HYSYS to separate methane from hydrocarbon feed, distill with a partial condenser and reboiler, and simulate CO2 combustion with mass and energy balances.

Explore the landing page in Aspen HYSYS and learn the physical property environment, including components, fluid packages, oil manager, and petroleum assays for crude oil modeling.

Explore the simulation environment in Aspen HYSYS. Learn unit operation blocks, their inputs, and how to model processes such as distillation columns by connecting real-life data to the digital model.

Explore flowsheet in Aspen HYSYS simulation environment. Learn to add material and energy streams, connect unit operations, and customize the flow chart and model pilot for efficient process modeling.

Input and define data for the profit and air streams in Aspen HYSYS, including temperature, pressure, molar flow, and composition; normalize data as needed and add CO2, oxygen, and nitrogen.

Learn to add, set up, and connect unit operations in a simulation using Aspen HYSYS. Explore control variables, transfer functions, and common equipment like heat exchangers, reactors, and distillation blocks.

Model a steady-state Aspen HYSYS process to separate methane from a three-hydrocarbon feed, combust methane in a reactor, and recover liquids via a distillation column with partial condenser and reboiler.

Learn to add a chemical reactor and build reaction sets in Aspen HYSYS, balancing methane plus oxygen to CO2 and water, and use free energy to estimate equilibrium constants.

Set up a distillation column in Aspen HYSYS with 20 stages, feed at stage 10, a partial condenser, and 2.5 molar reflux; maintain gas-to-distillate ratio of 1:10 and verify connections.

Set up the pump to move the bottoms liquid and pressurize to 150, then adjust delta pressure and pressure ratio for the Aspen HYSYS simulation.

Learn to retrieve and verify stream results in Aspen HYSYS by viewing temperature, composition, flow rates, and thermodynamic properties. See how to check condenser duty and validate temperatures from streams.

Explore case studies that test how temperature, distillation column size, reflux ratio, distillate to gas ratio, reactor conditions, oxygen or air, and pressure impact liquid product specifications in Aspen HYSYS.

Explore case studies to optimize your process by adjusting feed composition, flow rate, chiller temperature, distillate-to-gas ratio, and total column stages to balance cost, purity, and environmental goals.

In case study C, adjust the distillate to gas ratio in an Aspen HYSYS model, observing effects on methane purity, product flow, and convergence toward process specifications.

Explore how changing distillation stages from 20 to 30 affects mass transfer and vapor-liquid interaction, purity, and flow rate, weighing energy and equipment costs against product quality in Aspen HYSYS.

Learn to model chemical processes in Aspen HYSYS, covering unit operations such as reaction, separators, distillation, and heat exchange, and to set up physical properties and streams for analysis.

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