Simulation software for chemical engineering Ethene or Ethylene (C2H4) reacts with water at high temperatures to yield ethyl alcohol or ethanol C2H6O. Ethanol is produced through the direct hydration of ethylene by reacting a mixture of ethylene and water in the vapor phase over a supported sesqui-phosphoric acid catalyst. The preferred

This video is an introduction to using Aspen Simulation with a beginner-friendly approach. It focuses on the process of hydrating ethylene to form ethanol, providing a step-by-step guide for beginners to understand and utilize Aspen Simulation effectively.

Producing green hydrogen (H2) from water (H2O) through alkaline electrolysis, which results in the storage of hydrogen as ammonia (NH3). Discover the environmentally friendly method of generating hydrogen and storing it efficiently for future use.

The process of producing green hydrogen using water electrolysis, where water (H2O) is split into hydrogen (H2) and oxygen (O2). The tutorial showcases the use of Aspen Hysis V12.1 software to model and analyze the electrolysis process for efficient hydrogen production.

This video discusses the carbonylation of Dimethyl Ether (DME) to produce Methyl Acetate using ASPEN PLUS HYSIS simulation software and the Peng-Robinson (PR) and Soave-Redlich-Kwong (SRK) equations of state. The process involves an optimal temperature range of 180-200°C, a balanced chemical equation (CO + Dimethyl Ether ⟶ Methyl Acetate), and highlights the benefits of the carbonylation process, such as environmental friendliness, energy efficiency, versatility, and the utilization of renewable feedstock. By leveraging these advantages, the carbonylation process proves to be a valuable industrial route for producing Methyl Acetate.

PFR Reactor Design. Volume, Catalytic Weight, calculations Reactor Sizing - Volume Calculation Volume will be calculated using three different equations Option 1: V_(Volume of Catalyst for 1 tube)=(Mass of Catalyst )/(Density of catalyst ) Option 2: V_PFR=F_A0 ∫X dX/(-r_A ) | FA0 (dX )/dV=-r_A Option 3: V_reactor=(π D_s^2 L_tubes)/4+(4π(D_S/2)^2)/3 Summarized equations: 1. w=F_A0 ∫2 (X=0) X(1/(k((F_A0 (1-X))/(F_T0-2F_A0 X) P) ((F_B0-3F_A0 X)/(F_T0-2F_A0 X) P)^2-((2F_A0 X)/(F_T0-2F_A0 X) P)^3 1/k_C ) dX ------Equation 1 2.(dP_r)/d_w = β_0/(A_C (1-∅) P_C )(T/T_0 )(P_0/P)((F_T0-2XF_A0)/F_T0 )---------------Equation 2 3.T=T_0+(X[-∆H_RX (T_R )])/C_PA -----------Equation 3 Calculate W, P, T, rA, V using ODE Then solve for Volume: V_(Volume of Catalyst for 1 tube)=(Mass of Catalyst )/(Density of catalyst)

This video tutorial focuses on Kinetic Reactor Design using Aspen Hysis Plus V1.2 for the ammonia synthesis process. The tutorial demonstrates how to model and analyze the kinetics of the ammonia synthesis reaction using Aspen Hysis software.

This Aspen simulation tutorial focuses on designing a refrigeration cycle using carbon dioxide to cool water. Learn how to model and analyze the refrigeration process using Aspen software, specifically focusing on the use of carbon dioxide as the working fluid to achieve efficient cooling of water. Explore the different components of the refrigeration cycle, such as compressors, condensers, evaporators, and expansion valves, and understand how to optimize the cycle for maximum efficiency and performance. Join this tutorial to gain valuable insights into the Aspen simulation capabilities for designing innovative and sustainable refrigeration systems using carbon dioxide as the cooling agent.