Learning objectives
How to simulate vacuum distillation column to treat atmospheric unit residue.
Problem Statement
Additional steam is injected into the Vacuum Feed Heater to increase
velocity & minimize coke formation within the heater
Part 4
Learning objectives
How to simulate vacuum distillation column to treat atmospheric unit residue.
Problem Statement
Additional steam is injected into the Vacuum Feed Heater to increase
velocity & minimize coke formation within the heater
learning Objective Part 3
How to simulation debutanizer column to stabilize the Naphtha and to recover LPG.
Simulation of atmospheric distillation column
How to setup crude distillation unit with three side strippers
and three pump arounds in HYSYS.
Learning objectives
• How to generate petroleum assay from Light crude, Medium
crude and Heavy crude to have mix crude for atmospheric distillation.
• Preheat train for atmospheric distillation.
Problem Statement Crude Oil Feed:
100°F, 300 Psig, 101,000 bpd ,Preheater-1 outlet: 260°F, 294 Psig ,Desalter outlet: 260°F, 294
psig , 500 bpd water , Preheat-2 outlet: 450°F, 260 psig
learning objective
How to build dynamic simulation.
Interaction between set points and process variables
It is an extension of steady-state whereby time-dependence
is built into the models i.e. accumulation of mass and energy.
Control of real processes are possible.
The calculations are more complex and time consuming.
Interaction between set points and process variables
Heat Exchanger Hot water at 500°C and 2000psig is
used to heat cold stream of water in a shell and
tube heat exchanger. The inlet temperature and
pressure of the cold stream is 50°C and 260psig,
respectively. The outlet temperature of the cold and hot
streams are 300°c and 360°C, if the flow rate of the
hot stream is 100kg/h,determine the flow rate of the
cold stream passing throughout the exchanger.
Learning Objective > How to simulate a pump unit in Aspen HYSYS to find out actual power required to pump the fluid. > Pum...