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If you are looking for a program during which you want to see your dramatic progress in process engineering in a short period of time , the course is for you. Throughout this program you become professional in various subjects, standards, and softwares. Upon the completion of the program, you will be able to perform many process engineering-related tasks during engineering phase. The advantages of the course are as follows:
1.You will learn all packages of EIEPD in just one package.
2.It is more cost-effective.
3.All parts of engineering are connected.
4.Six-month monitoring of your progress and your mistakes.
The “From Operation to Design” Program could be regarded from two perspectives:
The course instruction lasts for 6 months but due to some possible time break needed by participants, the course might last for 7 months but in no way, it would not be extended. We know you work and after the work hours you have to attend the classes. That is the reason we give recordings and break time to review what you have learned in the classes or if you could not focus. So don’t worry and be relaxed.
Here is the content:
Part 1: Process Plant Design
Part 2: PFD and P&ID Development using Auto-cad P&ID
Part 3: Advanced Control
Part 4: Interlock Diagram Development using Auto-cad
Part 5: PSV
Part 6: Heat Exchanger Sizing
Part 7: Separator Sizing
Part 8: Equipment and Process Units Start-ups and Normal Operation
The “From Operation to Design” Program could be regarded from two perspectives:
The course instruction lasts for 6 months but due to some possible time break needed by participants, the course might last for 7 months but in no way, it would not be extended. We know you work and after the work hours you have to attend the classes. That is the reason we give recordings and break time to review what you have learned in the classes or if you could not focus. So don’t worry and be relaxed.
Here is the content:
Part 1: Process Plant Design
Part 2: PFD and P&ID Development using Auto-cad P&ID
Part 3: Advanced Control
Part 4: Interlock Diagram Development using Auto-cad
Part 5: PSV
Part 6: Heat Exchanger Sizing
Part 7: Separator Sizing
Part 8: Equipment and Process Units Start-ups and Normal Operation
The “From Operation to Design” Program could be regarded from two perspectives:
Here is the content:
Part 1: Process Plant Design
Part 2: Detailed Engineering Design
Part 3: Material Selection
Part 4: Aspen Hysys
Part 5: PSV Sizing and Flare Package Design
Part 6: Aspen Plus
Part 7: Advanced Control
The detail of each part is stated in next tabs:
Part 1: Process Plant Design
Session 1: Process design criteria
Session 2: Practices
Session 3: PFD development
Session 4: PFD development for process units
Session 5: PFD development for process units-continued
Session 6: Review
Session 7: P&ID development Intro-Gas station
Session 8: P&ID development for process units
Session 9: P&ID development for utilities units
Session10: Overview of process safety documents
Session11: PSV and flare header summary
Session12: Flare package design
Session13: Process emergency description and interlock diagram
Session14: Review of your month project
Part 2: Detailed Engineering Design
Session 15: Horizontal Heat-Exchanger data-sheet development
Session 16: Vertical Heat-Exchanger data-sheet development
Session 17: Air-Cooler data-sheet development
Session 18: PSV data-sheet development
Session 19: Tour on API-521
Session 20: Tour on API-520
Session 21: Sizing and Designing of Horizontal Separator
Session 22: Separator Sizing in Aspen Hysys
Session 23: Sizing and Designing of Vertical Separator with Mist Eliminator
Session 24: Sizing and Designing of Compressor Package Separator
Session 25: Knock-Out Drum Sizing
Part 3: Material Selection
Session 26: General Criteria for Material Selection
Session 27: Nace Overview
Session 28: Material Selection for Utilities
Session 29: Material Selection for Equipment
Session 30: Corrosion Types, Material Categories and Material Specification
Session 31: Special Processes
Part 4: Aspen Hysys
Session 32: Introduction
Session 33: Fluid Package Selection
Session 34: Separator simulation
Session 35: Pumps simulation
Session 36: Compressor simulation
Session 37: Turbine simulation
Session 38: Line Sizing
Session 39: Control valve simulation
Session 40: Simple heater
Session 41: Shell and tube heat exchanger
Session 42: Air coolers
Session 43: Conversion reactor simulation
Session 44: Equilibrium reactor simulation
Session 45: Gibbs reactor simulation
Session 46: PFR reactor simulation
Session 47: Distillation column using short-cut approach
Session 48: Distillation column using rigorous approach
Session 49: Absorber simulation
Session 50: Line sizing manager
Session 51: Vessel sizing
Session 52: Distillation-column sizing
Session 53: Relief load calculation and PSV sizing
Part 5: PSV Sizing
Session 54: Scenarios – EIEPD Equipment-Based Approach
Session 55: EIEPD Methodology-Based Relief Load Calculation
Session 56: Individual Overpressure Causes and Their Relieving Rates – Based on API-521
Session 57: Pressure Relief Device Types and Orifice Sizing
Session 58: Orifice Area Sizing Examples
Session 59: Construction, installation and material selection notes
Session 60: Flare Header Sizing
Part 6: Aspen Plus
Session 61: Property Set-up in Aspen Plus+
Session 62: Binary Analysis in Aspen Plus+
Session 63: Pressure Change in Aspen Plus+
Session 64: Separation and Mixing in Aspen Plus+
Session 65: Heat Exchanger Design and Simulation in Aspen Plus+
Session 66: Distillation Column Design and Simulation in Aspen Plus+
Session 67: Utilities in Aspen Plus+
Session 68: Solid Process Modeling in Aspen Plus+
Session 69: Electrolytes System Simulation in Aspen Plus+
Session 70: Pharmaceutical Application Simulation in Aspen Plus+
Part 7: Advanced Control
Session 71: Introductory session
Session 72: Flow controlling loops [FIC]
Session 73: Pressure controlling loops [PIC]
Session 74: Level controlling loops [LIC]
Session 75: Temperature controlling loops [TIC]
Session 76: Split-range for combined FICs and LICs
Session 77: Split-range for deaerator pressure control
Session 78: LIC-FIC cascade control
Session 79: Combined cascade and split-range
Session 80: FY, LY, PY Calculators
After over 140 hr. of training, you have gained comprehensive knowledge about the following categories:
1.Project Documents
You are able to prepare and develop the following documents
2.Standards, Codes, and References
3.Software
You are able to use the following software easily:
What you will receive throughout this comprehensive course
4.Materials
5.The Gift Packages
you will receive the following files free of charge:
6.References
All references will be provided.
Educational Institute for
Equipment and Process Design
We at EIEPD show you the way to become professional in oil and gas industry
Educational Institute for
Equipment and Process Design
We at EIEPD show you the way to become professional in oil and gas industry
