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Live Online Class Intermediate

Chemical Engineering Basics

4(14)
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$ 250
30 hrs
Next month
English
185 views
Enggenious (SAN Techno Mentors)
Enggenious (SAN Techno Mentors)
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  • Session recordings included
  • Interactive Video Lessons
  • Learn from Industry Expert

Why enroll

Chemical Engineering Basics (Unit Operations, process equipments: boiler, chiller, heat exchanger, distillation column; process plants and automation)

Upon Completion of this course the participant will be able to Understand basic process concepts behind the equipment Learn about fundamental design principles Learn about the key technical specification and selection aspects Understand the various of types and categories of equipment based on same or similar principle depending on the application Learn about the instrumentation commonly deployed with the equipment Develop an understanding about the control loops and strategies used Develop familiarity about the requirement analysis for application development for an automation system.

Is this course for you?

You should take this if

  • You work in Chemical or Industrial Automation
  • You're a Chemical & Process / Instrumentation Engineering professional
  • You have some foundational knowledge in the subject
  • You want to build skills in Artificial Intelligent, Control Systems

You should skip if

  • You're looking for an introductory overview course
  • You need a different specialisation outside Chemical & Process
  • You need fully self-paced, on-demand content

Course details

A variety of common process equipment is used in the Chemical Process Industries (CPI) such as chemicals, petrochemicals and oil and gas industries. Some of the equipment is even used in other industries such as power, iron and steel and cement. Examples of such widely used process equipment include various types of heat exchangers – heaters, coolers, condensers, evaporators; fired heaters and boilers, cooling towers and chilling units as well as columns such as distillation and absorption columns and flow equipment such as compressors and pumps. Apart from process engineers and supervisors who would like to revise and learn practical aspects of these equipment, the course will be very useful for non process professionals with electrical, mechanical and instrumentation background and working in maintenance, projects, design and site installation and commissioning. The course covers the theory in brief, design aspects, process and service specifications, selection and application aspects of these equipment and operations in a practical manner. Special emphasis is given on the requirement and selection of instrumentation and control for these process equipments.

Course suitable for

Key topics covered

Module 1 - Evolution of process and equipment engineering Introduction to core chemical process engineering Equipment design and chemical engineering Unit Operations

Module 2 - Heaters, coolers, heat exchangers, evaporators Types, Processes, Specification, Selection Instrumentation and control Requirements Control Schemes

Module 3 - Boilers , Pumps Types, Processes, Specification, Selection Instrumentation and control Requirements Control Schemes

Module 4 - Cooling towers, chilling plants, and Compressors Types, Processes, Specification, Selection Instrumentation and control Requirements Control Schemes

Module 5 - Distillation and absorption columns Types, Processes, Specification, Selection Instrumentation and control Requirements Control Schemes

Opportunities that await you!

Career opportunities

Training details

This is a live course that has a scheduled start date.

Why people choose EveryEng

Industry-aligned courses, expert training, hands-on learning, recognized certifications, and job opportunities-all in a flexible and supportive environment.

$250

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Questions and Answers

A: A would still occur because the level instruments and dump valves don’t depend on the PSV being available. B would occur because the primary overpressure safeguard is bypassed and pressure rises unchecked. C can happen but it’s a secondary mechanical effect, not the main hazard path here. D is correct because PSV isolation never protects against fire exposure; that’s handled by fireproofing, depressurization, and layout.

A: A leads to missed failure modes because you’d ignore installed redundancy shown in the index. B would imply a function block that isn’t documented anywhere on the P&ID or logic drawings. C assumes a SIL architecture without any evidence of voting logic or safety function tagging. D is correct because the A/B designation plus a selector normally means one transmitter drives the loop at any given time.

A: A would give unstable flow and noise but not sustained high discharge pressure. B explains low flow but conflicts with the observed pressure and current. C fits the electrical symptom only and ignores the process indicators. D is correct because operation near shutoff increases head and often drives motor amps up.

A: A misapplies a stainless failure mode to carbon steel service. B requires a different chemistry and temperature window. C would show discrete pits tied to oxygen ingress rather than uniform loss. D is correct because wet CO₂ forms carbonic acid that aggressively attacks carbon steel.