- APEGA P.Eng. · ID 209405
- B.Sc. Mechanical Engineering
- M.Eng.
- University of Alberta
Delivered $16M of static and rotary shutdown work. Mechanical engineering support for rotating and static equipment, frames and skids.
I’m Abdullah Abdullah, P.Eng. (APEGA ID 209405), with 7+ years as a mechanical engineer. I’ve coordinated up to 60 contractors and scoped projects from $100K to $4M. My focus: SolidWorks models, fabrication drawings, FEA and equipment reviews for Alberta plants and engineering firms.
What I deliver
Practical engineering for plant owners and engineering firms in Alberta.
SolidWorks 3D models & drawings
Parametric models and weldment frames for skids, supports and stands.
Fabrication packages
GAs, cut lists, base plate and weld details.
As-built drawings
After shutdowns and modifications, in SolidWorks or AutoCAD.
FEA & design checks
Finite element analysis in SolidWorks for equipment design and modifications.
Rotating & static equipment reviews
Pumps (API 610/676/685), exchangers, vessels; FFS to API 579.
Shutdown planning support
Scopes, work packages, MRQs; HAZOP, RCA, PSSR and MOC.
Engineering services for clients begin once an APEGA Permit to Practice is issued. Until then, I welcome enquiries and scoping conversations.
How I solve problems
The same four steps behind $16M of static and rotary shutdown work.
Understand the failure or need
Plant tours, root cause analysis, and the HAZOP and MOC context.
Model & analyse
SolidWorks 3D and FEA, checked against API, ASME and ABSA requirements.
Deliver fabrication-ready packages
Drawings, cut lists, scopes and MRQs your team can build and buy from.
Support execution
Shutdown planning, schedules and QA/QC, coordinating up to 60 contractors through commissioning.
Have a frame, skid or retrofit?
Tell me about it in about two minutes.
Projects: problem, fix, result
Every project below is from my own work, grouped by capability.
Rotating equipment
- Problem
- Kiln trunnions suffered a breakdown failure.
- What I did
- Replaced all of the kiln’s trunnions, then aligned the incinerator.
- Result
- $400K · done to preserve operations and asset health
- Problem
- The facility’s main induced draft fan needed a complete overhaul.
- What I did
- Overhauled the casing, bearings and motor, then commissioned the fan.
- Result
- $500K · fan overhauled and commissioned
- Problem
- Volatile organic waste fluids needed homogenizing in a tank.
- What I did
- Installed a tank agitator.
- Result
- $185K · agitator installed
Heat transfer & pressure equipment
- Problem
- The facility’s air compressors needed cooling and piping work.
- What I did
- Delivered two fin-fan heat exchangers, a pump skid and piping for the air compressors.
- Result
- $800K static shutdown scope delivered
- Problem
- Corrosive process fluids called for corrosion-resistant heat exchange.
- What I did
- Installed three titanium plate heat exchangers.
- Result
- $500K static shutdown scope delivered
- Problem
- Static equipment had to meet company standards and ABSA requirements.
- What I did
- Designed, sized and purchased shell and tube heat exchangers, pressure vessels, condenser pots and chemical dosing skids.
- Result
- Equipment specified to standard and ABSA requirements
Materials handling
- Problem
- The main shredder had to handle solid wastes, light metals and concrete.
- What I did
- Upgraded the main shredder.
- Result
- $900K rotary shutdown scope delivered
- Problem
- The incinerator’s feed system needed an upgrade.
- What I did
- Upgraded the entire hydraulic feed system: gates, rams and conveyors.
- Result
- $300K rotary shutdown scope delivered
- Problem
- An elevator critical to moving barrels and drums for incineration needed work.
- What I did
- Executed its mechanical overhaul.
- Result
- $70K · critical elevator overhauled
FEA & fitness-for-service
- Problem
- Pressure vessels needed integrity checks.
- What I did
- Ran FEA in SolidWorks and fitness-for-service analysis in INSPECT to API 579 and ASME VIII/IX.
- Result
- FEA and fitness-for-service analysis delivered
- Problem
- Rotating equipment had to meet API 610, 685 and 676.
- What I did
- Designed, sized and purchased canned hermetic, 13-stage VS6/VS7, centrifugal and PD dosing pumps.
- Result
- Pumps specified to API standards
- Problem
- A plant needed to keep running until its next outage.
- What I did
- Provided plant support and designed modifications.
- Result
- Modifications designed to sustain operations to the next outage
Shutdown execution
- Problem
- Five critical-path shutdown projects had to improve production efficiency and minimize downtime.
- What I did
- Conceptualized, planned, executed and commissioned them, running schedules, budgets and reporting for crews of up to 42.
- Result
- $3.3M across five critical-path shutdowns
- Problem
- Combustion air flow needed better monitoring and control.
- What I did
- Installed venturi meters (phase 1).
- Result
- $160K · phase 1 delivered
- Problem
- Power distribution to critical plant equipment needed inspection.
- What I did
- Inspected and maintained MCCs and switchgear.
- Result
- $53K · inspection and PM completed
Summaries use only publicly shared experience, never confidential information. Values are project values as stated in my work history.
Experience
- Senior Reliability Engineer (current)Jan 2025 – present
- Engineering Project Lead · industrial waste treatment facility, Western CanadaNov 2018 – Nov 2025
- Mechanical Design Engineer · contract assignment, global chemical manufacturerSep – Dec 2023
- Engineering Project Lead (co-op) · industrial treatment facility, Western CanadaMay – Sep 2018
- Research Engineer (co-op) · national research laboratoryMay – Sep 2016
Client and employer names withheld for confidentiality; references available on request.
Education
- B.Sc. Mechanical EngineeringUniversity of Alberta
- M.Eng.University of Alberta
Codes, standards & tools
- API 610 / 676 / 685
- API 579 FFS
- ASME VIII / IX
- ABSA
- SolidWorks (incl. FEA)
- AutoCAD
- INSPECT
- MATLAB / R