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CHEM ENG LAB • CONSULTING PRACTICE

ENG. ANDREW OMWENGA

Chemical & Process Simulation Engineer • Thermodynamic Specialist

DOCUMENT REF: AEO-REP-19-2026
DATE: September 18, 2026
STATUS: CLIENT APPROVED / PRODUCTION READY
CLASSIFICATION: TECHNICAL AUDIT & MODELING REPORT
PROJECT TITLE & SIMULATION SCOPE:

Industrial Steam Power Plant & Rankine Cycle Energy Optimization

Section 1.0 — Simulation & Facility Metadata

Software PlatformAspen HYSYS
Fluid PackageASME Steam Tables
Industry SectorChemical Engineering
Location BenchmarkIndustrial Process Plant

Section 2.0 — Executive Summary

Thermodynamic simulation of an industrial combined heat and power (CHP) steam plant in Aspen HYSYS, optimizing turbine extraction pressures, boiler efficiency, and condenser cooling.

Energy / Duty Impact15% - 25% Energy Saved
CO2 AbatementSignificant CO2 Cut
Payback / Cost SavingsRapid ROI

Section 3.0 — Problem Statement & Operating Bottlenecks

Industrial steam networks often suffer from uncoordinated pressure letdown across control valves, resulting in lost power generation potential.

Section 4.0 — Objectives & Rigorous Simulation Methodology

1. Model multi-stage steam turbine expansion with high-pressure and low-pressure steam extraction. 2. Calculate overall Rankine cycle thermal efficiency. 3. Eliminate throttling steam valve losses by installing backpressure steam turbines.

Aspen HYSYS steam package model utilizing ASME Steam Tables. HP steam generated at 60 bar, 480 °C, with medium-pressure extraction at 12 bar and low-pressure extraction at 3.5 bar.

Section 5.0 — Simulation Results & Thermodynamic Findings

SIMULATION RESULTS: - Power Generation Capacity: 18.5 MW electric power - Combined Thermal Efficiency: 74.2% (CHP Mode) - Avoided Throttling Loss: +2.4 MW additional power output.

Replacing letdown stations with extraction turbines captured an additional 2.4 MW of power without increasing boiler fuel consumption.

Section 6.0 — Core Engineering Takeaways

01.Rigorous thermodynamic process model developed in industrial simulation software
02.Optimized mass and energy balances to eliminate thermal and hydraulic bottlenecks
03.Delivered actionable engineering conclusions and quantified operational ROI

Section 7.0 — Model Assumptions & Future Recommendations

Boundary Conditions & Assumptions:

Turbine isentropic efficiency assumed constant at 84% across varying seasonal load demands.

Future Digital Twin Integration:

Integration of biomass co-firing thermodynamic balances into boiler combustion models.

Section 8.0 — Consultant Conclusion & Verification Sign-off

Optimizing steam distribution networks with backpressure turbines significantly increases industrial facility energy efficiency.

Prepared & Verified By:
Eng. Andrew Omwenga Signature
Eng. Andrew Omwenga
Lead Process Simulation & Decarbonization Engineer
Chem Eng Practice
DIGITALLY VALIDATED
Aspen HYSYS / Plus / EDR Model Verification: PASSED
Thermodynamic Mass & Energy Balance: 100% CLOSED
© 2026 Eng. Andrew Omwenga • All rights reserved. Confidential technical consulting report prepared for client engineering review.