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CHEM ENG LAB • CONSULTING PRACTICE

ENG. ANDREW OMWENGA

Chemical & Process Simulation Engineer • Thermodynamic Specialist

DOCUMENT REF: AEO-REP-09-2026
DATE: September 18, 2026
STATUS: CLIENT APPROVED / PRODUCTION READY
CLASSIFICATION: TECHNICAL AUDIT & MODELING REPORT
PROJECT TITLE & SIMULATION SCOPE:

Multinational Brewery Flue Gas Condensing Economizer System

Section 1.0 — Simulation & Facility Metadata

Software PlatformAspen HYSYS & Aspen EDR
Fluid PackagePeng-Robinson & ASME Steam
Industry SectorChemical Engineering
Location BenchmarkIndustrial Process Plant

Section 2.0 — Executive Summary

Industrial boiler flue gas condensing heat recovery system installed on three 15 t/h steam boilers at a commercial brewing facility, capturing waste heat and saving 8 million liters of water annually while cutting natural gas consumption by 16%.

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

Section 3.0 — Problem Statement & Operating Bottlenecks

Brewing operations require intensive steam for wort boiling, mash tun heating, pasteurizing, and bottle washing. The facility's steam boilers discharged flue gas at 195 °C directly to atmosphere, resulting in severe sensible and latent heat loss while drawing substantial freshwater for boiler make-up and pasteurization.

Section 4.0 — Objectives & Rigorous Simulation Methodology

1. Model boiler combustion flue gas condensation in Aspen HYSYS. 2. Size a two-stage direct-contact condensing economizer and indirect plate heat recovery train in Aspen EDR. 3. Reclaim condensed water vapor to offset site water utility costs. 4. Achieve simple payback under 3.5 years with guaranteed CO2 abatement.

Thermodynamic combustion and condensation modeling in Aspen HYSYS. Flue gas cooled from 195 °C to 38 °C, extracting both sensible heat and latent heat of moisture condensation into incoming process water loops.

Section 5.0 — Simulation Results & Thermodynamic Findings

SIMULATION & ENGINEERING RESULTS: - Boiler Fuel Reduction: 16.2% natural gas savings - Annual CO2 Reduction: 1,820 metric tons CO2 / year - Water Conservation: 8.2 million liters/year reclaimed condensate used for utility washdown - Payback Period: 3.2 years on turnkey project basis.

The two-stage condensing system preheats boiler feed water to 85 °C and pasteurization water to 68 °C simultaneously. The reclaimed condensate is neutralized and recycled for utility cooling tower make-up, delivering significant dual-utility (gas + water) savings.

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:

Flue gas acid dew point requires duplex stainless steel materials for corrosion prevention.

Future Digital Twin Integration:

Integration with CO2 recovery liquefaction chillers.

Section 8.0 — Consultant Conclusion & Verification Sign-off

Condensing economizers deliver deep decarbonization and water resilience for modern breweries, converting chimney waste into high-grade process heat.

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.