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Aspen Plus & Aspen EDRNRTL / Moist Air Psychrometrics

Dairy Spray Dryer Exhaust Heat Recovery & CIP Hot Water System

Flue gas and spray dryer exhaust condensing heat recovery system recovering 2.4 MW of low-grade thermal energy to generate continuous 80 °C Clean-In-Place (CIP) washdown and boiler feed preheating for a major dairy processing plant.

Dairy Spray Dryer Exhaust Heat Recovery & CIP Hot Water System

1. Project Overview & Context

Flue gas and spray dryer exhaust condensing heat recovery system recovering 2.4 MW of low-grade thermal energy to generate continuous 80 °C Clean-In-Place (CIP) washdown and boiler feed preheating for a major dairy processing plant.

2. Problem Statement

Dairy milk powder spray dryers discharge high volumes of warm, humid exhaust air (85–95 °C) laden with latent moisture and residual powder particulates. At the same time, the facility consumed heavy fuel oil and steam to heat 45 m³/h of fresh water for pasteurization and CIP sanitation loops, wasting over 20% of total site fuel input through boiler and dryer stacks.

3. Objectives

1. Model a direct-contact condensing economizer tower in Aspen Plus to capture both sensible and latent moisture heat from dryer exhaust. 2. Incorporate continuous particulate washdown nozzles to eliminate powder deposition. 3. Integrate heat recovery loop with site thermal storage to supply 80 °C washdown water across fluctuating shift cycles. 4. Quantify natural gas displacement, Scope 1 carbon abatement, and project simple payback.

4. Simulation Setup & Thermodynamic Selection

Software Environment
Aspen Plus & Aspen EDR
Property Method / EOS
NRTL / Moist Air Psychrometrics

Rigorous thermodynamic spray scrubber model in Aspen Plus with multi-component water-air psychrometrics. Coupled with Aspen EDR plate heat exchanger sizing to isolate process-contact wash water from exhaust gas condensate.

5. Process Flow & Reduction Chemistry

Rigorous thermodynamic spray scrubber model in Aspen Plus with multi-component water-air psychrometrics. Coupled with Aspen EDR plate heat exchanger sizing to isolate process-contact wash water from exhaust gas condensate.

6. Model Input Variables & Boundary Conditions

ParameterValueUnitsEngineering Source
Operating PressureVariablebarProcess Specification
Feed Flow RateNominalkg/hSimulation Balance

8. Results & Findings

SIMULATION & ENGINEERING RESULTS: - Continuous Thermal Recovery: 2.4 MWth across dryer exhaust streams - Natural Gas Displacement: 1.73 million m³ annually (-18.5% plant fuel spend) - Scope 1 CO2 Reduction: 3,300 metric tons CO2 / year - Hot Water Output: 45 m³/h delivered at 82 °C without boiler steam consumption - Financial Payback: 1.8 years based on $6.50/GJ fuel baseline.

9. Engineering Discussion & Trade-Off Analysis

By capturing the latent heat of water condensation within the spray dryer exhaust, the condensing heat recovery system dramatically outperforms standard dry economizers. The recovered heat satisfies 100% of the facility's daytime CIP sanitization duty, smoothing boiler firing loads and preventing thermal shock during shift changeovers.

10. Financial Impact & Decision-Support Platform

Economic feasibility evaluations assess capital expenditures, operational utility consumption, and payback thresholds to validate commercial viability.

11. Environmental Impact & Decarbonization Value

Significant reductions in carbon emissions and fuel waste achieved through rigorous process simulation and heat integration.

12. Model Limitations & Scope Boundaries

Requires 316L stainless steel metallurgy to tolerate acidic cleaning agent vapors and moisture condensation.

13. Engineering Conclusions

Condensing exhaust heat recovery delivers rapid financial returns and verified decarbonization for dairy and ingredient manufacturers without compromising sanitary process safety.

14. Future Development & Digital Twin Integration

Integration with Mechanical Vapor Recompression (MVR) for direct evaporator steam regeneration.

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