kWhScanIntegrated energy audit case library

Dairy processing integrated-energy audit example

Pasteurization, refrigeration, CIP hot water and cold storage diagnosed as one dairy energy system.

This case shows how a dairy processing facility should be reviewed from the process boundary first: raw milk cooling, pasteurization, product cooling, chilled storage, CIP hot water, boilers, compressed air and electrical demand.

  • Starts from dairy process operations before estimating savings.
  • Separates refrigeration electricity, thermal fuel reduction and heat-recovery offsets.
  • Protects the sanitary boundary for CIP and pasteurization temperature validation.

Process boundary first

Dairy energy opportunities come from heating and cooling the same product stream.

A dairy case cannot be treated as a generic refrigeration or boiler calculation. Pasteurization regeneration, product cooling, CIP hot water, cold storage and sanitary operation define what can be saved and what must be validated on site.

01Raw milk reception and pre-cooling

Milk temperature, receiving schedule and storage tanks establish refrigeration base load before production starts.

02Standardization, homogenization and heat treatment

Pasteurization and plate heat-exchanger regeneration determine both hot utility demand and downstream cooling load.

03Fermentation, blending and product cooling

Yogurt or fresh dairy batches can add temperature-control windows that interact with refrigeration staging.

04Filling, packaging and compressed air

Valves, instruments, packaging and filling air create a secondary compressed-air opportunity with reliability constraints.

05Chilled storage and cold chain

Cold-room temperature, doors, defrost and storage turnover keep refrigeration running outside production hours.

06CIP cleaning and hot-water cycles

CIP hot-water timing and temperature cap how much condenser or compressor heat can be reused.

Energy-flow map

The report keeps refrigeration, heat recovery and sanitary hot water separate.

The plant may need heat and cooling in the same production window. The report separates physical electricity savings, fuel reduction, avoided heat utility and demand-charge effects before showing the project total.

Dairy process boundary Milk reception, pasteurization, CIP, cooling and packaging

Product safety and cold-chain quality define which energy measures are acceptable.

Refrigeration Product cooling and chilled storage

Evaporating temperature, condenser control, cold-room doors and low-load sequencing drive electricity savings.

Pasteurization and CIP heat Hot water, steam and regeneration

Plate heat-exchanger effectiveness and CIP hot-water demand set the thermal target gap.

Boiler / hot-water system Fuel input and return conditions

Combustion, return temperature, condensate or hot-water loop losses remain thermal-side measures.

Compressed air Valves, instruments and packaging

Pressure, leakage and dryer losses are reviewed as secondary electricity measures.

Electrical demand Coincident refrigeration, pumps, packaging and CIP

Peak coordination is shown separately from kWh reduction.

Heat recovery cap Sanitary isolated preheating only

Recovered heat can preheat utility water only within the validated sanitary boundary.

Diagnosis result structure

What the dairy workflow produces.

The workbench maps the dairy process into the same pre-audit report skeleton used across KWH Scan: baseline, target gap, equipment, controls, distribution, multi-energy boundary, measure priority and M&V.

Measure group Why it matters in dairy Energy boundary Data to improve confidence
Refrigeration control and cold-room operation

Product cooling and chilled storage often continue beyond packaging hours.

Electricity saving from refrigeration controls and distribution losses.

Refrigeration trend data, cold-room temperature and door/defrost logs.

Pasteurizer regeneration and thermal recovery

Heating and cooling the same product stream makes regeneration performance critical.

Fuel reduction and cooling-load interaction shown with overlap control.

Pasteurizer temperatures, flow, regeneration approach and heat-source data.

CIP hot-water and condenser heat recovery

CIP creates concentrated hot-water demand windows that can use recovered heat.

Separate thermal offset capped by actual hot-water preheat demand.

CIP schedule, hot-water volume, temperature and utility loop design.

Boiler, hot-water loop and distribution losses

Combustion, return temperature, standby and pipe losses affect process heat cost.

Fuel-side savings, not mixed with refrigeration electricity.

Boiler efficiency, stack temperature, return temperature and operating logs.

Compressed air pressure and leakage review

Valves, filling, packaging and instruments need reliable dry air but usually not excessive pressure.

Secondary electricity saving with reliability and air-quality constraints.

Station power, pressure trend, dryer type and leakage survey.

Evidence basis

Public references support the process-energy boundary.

The page does not rely on a named customer logo. It exposes the engineering basis: public dairy energy references, equipment behavior, report calculations and user-replaceable site values.

DOE / LBNL dairy processing energy guide

Used to support the presence of material refrigeration, process heat, motor and utility opportunities in dairy facilities.

Open public reference
Engineering estimate labels

Where the public page shows opportunity logic, the workbench report labels confidence and lists the data needed to improve precision.

User data replaces the public example

The workflow is designed for utility bills, operating hours, equipment data and optional trend logs from the user's own site.

Use the dairy workflow

Open the full dairy processing case in the diagnosis workbench.

Use this case as the dairy processing audit starting point.

Start from the dairy processing workflow, then replace the values with your own plant data and unlock the full report if the result is useful.