Inzonex ← Brewery heat-loss map Your savings

Inzonex Modular Insulation · Brewhouse

Brewery cooker

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Brewhouse vessel dome before insulation, with stack and access hatch Same vessel dome fitted with segmented Inzonex insulation BeforeBare metal AfterInzonex insulation
Removable dome insulation
Energy cost saving / year£13,831£50.00/MWh fuel
Heat retained / year260.0 MWhAt your selected operating hours
Emissions avoided / year51.2 t CO₂e185.0 kg CO₂e/MWh fuel
Modelled outer surface29.4 °CBelow the 45 °C design target

Estimate: 1 cooker · 39 m² · 95 °C bare surface · 6,600 operating hours/year.

Inzonex benefits

Less heat loss.
Easy access for inspection.

Inzonex removable insulation covers exposed brewery-cooker surfaces while keeping ingredient access, the manway and agitator connections available.

Less heat into the hall

39.4 kW less heat released from the covered surface, based on your inputs.

A cooler outer cover

29.4 °C calculated outer temperature with 50 mm insulation.

Open, inspect, refit

Remove the insulation section, inspect the equipment and refit it.

Access points stay usable

Keep ingredient access, the manway and agitator connections accessible. Leave vents, motor cooling and required clearances unobstructed.

For your operating conditions

Your savings

Enter the area to insulate, surface temperature and operating hours.

£13,831Energy saving / year260.0 MWh/yrHeat retained
Brewery cooker & operating hours
°C

Use the metal surface temperature, not the steam supply temperature.

Enter the area to insulate. Exclude surfaces already insulated.

units

For cookers with the same area and operating conditions.

h/yr

Set your annual operating hours.

Energy & CO₂
£/MWh
kg/MWh

kg CO₂e per MWh.

Per MWh of fuel. Natural gas is prefilled.

Calculation settings 50 mm · 25 °C air

Fuel saved = heat retained ÷ efficiency.

Natural-gas example: 94% efficiency and 185 kg CO₂e/MWh fuel, following the Cochran calculator. Calculation method.

Reference & method

What the numbers mean

Calculation inputs, formulas and limits.

Worked example

1 cooker · 39 m² · 95 °C · 6,600 h/yr
Bare heat loss
41.6 kW
Insulated heat loss
2.2 kW
Annual heat retained
260.0 MWh
Outer surface
29.4 °C

50 mm mineral wool · air 25 °C at 0.5 m/s · emissivity 0.90 bare / 0.85 cover. Starting area: 39 m²; bare surface: 95 °C. Area and temperature are editable. The dome is a shared brewhouse design illustration; confirm your vessel dimensions before ordering.

Annual example: 6,600 operating hours; natural gas at £50/MWh, 94% heat-supply efficiency and 185 kg CO₂e/MWh fuel. Price and hours are editable starting values. The efficiency and fuel factor follow our Cochran calculator. Price and factor apply to the same fuel-energy basis; no second efficiency adjustment is applied to the money or CO₂ totals.

Can I calculate insulation savings for an adjunct cooker?

Yes. Enter the exposed area and measured surface temperature of the cooker. The example starts at 95 °C. It estimates surface heat retained and the corresponding fuel equivalent, not changes in cooking time, evaporation or recipe performance.

How is heat loss calculated?

For each square metre, bare heat loss combines convection and radiation: q = h(Ts − Ta) + εσ[(Ts + 273.15)⁴ − (Ta + 273.15)⁴]. The convection coefficient is estimated as h = 5.7 + 3.8v W/m²K, where v is air speed in m/s.

The insulation calculation balances conduction through the layer against heat released from its outer surface. Conductivity is approximated as λ = 0.031 + 0.000188 × mean layer temperature, in W/mK. This conductivity curve is an assumption; check it against the selected insulation’s certified data.

Heat retained per year = (bare kW − insulated kW) × operating hours ÷ 1,000. The calculation uses a flat-area approximation and does not separately resolve thermal bridges, fixings, dome curvature, gaps or temperature changes during a batch. Validate coverage, temperatures and material properties for a project estimate.

Is retained heat the same as a gas saving?

No. Retained heat is energy no longer lost through the modelled surface. For a fuel-fired heat supply, the fuel equivalent divides that heat by the heat-supply efficiency. This assumes the heat supply controls reduce input accordingly.

A boiler nameplate efficiency alone may not include steam distribution losses. Use a consistent net or gross calorific basis for efficiency, tariff and emissions factor. The estimate does not include evaporation, flue-gas losses, batch throughput gains or measured changes in burner consumption.

Are these thermal images measured?

No. The thermal view uses coloured 3D images, not camera measurements. Changing the inputs updates the numbers, not the images. Use a site thermal survey to measure surface temperatures.

What should I check before ordering?

Confirm the area, surface finish, measured temperatures, operating hours and access requirements. Use your energy tariff and an installed quotation for payback. The calculation covers surface heat loss only; it excludes maintenance savings and changes in equipment life or room temperature.

The 45 °C outer-surface value is a design target, not a universal safe-touch guarantee. Actual contact conditions, joints and exposed parts need a site-specific check.

Compare insulation thicknesses
Brewery cooker: 39 m² at 95 °C, air 25 °C, 6,600 h/year. Select a thickness to load this example.
ThicknessInsulated loss, kWHeat retained, MWh/yrOuter surface, °C
25 mm4.1247.133.2
50 mm2.2260.029.4
75 mm1.5264.628.0
100 mm1.1267.027.3

Engineering basis: Calculation methodology · Inzonex Modular Insulation