The frame is the radiator
The pack is clamped between two heavy end frames. They are flat, vertical and large, the most efficient shape there is for shedding heat into a plant room.


Inzonex Modular Insulation · Hot-water skid
A plate pack runs hot on every face. Drag the divider: the right-hand side is a fitted removable module on this exact geometry.
Estimate: 2 × 6.000 m² · 60 °C bare surface · 8,000 operating hours/year.
For your operating conditions
Change any input and every figure recomputes. The defaults describe the equipment modelled here.
What this is
A plate pack runs hot on every face.
A plate heat exchanger is a stack of thin corrugated metal plates, clamped between two heavy end frames. It carries two fluids through alternate channels, so heat passes from one to the other without them mixing.
On this hot-water skid there are 2, each about 6.0 m² of surface above room temperature. At 60 °C they shed 5.7 kW into the plant room. With 50 mm of removable insulation the same surfaces shed 349 W, 93.9 % less. The module settles at 23.5 °C, at or under our 45 °C touch-safe target. We set that target against the burn thresholds in EN ISO 13732-1.
These are steady-state model estimates using the stated areas and class assumptions. Agreement with site measurements or a survey report has not been established.
Inzonex benefits
Water-to-water duty on this skid. Modules unclip for operation and inspection, then refit onto the same geometry.
The pack is clamped between two heavy end frames. They are flat, vertical and large, the most efficient shape there is for shedding heat into a plant room.
Four to eight tie bars run the length of the unit. Lagging wrapped over them conducts straight through, so the bridging factor is carried, not assumed away.
Plate packs come apart for cleaning and gasket renewal on a fixed cycle. A module that will not unclip in minutes is cut off once and never replaced.
Separate sections around the port necks, the gauges and the frame bolts, so nothing is cut to take a reading.
Area and temperature scenarios
Bare surface loss per item. Nothing here is interpolated — each cell is a separate solution of the same balance, at 20 °C ambient.
| Pack area | Area m² | 50 °C | 55 °C | 60 °C | 65 °C | Insulated 60 °C | Cut |
|---|---|---|---|---|---|---|---|
| 2 m²plate pack and frames | 2.00 | 672 W | 810 W | 954 W | 1.1 kW | 58 W | 93.9 % |
| 3 m²plate pack and frames | 3.00 | 1.0 kW | 1.2 kW | 1.4 kW | 1.7 kW | 87 W | 93.9 % |
| 4 m²plate pack and frames | 4.00 | 1.3 kW | 1.6 kW | 1.9 kW | 2.2 kW | 116 W | 93.9 % |
| 6 m²plate pack and frames | 6.00 | 2.0 kW | 2.4 kW | 2.9 kW | 3.3 kW | 175 W | 93.9 % |
| 8 m²plate pack and frames | 8.00 | 2.7 kW | 3.2 kW | 3.8 kW | 4.4 kW | 233 W | 93.9 % |
| 10 m²plate pack and frames | 10.00 | 3.4 kW | 4.0 kW | 4.8 kW | 5.5 kW | 291 W | 93.9 % |
| 12 m²plate pack and frames | 12.00 | 4.0 kW | 4.9 kW | 5.7 kW | 6.6 kW | 349 W | 93.9 % |
| 15 m²plate pack and frames | 15.00 | 5.0 kW | 6.1 kW | 7.2 kW | 8.3 kW | 437 W | 93.9 % |
| 20 m²plate pack and frames | 20.00 | 6.7 kW | 8.1 kW | 9.5 kW | 11.0 kW | 582 W | 93.9 % |
| 25 m²plate pack and frames | 25.00 | 8.4 kW | 10.1 kW | 11.9 kW | 13.8 kW | 728 W | 93.9 % |
| 30 m²plate pack and frames | 30.00 | 10.1 kW | 12.1 kW | 14.3 kW | 16.5 kW | 873 W | 93.9 % |
| 40 m²plate pack and frames | 40.00 | 13.4 kW | 16.2 kW | 19.1 kW | 22.1 kW | 1.2 kW | 93.9 % |
Area is the four exposed edge faces of the plate pack plus both end frames — 2 × (width + height) × depth. The nozzles, the tie bars and the pressing plates are counted separately. Nothing here is derived from the render: enter the geometry off the nameplate or the drawing.
Insulated column: 50 mm lamella at λ 0.038 W/m·K. Outer surface calculated without clamping. Our 45 °C design target is checked against the burn thresholds in EN ISO 13732-1
What this means
At the modelled defaults, on this equipment.
Asked about plate heat exchangers
Answers distinguish modelled heat-loss estimates from equipment selection and service guidance.
Two fluids run through alternate channels formed by the corrugated plates. Heat crosses the plate wall; the fluids never meet. The corrugations force turbulence. A plate unit transfers far more per square metre than a plain tube.
It transfers heat from the primary supply into the domestic hot water without mixing them. On this skid that is a water-to-water duty at 60 °C.
Plate-and-frame (gasketed, openable for cleaning), brazed plate (sealed, compact) and shell-and-tube (takes dirty fluids, larger footprint). Only the gasketed type is opened on a service cycle. Fixed lagging is cut off it and never refitted.
Modelled here: 2 units of 6.0 m² at 60 °C lose 5.7 kW bare, and 349 W with 50 mm of removable insulation. That is 93.9 per cent less. This is external loss from the exposed faces, not the useful duty transferred inside the unit.
What the numbers mean
Steady-state estimate using convection, radiation and an insulation energy balance. Equivalence to a surveyed equipment model has not been established.
Going deeper
The figures on this page say what the heat costs. These say which type to specify, when the pack has to come apart, and what the approach temperature is telling you.
The first question is not the size. It is whether it can be opened.
OpenPlate heat exchangersIt tells you it is fouled long before it stops working.
OpenPlate heat exchangersAlmost every complaint about an exchanger is one of four things.
OpenThe rest of the skid
The casing stays hot. The motor must not.
OpenHot waterThe smallest surfaces lose the most.
OpenHot waterEvery joint is a fin the pipe did not ask for.
OpenHot waterA sieve in the line, and it is opened on a cycle.
OpenHot waterA separator holds its charge at line temperature.
Open