Technical resources · PHE-INDIA

Plate heat exchanger working principle

A plate heat exchanger transfers heat between two fluid streams through metal plates. In a gasketed unit, the plates form alternating channels: one stream gives up heat while the other receives it. The fluids remain in separate passages during normal operation.

How the plate pack works

A fixed frame plate and a movable pressure plate hold the plate pack together. Gaskets seal the edges and route each fluid into its assigned channels. Heat passes from the hotter fluid, through the plate wall, to the colder fluid. Corrugated plates increase the effective surface and disturb the flow, helping heat transfer.

In a typical counterflow arrangement, the streams travel in opposite directions. This maintains a useful temperature difference along the plate surface. Actual port positions and the number of passes depend on the selected unit; always use its approved connection drawing.

Plate heat exchanger flow diagram

Simplified counterflow: hot fluid flows down one channel and cold fluid flows up the adjacent channel, with heat crossing the separating plate
Schematic of two adjacent channels, not a fabrication drawing. A complete exchanger repeats these channels through its plate pack.

Follow the hot inlet to the hot outlet and the cold inlet to the cold outlet. The arrows across the centre show heat transfer, not fluid crossing the plate. The drawing omits manifolds, gasket grooves and pass partitions.

What changes the outlet temperature?

Outlet temperatures depend on both inlet temperatures, the flow rates, fluid properties, available plate area and the condition of the heat-transfer surfaces. Reducing a flow rate can change the outlet temperature without increasing total heat recovered. A change in viscosity or fouling can alter both heat transfer and pressure drop.

For a single-phase fluid with approximately constant specific heat, the heat duty is Q = ṁ × cp × ΔT. Flow and temperature measurements must use consistent units. Condensing steam and other phase-change duties require an enthalpy calculation instead.

From principle to plant application

The same separation principle supports industrial oil and water cooling and food and beverage heating or cooling. Material compatibility, cleanability and the required temperature programme decide whether a particular plate pack is suitable.

A compact exchanger still needs space for connections, inspection and opening the frame. See the design and selection checklist before requesting a quotation.

Common questions

Do the two liquids mix?

They are separated in normal operation. A damaged plate or sealing fault can compromise separation; a process requiring special contamination protection needs an appropriate design review.

Does every PHE use counterflow?

No. Counterflow is common, but multi-pass and specialised arrangements differ. The supplied drawing determines the correct connections.

Can I save this explanation as a PDF?

Download the working principle notes (PDF), or use your browser’s Print / Save as PDF command for this illustrated page.

Component roles and flow arrangements

What each part does
ComponentFunction
Heat-transfer plateSeparates adjacent fluid passages and provides the surface for heat transfer.
GasketSeals the passage and routes fluid through the intended ports.
Frame and pressure plateSupport and compress the plate pack to the specified assembled dimension.
Connections and pass arrangementDistribute the fluid; actual inlet and outlet positions follow the unit drawing.

In counter-current flow, the streams move in opposite directions. In co-current flow, they move in the same direction and the temperature difference typically reduces along the flow path. The effect on outlet temperature depends on heat-capacity rates and available area; there is no single efficiency percentage for every exchanger.

For Q = ṁ × cp × ΔT, using mass flow in kg/s, specific heat in kJ/(kg·K) and temperature change in K gives heat duty in kW. A temperature difference of 1 K equals a difference of 1 °C. This sensible-heat relation assumes no phase change; use appropriate property data and check both sides of the heat balance.

See design and pressure-drop considerations and application-specific inputs. The diagram illustrates heat flow, not a piping or fabrication specification.

Need help applying this to your process?

Share your duty or existing unit details for engineering review.

Discuss your requirement →