Plate
Heat Exchanger History :
The plate heat exchanger (PHE) was invented by Dr
Richard Seligman in 1923 revolutionising the methods for
the indirect heating and cooling of fluids. Dr Seligman
founded in 1910 as the Aluminium Plant & Vessel
Company Limited, a specialist fabricating firm supplying
welded vessels to the brewery and vegetable oil trades.
A plate heat exchanger is a type of heat
exchanger that uses metal plates to transfer heat
between two liquids. This has a major advantage over a
conventional heat exchanger in that the liquids are
exposed to a much larger surface area because the
liquids spread out over the plate. This facilitates the
transfer of heat, and greatly increases the speed of the
temperature change. It is not as common to see plate
heat exchangers due to the fact that they need well-sealed
gaskets to prevent the liquids from escaping, although
modern manufacturing processes have made them feasible.
The concept behind a heat exchanger is the use of
pipes or other containment vessels to heat or cool one
liquid by transferring heat to another. In most cases,
the exchanger consists of a coiled pipe containing one
liquid that passes through a chamber containing the
other. The walls of the pipe are usually made of metal,
or another substance with a high thermal conductivity,
to facilitate the interchange, whereas the outer casing
of the larger chamber are made of a plastic or coated
with thermal insulation, to discourage heat from
escaping the exchanger.
The plate heat exchanger is a specialized design well
suited to transferring heat between low-pressure
liquids. In place of a pipe passing through a chamber,
there are instead two chambers, usually thin in depth,
separated at their largest surface by a metal plate. The
plate produces an extremely large surface area, which
allows for the fastest possible transfer. Making each
chamber thin ensures that the majority of the volume of
the liquid contacts the plate, again aiding exchange.
In a Plate Heat Exchanger (PHE), plates are generally
arranged in such a way that it forms channels of hot and
cold liquid alternately. Due to corrugations in the
plate, high turbulent flow increases the heat transfer
rate. As compared to Shell & Tube Heat Exchanger, PHE
can give approach of 1°C whereas Shell & Tube Heat
Exchanger gives approach up to 5°C. For the same amount
of heat exchange the size of the PHE is less, because of
the large heat transfer area afforded by the plates (the
large area through which heat can travel). Expansion of
the heat transfer area is possible in PHE. Due to the
above reasons PHE are used for the better and controlled
heat transfer.