Economizers

An economizer is a subcooler that uses part of the refrigerant flow from the condenser to cool the rest. A portion is expanded and boiled off to chill the main liquid stream before it reaches the expansion valve.

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REFRIGERANT DUTY

Economizers

The gain is real and it comes from a small, cheap exchanger. Subcooling the liquid lowers the vapor quality entering the evaporator, so more of that surface does useful boiling, and the compressor does less work per unit of cooling.

Economizer duty is small relative to the main circuit, so the exchanger is small. The selection is driven by the subcooling target rather than by system tonnage.

economizers duty with SWEP brazed plate heat exchangers

A large plant can take a small economizer and still see the COP gain.

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It is worth being precise about the mechanism, because it decides how much subcooling is worth buying.

economizers - sized on subcooling, not tonnage

Sized on Subcooling, Not Tonnage

In Practice

  • Sized on Subcooling, Not Tonnage
SWEP B18
economizers - co2 economizers need the u class

CO2 Economizers Need the U Class

In Practice

  • CO2 Economizers Need the U Class
SWEP B18

Where the COP actually comes from

Liquid arriving at the expansion valve at saturation temperature flashes as it expands, and the flash fraction is refrigerant that will not absorb any latent heat in the evaporator. It is carried through as vapor and compressed again for nothing.

Every degree of subcooling reduces that flash fraction. The evaporator sees denser liquid and behaves as though it had more surface; the compressor sees the same suction conditions but delivers more cooling for them.

The economizer pays for itself by being the cheapest way to add that subcooling - cheaper than extra condenser plates, because it works on a side stream at a lower temperature.

  • V80 at moderate plate counts - is a common economizer selection on conventional refrigerants.

Economizers
Distribution
Charge Volume
Pressure Class
Superheat Control

Sizing This Duty

Economizer sizing starts from the refrigerant and the system capacity. Add the entering liquid temperature, the subcooling you are after and the saturation temperature on the evaporating side. The quote names a frame, a plate count and a pressure class.

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On Site: Economizers

The main liquid flow and its temperature leaving the condenser, the liquid temperature you want at the expansion valve, the refrigerant, and the intermediate pressure at which the side stream boils. That last figure is the one people leave out, and it is not a free choice: it is fixed by the economizer port on the compressor.

Add the superheat the compressor needs on the vapor returning to that port. With those the unit can be rated. Plant capacity alone tells us almost nothing about it.

Nearly always the way the boiling side is fed. The side stream enters as a liquid and vapor mixture, so the unit has to stand vertically with that mixture entering at the bottom and the main liquid running counter-current to it. Laid on its side, or piped so both streams travel the same direction, part of the plate pack sits full of liquid and does nothing while the rest runs dry.

The signs are an expansion valve that never settles, liquid carried over toward the compressor port, and a liquid line warmer than the selection promised. Mounting and Piping covers the port order.

Match the frame, plate count, pressure class and connections, yes. The piping is brazed to the old port positions, and an economizer is small enough that a few plates either way moves the subcooling noticeably.

Read the whole string off the nameplate, including the series letter in front of the frame number. A V80 and a B80 look the same on the bench, but only one has a distribution device on the boiling side. If the plate has corroded past reading, send the outside dimensions, the port centres and the refrigerant, and we will work back to the build.

Treat the whole unit as high pressure. The class letter applies to the exchanger, not to one circuit, and on CO2 the side that runs at intermediate pressure in operation can climb well above it when the plant stands idle and warms up. The U class covers 64 to 140 bar, which is why the B4T and B18 are the frames used here.

Where UL approval is required for CO2 duty, plan on a relief valve on each side set at 0.9 times design pressure. Leaving the valve off the lower-pressure side is the usual omission. See Pressure Classes for the other class letters.

Frames for This Duty

SWEP B18 brazed plate heat exchanger

SERIES • 18 TO 75 GPM

SWEP B18

U pressure class - 64 to 140 bar, built for transcritical CO2.

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SWEP B80 brazed plate heat exchanger

SERIES • 18 TO 75 GPM

SWEP B80

The 526 mm standard - and the plate shared by the F80, P80 and V80 evaporators.

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SWEP B4T brazed plate heat exchanger

SERIES • UP TO 18 GPM

SWEP B4T

SWEP B4T: a small copper-brazed plate heat exchanger for refrigerant and cooling duties up to 30 kW.

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