HVAC and Chilled Water

Approach Drives the Cost

A brazed unit has no gaskets, so it has no gasket replacement schedule and no gasket failure mode. In a mechanical room where access is poor and the maintenance budget is thin, that removes the single most common source of unplanned work.

The trade is that a brazed unit cannot be opened. If it fouls it is cleaned in place with a circulating acid solution rather than pulled apart, and if the water is dirty enough to defeat that, a gasketed unit is the better answer. Specify the strainer with the exchanger, not after the first cleaning.

Approach drives the cost. Tightening the approach means more plates, and plate count is most of the price. Decide what approach the system actually needs rather than inheriting a number from a previous job.

Plate angle is the second lever. H-type plates give the highest coefficient and the highest pressure drop, L-type the least of both. Where pumping head is plentiful an H plate buys a tight approach cheaply.

Glycol changes the numbers. A unit sized on water will be undersized on a 30 percent propylene mix. AHRI certification now covers propylene and ethylene glycol, so the performance can be relied on rather than derated by rule of thumb.

hvac and chilled water with SWEP brazed plate heat exchangers
Boiler Isolation Boiler Isolation
Chilled Water Chilled Water
Glycol Loops Glycol Loops
Approach Temperature Approach Temperature

HVAC and Chilled Water Selection

What decides the frame, and what to send with the enquiry.

Duty Inputs

  • Flows: both sides
  • Temperatures: in and out
  • Fluids: named, not described
  • Pressure drop: what is affordable

Typical Frames

Watch Items

  • Send the duty for a check
DUTY TYPICAL FRAME WHY
Boiler isolation B25T, B120T Stock availability, standard pressure class
Chilled water isolation B28, B45 Higher flow on the same footprint
Glycol to water B120T, B200T Plate count for the glycol derate
Chiller evaporator B250AS, B220 Asymmetric channels, low charge

Where the approach temperature actually goes

On a chilled water isolation duty the exchanger sits between two loops that are both trying to be the same temperature, and every degree it fails to close costs compressor work upstream.

A chiller asked to make 42 F water so that a building loop can see 44 F is doing measurably more work than one making 43 F. The exchanger in between is what decides that penalty, and it is paid every hour the plant runs rather than once at purchase.

The same logic runs backwards on the condenser side. A tight approach to the tower loop lowers condensing temperature, and condensing temperature is the single biggest lever on chiller efficiency. Sizing the isolating exchanger generously is usually the cheapest efficiency available in the whole plant room.

Where the budget will not stretch, spend it on the side with the larger temperature difference to gain. That is almost always the condenser.


Frames for This Duty


SWEP B25T brazed plate heat exchanger - the most widely stocked frame in the range
SWEP B28 brazed plate heat exchanger - two-pass series arrangement on the 526 mm frame
SWEP B45 brazed plate heat exchanger - three-pass capable on the 525 x 243 mm frame

What People Ask About HVAC and Chilled Water

No. Maximum flow on a datasheet is a ceiling set by the ports - the most the connections can pass - not a flow at which the unit performs a duty. A frame picked because its maximum flow matches the system flow will usually carry far too much pressure drop, and the figure says nothing about whether the plate count reaches the approach.

Use maximum flow only to rule frames out. The selection itself comes from the flows, the four temperatures and the pressure drop available, and it often lands in a larger frame than the flow alone suggested.

As much as the pumps can give without being upsized, and it should be stated, not left open. Pressure drop is what buys turbulence, so a generous allowance means fewer plates for the same approach and a less expensive unit. A very low allowance forces a large plate count, and at low channel velocity the pack is also more inclined to foul.

On a retrofit, the limit is whatever head the existing pump has spare at design flow - measure it instead of reading the pump nameplate.

By measurement. A frame is identified by the height and width of the plate pack and the distance between port centres, vertically and horizontally. The pack depth indicates the plate count, though not precisely enough to order from alone. Note the connection type and size on each port, and which ports are in use.

Add what the unit does: the fluids, the approximate flows and temperatures, and the equipment it serves. With those and a couple of photos we can name the frame and confirm the configuration before quoting.

It can, with conditions. Tower water is open and aerated and carries airborne dirt, scale and biological growth, and a brazed pack cannot be opened to remove any of it. A strainer matched to the frame's particle limit is the minimum; side-stream filtration and steady water treatment are what make the unit last.

Check the chemistry as well. Tower water concentrates as it evaporates, and chlorides that are harmless in the make-up water can reach a level where 316 pits - the case for SMO 254 plates. Where treatment is poor or the tower sits in a dirty location, a gasketed unit that can be opened is the better choice for free cooling.

Yes, and it is one of the more avoidable losses in HVAC. The glycol loop is protected by its antifreeze; the water on the other side of the plate is not. If cold glycol keeps circulating while the building water pump is off - a night setback, a tripped pump, a closed control valve - the standing water in the channels freezes and the plates split.

Interlock the two sides so glycol flow through the exchanger stops, or is bypassed, whenever water flow is lost, and prove water flow with a switch, not a pump run signal. The measures are set out under Freeze Protection.

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