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2000 Hook-up Book - Spirax Sarco

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SYSTEM DESIGN<br />

32<br />

Make<strong>up</strong> Air Heating Coils<br />

The steam trap must handle<br />

lots of air and drain condensate<br />

at saturated steam temperature<br />

continuously while the load and<br />

pressure are changing and thus a<br />

Float-Thermostatic type is recommended<br />

for all air heating coils.<br />

The trap is mounted below the<br />

condensate outlet from the coil<br />

with a vertical drop giving enough<br />

hydraulic head to enable a suitable<br />

size to be selected. A 14"<br />

head should be the minimum and<br />

represents about 1/2 psi, a 28"<br />

head about 1 psi, and to reduce<br />

possibility of freeze-<strong>up</strong>, a drop of<br />

3 ft. to the trap is recommended.<br />

Preheat/Reheat Coils<br />

The preheat/reheat coil hook<strong>up</strong><br />

shown in Fig. II-26 (page 96) may<br />

employ a direct-acting temperature<br />

control or with larger coils, a quicker<br />

responding pilot-operated type<br />

with a closer control band is recommended.<br />

This arrangement<br />

allows filtration and perhaps humidification<br />

of the air to be carried out<br />

at the controlled preheat temperature,<br />

and the reheat coil brings the<br />

dry bulb temperature of the conditioned<br />

air to the required value for<br />

distribution. The preheat coil is<br />

used to heat outside air <strong>up</strong> to the<br />

intermediate temperature but as<br />

outside temperature increases, the<br />

temperature control lowers the<br />

steam pressure in the preheat coil<br />

and condensate drainage tends to<br />

slow down. If the coil is being used<br />

where design loads occur at subzero<br />

temperatures, there can<br />

sometimes be only atmospheric<br />

pressure in the coil, although the air<br />

passing over it is still cold enough<br />

to lead to freeze-<strong>up</strong> problems.<br />

This difficulty is greatly<br />

reduced if the temperature sensor<br />

controlling the steam s<strong>up</strong>ply to the<br />

preheat coil is set to the needed<br />

distribution temperature. Part load<br />

conditions would then lead firstly to<br />

lowering the steam pressure in the<br />

reheat coil, where freezing will not<br />

occur, but pressure is maintained<br />

in the preheat coil until outside air<br />

temperatures are above the danger<br />

point. Such an arrangement<br />

reduces freeze-<strong>up</strong> problems in<br />

many instances on existing installations,<br />

at minimal cost.<br />

Corrosion And Waterhammer<br />

Problems<br />

Condensate mixed with air<br />

becomes corrosive and assuming<br />

the boiler water treatment is satis-<br />

Case in Action: Air Handling System Steam Coil Drainage<br />

Typical storage buildings are extremely large and difficult to<br />

heat. This example in specific has three floors with approximately<br />

486,000 ft 2 of floor space and heated with 150 air<br />

handling units. These units are comprised of bay heaters,<br />

overhead door heaters and administrative office area<br />

heaters. The minimum steam s<strong>up</strong>ply pressure to all of them<br />

is 20 psig and are pneumatically controlled.<br />

In the preceding 12 month period, $201,000 was<br />

spent on labor and materials to repair damaged coils. The<br />

common problem was condensate standing in the coils,<br />

unable to drain, causing erosion due to presence of carbonic<br />

acid and bulging/splitting as a result of freezing.<br />

Solution<br />

Starting with a training session at the facility that addressed<br />

this problem and typical solutions, <strong>Spirax</strong> <strong>Sarco</strong>’s local<br />

sales office implemented a “Cooperative Research and<br />

Development Agreement” (CRDA). The purpose of the<br />

agreement was to test a proposed solution including<br />

Pressure Powered Pumps and Pump/Trap combinations<br />

to eliminate system stall, thereby assuring thorough condensate<br />

drainage, regardless of s<strong>up</strong>ply air temperature,<br />

control valve turn-down or over-sized heaters.<br />

A test was conducted on four air handling units. One<br />

unit was hooked <strong>up</strong> as usual, without Pressure Powered<br />

factory, coil corrosion problems<br />

are usually due to condensate<br />

regularly backing <strong>up</strong> or lying stagnant<br />

on the bottom of the tubes<br />

during shutdown. If the coil is<br />

trapped correctly, the most likely<br />

cause is an overhead return<br />

which prevents the coil from draining.<br />

One remedy for this is to fit a<br />

liquid expansion steam trap at the<br />

lowest piping level, as shown in<br />

Fig. II-26 (page 96), set to open<br />

when the temperature drops<br />

below 90°F. The coil then drains<br />

only cold condensate to a sewer.<br />

In high pressure systems<br />

where waterhammer on start<strong>up</strong><br />

remains troublesome, a “safety<br />

drain” trap is sometimes used. This<br />

consists of a stock 15 psi rated<br />

inverted bucket trap fitted above<br />

the main trap which discharges to<br />

drain whenever coil pressure is<br />

low, but due to its design locks shut<br />

at higher pressure. While this is<br />

useful on pressurized mains, the<br />

safety trap may require a pressure<br />

considerably higher than its nominal<br />

rating to lock shut and on<br />

modulating service a considerable<br />

amount of condensate may be<br />

wasted. This makes the combination<br />

pump/trap a more viable<br />

solution to this problem.<br />

Pump drainage systems. The other three were drained<br />

by either open or closed loop PPP systems. Four days into<br />

the test and the unit without a PPP drainage system had<br />

three frozen coils. It was found that as outside s<strong>up</strong>ply air<br />

temperature dropped below 36˚F, it was necessary to close<br />

outside dampers and use 100% recirculated air, or the<br />

coils would freeze. The three units drained by PPP systems<br />

continued operating trouble-free.<br />

Benefits<br />

Employee Safety<br />

• Improved indoor air quality through the use of a higher<br />

percentage of outside air s<strong>up</strong>ply.<br />

• Reduced chance of injury by eliminating water leakage on<br />

the floor from broken coils and subsequent slippage.<br />

• Fewer burns because there are fewer steam leaks.<br />

• Greater employee awareness of hazards because of<br />

training.<br />

Cost Savings<br />

• Reduced steam and condensate losses resulting in<br />

energy savings.<br />

• Reduced cost for management s<strong>up</strong>port (paper-work).<br />

• Cost savings of <strong>up</strong> to 30% above the initial installation<br />

cost in a 12 month period.

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