Several variables affect efficiency. The functions described here highlight the main service procedures applicable to all centrifugal chillers to maintain high efficiency, low upkeep, and long life.

HEAT TRANSFER

Heat transfer has the single greatest effect on chiller efficiency. Large chillers can have over five miles of tubing in their condenser and evaporator tubes, so clean heat transfer is fundamental to maintaining high efficiency.

Chiller efficiency declines rapidly with fouled or contaminated tubes. Minerals, scale, mud, algae, and other impurities increase thermal resistance and degrade overall performance. These contaminants accumulate on the water side of heat transfer surfaces in closed- or open-loop systems. (For more information, see the accompanying sidebar, “Tube Cleaning Checklist,” below.)

Approach temperatures (the difference between a heat exchanger’s leaving fluid temperature and the saturated temperature of the refrigerant being cooled or heated) are a good indicator of heat transfer efficiency. Higher approach temperatures are prime indicators that heat transfer efficiency is decreasing.

By keeping log sheets, the servicer can easily detect when temperatures start to change from their efficient levels.

A hypothetical example of a 600-ton chiller operating year- round in a hospital shows how operating costs can increase by $20,000. As the evaporator and condenser fouling factors increase, operating conditions move to 42.4 degrees F evaporator temperature and 97.4 degrees condensing temperature, resulting in 0.593-kW/ton operation — an 8% operating cost increase. Keep those tubes clean!

CONDENSER WATER TREATMENT

All condenser water loops using open cooling sources (such as atmospheric cooling towers) require water treatment of some sort. Scale, corrosion, and biological growth lead to fouling in the condensers. This impedes heat transfer.

Erosive conditions (sand flowing through the tubes at high velocity) may pit tubes, decreasing tube effectiveness. Serious water conditions can damage tubes, piping, and other materials in contact with the water. Inspect chilled water loops once a year for general water quality and evidence of corrosion.

The entering condenser water temperature (from the cooling tower) also affects chiller efficiency. Lowering this temperature improves the chiller’s efficiency. On some building systems, the operator will lower the chilled water setpoint to overcome air handler deficiencies, such as dirty coils. This cures the symptom, not the problem, and makes the chiller work harder for the same net cooling effect.

REFRIGERANT

The actual amount of cooling a chiller performs depends on how much refrigerant (cfm) it moves through the compressor. It is important to maintain the proper level of refrigerant for the conditions desired. Refrigerant leaks, as well as air and moisture introduced into the system, decrease system efficiency and reliability.

Refrigerant charge: A low refrigerant charge, usually due to leaks, causes the compressor to work harder for less cooling effect. Positive-pressure chillers can store their entire refrigerant charge in the condenser, so leak repair is usually a simple task. Low-pressure chillers do not have inherent storage capability, and the charge must be removed for leak checks and repair. For large-capacity machines, some type of pumpout storage needs to be provided.

Low-pressure chiller: Although they will be phased out by 2020, low-pressure chillers are still commonly used. Their evaporators operate in a vacuum and use either CFC-11 (now phased out) or the alternative, HCFC-123. It is difficult to create a perfectly sealed unit, so noncondensables (air and moisture) leak into the chiller. Noncondensables create two problems:

1. They offer no refrigeration effect, even though the compressor uses energy to move them. At the same time, they can blanket tubes with air, preventing them from doing any heat exchange work.

2. Noncondensables contain moisture, which causes acids to form within the chiller. These acids can damage motor windings and bearings.

Noncondensables lower the real efficiency of the chiller from the rated performance by as much as 8% at 60% load and 14% at 100% load.

Purge units on low-pressure chillers minimize the effect of noncondensables. Purge units must be serviced and maintained according to the manufacturer’s recommendation. While modern, high-efficiency purge units minimize air in the chiller and refrigerant loss, older purge systems can lose as much as 25% of the chiller’s refrigerant charge per year.

Positive-pressure refrigerants: Eventually, positive-pressure chillers using HFC-134a, HFC-410A, and HCFC-22 will replace low-pressure chillers. They do not require purge units because noncondensables cannot enter the chiller.

CONTROLS, STARTERS, MOTORS

The chiller motor is typically the largest single electrical load in a building. Constant-speed compressors match capacity to load through inlet vanes, throttling the gas allowed into the compressor impellers. Closing the inlet vanes reduces flow, affecting efficiency at part-load conditions. This is not the most effective method of chiller capacity modulation.

With the right operating conditions, variable-speed drives (VSDs) can offer significant energy savings. Varying motor speed is a much more efficient method of capacity control, as it matches motor efficiency to load and wastes less energy. VSDs also act as soft starters to lower the inrush current for the motor to almost that of the full-load-running amps. This is an important factor for chillers operating on emergency power generators. VSDs also reduce the mechanical shock of starting large-horsepower motors, increasing reliability and life.

However, VSDs introduce another efficiency concern. Proper VSD calibration is essential for optimum part-load operation. Operation and controls must be checked to ensure that speed is matched to load.

Here is a brief checklist for efficient operation of starters and motors:

Check safety and sensor calibrations on microprocessor controls (consult manufacturer’s guidelines).

Check electrical connections, wiring, and switchgear related to the chiller for hot spots and worn contacts.

To prevent insulation faults, test electrical motor windings for insulation resistance to ground and winding to winding.

Check the cooling line filter of hermetic refrigerant-cooled motors.

Check the shaft seal of open-drive motors for possible refrigerant leaks.

Clean motor-cooling air vents to ensure maximum cooling effect.

COMPRESSOR LUBRICATION

Once a year, take a sample of lubrication oil in the compressor and send it to a laboratory for a “Spectrometric” chemical analysis and report. This gives the levels of any moisture content, wear metals, acids, and other contaminants that affect performance.

Like any hermetically sealed refrigeration system, the oil should only be replaced if indicated by analysis.

High moisture content can indicate a problem with the purge unit. Sample low-pressure chillers more frequently based on purge run-hours. Check oil filters for pressure drop; replace them if the oil charge is replaced.

FUTURE OF CHILLER OPERATION

Daily, weekly, monthly, and annual operational reviews give you optimum chiller efficiency. The press for improved efficiency will continue; manufacturers are developing systems that respond to this demand.

The emphasis is already changing from scheduled maintenance to predictive and reactive maintenance, based on operating information gathered via microprocessors. This will help prevent major failures, reduce downtime for maintenance functions, and minimize emergencies. With improved technologies, service representatives will have more information to keep chillers operating at the levels customers expect.

Sidebar: Tube Cleaning Checklist

Condenser water tubes:

Drain water from condenser.

Remove nonconnection head.

Visually inspect tube sheets and water boxes for obstructions, fouling, and scale.

Using a mechanical rotating tube brushing machine with nylon brushes, brush clean the length of each tube, removing soft debris and mud.

Clean visible scale (hard mineral deposits) chemically (consult a chemical water treatment firm). Never use cutting devices or hard metal tools to clean tubes.

Flush clean the tubes with water.

Replace head gaskets if they are worn.

Check pressure drop to confirm proper design water flows.

Perform eddy current scan (nondestructive tube analysis) every three years; perform during the first year of operation to establish a baseline.

Evaporator tubes:

Brushing is not typically required due to the closed chilled-water loop (if required, see checklist for condenser water tubes).

Monitor approach temperatures to determine evaporator fouling.

Check pressure drop to confirm proper design water flows.

Perform eddy current scan (nondestructive tube analysis) every five years; perform during the first year of operation to establish a baseline.

Grenz is with McQuayService. McQuay International products and services are provided through a worldwide network of sales and service offices. For more information, call 800-432-1342 or visit www.mcquay.com (website). For training on servicing centrifugal chillers, contractors can attend McQuay training classes in Staunton, VA. To enroll, go to www.mcquay.com/training.

Publication date: 07/08/2002

Table 1. Maintenance schedule for centrifugal chillers. (Courtesy of McQuay International.)