Inlet Air Cooling Improves Gas Turbine Performance

Inlet Air Cooling Improves Gas Turbine Performance

by Sanjeev Jolly, PE – Senior Engineer, Engineering Services

An inlet air cooling (IAC) system offers one of the most cost-effective ways to improve gas turbine (GT) performance – especially during the peak hours of hot summer months. After all, GT output depends on ambient air temperature – the higher the temperature, the lower the density, and the harder it is to move air mass through the GT. However, that’s not the only way IAC improves GT output. It also enhances compressor performance and enables more fuel to be ignited without increasing the firing temperature.

There are two major types of inlet air cooling: evaporative and chilling. Evaporative coolers and foggers fall in the first category; chillers and mechanical refrigeration make up the second. Evaporative cooling can cool the inlet air only to within 1 or 2°F of wet bulb temperature, whereas chillers can cool to below dew point temperatures – in the 45 to 50°F range. OEMs have strict guidelines for cooling below this range due to icing concerns. As the air flow accelerates at the compressor inlet, it decreases the dynamic temperature by 8 to 10°F, causing ice flakes to develop. At high velocities, these can cause serious blade damage and excessive vibration. Evaporative cooling systems require less capital investment and offer a shorter payback period, but they limit the potential gain in output.

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Figure 1: Pinless nozzle in a fogging system creates a fine mist of water droplets with the sole purpose of evaporation.

Evaporative Cooling

In evaporative coolers, water is sprayed over the media and the latent heat of vaporization of water provides sensible cooling of the air. The quantity of evaporated water depends on the air’s ability to hold water vapor and is limited by the wet bulb temperature. In arid regions with low humidity, the potential gains are significant. Many evaporative systems have mist eliminators downstream that capture water droplets to prevent carry-over into the compressor. Foggers operate on the same principle: a fine mist of water droplets is sprayed in the air, but all the water is supplied with the sole purpose of evaporation with no water circulated back (figure 1).

The design of the fogging system, including the selection of pumps, is important. The placement of fogging nozzle arrays is critical in determining the residence time for evaporation. Residence time is primarily a function of droplet size, dry bulb and wet bulb temperature: it’s essential that all the droplets evaporate before they reach the compressor inlet to prevent water carry-over. Some droplets will agglomerate and condense on the walls, silencers and other obstructions, so it’s important to provide drains. The system should be designed to minimize wastage of water. Nozzle arrays and location of nozzles within the arrays must be positioned to provide uniform coverage in a wide variety of operating conditions.


With mechanical chilling, the inlet air can be cooled to below dew point temperatures, achieving a more consistent and dependable compressor inlet air temperature. Since this process involves removing water vapor from the air, it can add a significant auxiliary load – even more so in regions with higher humidity during the summer months. On average, the auxiliary load equals about a third of the output gain (figure 2).

Depending on whether the plant is simple- or combined-cycle, this may impact the heat rate. Chillers typically run on electric power, although there are also absorption chillers that operate on steam, hot water or natural gas. Absorbers have a low coefficient of performance (COP) – in the range of 0.7 to 1.2 – depending on whether they are single- or double-effect. Electrically driven chillers, on the other hand, have a COP of 3 or higher, so absorbers are justified only when there is excess steam or hot water available that cannot be used for other purposes. If steam is pulled from the steam turbine to operate them, it can negatively impact the heat rate.

If the objective is to increase output for a few hours a day, chilling can be combined with thermal storage to accomplish this during peak periods. With thermal storage, the cold reservoir is built during off-peak hours, and the chilled water is used during peak hours to provide cooling. Since the chillers may not be running at all – or only at partial load during peak hours – the output is optimized during peak hours when it is needed most. However, the thermal storage design is site-specific and requires detailed evaluation to maximize the benefit.

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Figure 3: Wet compression nozzle placement for GE Frame 7EA

Wet Compression

In addition to evaporative cooling and chilling, there is another class of inlet air cooling known as wet compression, high fogging or SPRINT, depending on the OEM (figure 4). With wet compression, water droplets are introduced in excess of what is required for evaporative cooling – with the intention of producing carry­over to the compressor. The work of compression raises the air temperature, which in turn increases its capacity to absorb water. The excess water carried over into the compressor is thus absorbed in the successive compressor stages (figure 3).

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Figure 2: Chiller package for a typical ‘F’ machine

The compressor stage in which full evaporation takes place depends on the quantity of water injected. The compressor consumes about half to two-thirds of the power produced by the gas turbine, so any reduction in its power consumption corresponds to higher net power output. Since it takes less energy to compress cooler air, the compressor draws less power, increasing the turbine’s net output. This also reduces the compressor’s discharge temperature, allowing more fuel to be fired in the combustor while maintaining the same firing temperature. The increased mass flow, improvement in compressor efficiency and ability to fire harder without raising firing temperature cumulatively produce more power.

Wet compressor injection flow rates are typically expressed as a percentage of air intake – usually from 0.5 to 2 percent. Rarely, this number is allowed to go higher. For example, the suggested low-pressure compressor (LPC) flow rate for the LM6000 SPRINT is less than 1 percent of airflow.

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Figure 4: Fogging skid and wet compression skid for GE Frame 7EA

Of all the cooling system options, wet compression requires the most caution, since the nozzles are placed close to the compressor inlet. It’s important to minimize the risk of any part becoming loose and carrying over into the compressor. Wet compression is sometimes used in combination with either evaporative cooling or chilling to further enhance performance (figure 4).

If IAC interests you as a cost-effective way to improve turbine performance, we can answer any questions you might have. If you should decide to install IAC, we can help you select and review the complete system before installation. Contact us at