options for optimizing combined cycle plants

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Prepared by. Hossam Ahmed Zein 2015 Optimizing combined cycle power plants efficiency ــــOptions for Optimizing Combined Cycle Plants ــــQuickly Boost Your Combustion Turbine Response CEPC Egypt :) :(

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Page 1: Options for optimizing combined cycle plants

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Options for Optimizingــــ

Combined Cycle Plants

Quickly Boost Yourــــ

Combustion Turbine Response

CEPC Egypt

:) :(

Page 2: Options for optimizing combined cycle plants

Options for Optimizing Combined Cycle

Plants

12/01/2015 | Thomas W. Overton, JD

With low gas prices and renewable generation boosting demand and capacity

factors for combined cycle plants, plant operators are being called upon to

squeeze out every last megawatt from their systems. Fortunately, there have

never been more ways to do it. Here are some you may not have thought of.

Gas-fired power is booming—even more than expected. For only the second

time ever, but also the second time this year, gas generated more electricity in a

month in the U.S. than coal. According to statistics from the Energy

Information Administration (EIA), in July 2015 coal generated 139 TWh, while

natural gas generated 140 TWh. Those statistics are a stark break from 2014,

when coal produced 150 TWh and gas was responsible for only 114 TWh.

While coal remained in the lead with a 34.5%-to-31.1% advantage in the power

mix through July, those numbers represent a fairly substantial departure from

EIA predictions. In its Annual Energy Outlook this year, the EIA predicted gas

would reach a 31% share—in 2040.

With gas-fired plants being called upon to shoulder an ever-growing share of

the power mix, plant owners are looking for more and better ways to squeeze

extra performance out of their equipment, without breaking the bank.

While gas turbine manufacturers such as GE, Siemens, and Mitsubishi-Hitachi

Power Systems offer a selection of upgrade packages to improve performance,

these kinds of choices are both expensive and require significant down time.

For plants that are not in the position to undertake costly outages and upgrades,

and those newer plants already operating state-of-the-art equipment, there are

still some ways to tweak out a few extra kilowatts.

Page 3: Options for optimizing combined cycle plants

Clean-Up Time

Jeff Fassett of IEM Energy Consultants, who spoke to POWER in October,

recommended that plant operators think first about cleanliness.

Fassett pointed out that a substantial portion of a turbine’s energy is used by the

compressor, which means dirty compressor blades can have a serious effect on

efficiency. “When the blades are dirty, the airflow is more turbulent, and that

will degrade performance.”

Of course, the importance of maintaining inlet filters and keeping intake air

clean isn’t a novel idea. Poor-quality inlet air can also lead to blade erosion and

corrosion of turbine components, both of which will hurt efficiency. One

problem is that the effects of poor-quality air are cumulative: Though cleaning

can address blade fouling to some extent, restoring original turbine

performance is typically not possible—and erosion can only be addressed by

replacement. Thus, it behooves turbine operators to keep air quality as high as

possible from initial startup.

But Fassett said the solution he recommends isn’t one operators often take:

Swapping out standard ASHRAE filters for HEPA-rated filters.

“The common approach is just changing the filters more often,” he said, “but

this doesn’t get to the root problem,” which is that lower-rated filters allow

more particulate matter into the turbine and that everything getting into the

compressor that doesn’t belong there degrades both short-term and long-term

performance.

Fassett has worked with plant managers to upgrade their turbine filters, which

usually involves a retrofit, depending on the configuration of the filter house.

A number of companies currently market gas turbine HEPA filters. Louisville,

Ky.–based AAF, which has supplied HEPA filters for more than 50 F-class

turbines worldwide, estimates that using these filters can recover 6% of the

power output normally lost to engine fouling. With HEPA filters, time between

turbine cleaning cycles can be at least 8,000 hours (Figure 1). Though the use

Page 4: Options for optimizing combined cycle plants

of HEPA filters results in a larger pressure differential, the initial power loss is

more than compensated for by substantially increased cleanliness and reduced

downtime.

1. Clean sweep. The differences in turbine blade fouling from operating with

different filters can be dramatic. The left photo shows turbine blades after 8,000

hours with a HEPA filter; the right photo, after 2,000 hours with a standard

filter. Courtesy: AAF International

Bill Lovejoy, chief engineer for engineering services firm NAES, concurred on

the importance of maintaining cleanliness, not just because of impact on the

turbine blades but also because of the effects dirty filters will have on

performance.

“It can catch up to you over time, and you are really hurting yourself. You pay

for that pressure drop in your overall efficiency.”

Operational Adjustments

Another performance element Fassett recommends that operators think about is

the low-load setpoints on their gas turbines—not just because of effects on the

gas turbine but also the downstream effects on the steam turbine.

“When the steam turbine is operating at low loads, you can exhaust the thermal

energy before the steam reaches the final stages and get condensation. That can

cause erosion of the turbine blades.”

Page 5: Options for optimizing combined cycle plants

Fassett said low-load setpoints for the gas turbines need to consider effects not

just on the turbines themselves but also on the rest of the plant.

Other efficiency losses can be found and eliminated by thinking about ways

energy may be escaping the system.

“One site we worked with has an auxiliary boiler and is using it to keep vacuum

on the steam turbine generator,” Fassett said. “All excess steam is being piped

to the heat-recovery steam generator (HRSG) to keep the boilers warm, so hot

restarts are minimized.” Another relatively simple tweak is installing heat

blankets to insulate the steam turbine, which cuts down on cold restarts, he said.

Aftermarket Add-Ons

In addition to relatively simple tweaks, there are more sophisticated aftermarket

tuning solutions that can be added to existing plants.

EthosEnergy has marketed its ECOMAX automated combustion tuning system

for several years. ECOMAX is designed to address performance instabilities

that can result from manual tuning to maintain emissions compliance,

particularly for NOx. Operating with lean premixed flames in the combustor

keeps NOx low but can cause instability in combustion dynamics, which can

damage turbine components over time. These instabilities are exacerbated by

large ambient temperature swings—common in many areas where gas is a

major element of the power mix, such as the U.S. Southwest and West Coast—

as well as by fuel quality and instrument drift. When the operating envelope

strays outside the optimized range, performance will suffer and emissions can

fall out of compliance.

Using real-time monitoring of combustion and emissions, the ECOMAX

system automatically tunes combustion to keep the turbine within the optimized

operational envelope (Figure 2). ECOMAX can communicate directly with the

turbine or integrate with the plant’s digital control system.

Page 6: Options for optimizing combined cycle plants

2. Autopilot. The ECOMAX automated combustion tuning system is capable

of monitoring a range of key turbine operating parameters and keeping output

within a specified range to avoid emissions problems and to maintain peak

performance. Courtesy: EthosEnergy

ECOMAX can also be used to boost performance, as necessary, with the

addition of the Tru-Curve option, which raises the baseload fuel-air ratio while

still controlling emissions and combustion dynamics. Tru-Curve can be turned

on and off as desired.

EthosEnergy says the ECOMAX Tru-Curve package can improve heat rate by

0.20% to 0.25% and boost power output by up to 11 MW, depending on the

size of the plant.

Another, more outside-the-box upgrade is the Turbophase compressed air

peaking power system. Offered by Jupiter, Fla.–based Powerphase, the

Turbophase unit uses a separate reciprocating engine to add additional

compression to the turbine air inlet, without the use of steam or water injection,

which can cause operational issues. Powerphase says this system allows faster

peaking response than existing options, allowing 10% to 20% additional

peaking power capability and up to 7% heat rate improvement, depending on

the model of turbine.

Page 7: Options for optimizing combined cycle plants

Low-Load Combined Cycle Operation

Combined cycle plants often do not operate in combined cycle mode at low

loads because the system is optimized for baseload operation, and improper

optimization can result in damage to the heat recovery steam generator, as well

as emissions violations. However, giving up the ability to operate at low loads

can mean lost revenue.

Many of the newest models of combined cycle plants are designed for load

following and low-load operation, but with the right approach, some older

plants can optimize their operations for low-load generation as well. The

Electric Power Research Institute (EPRI) recently conducted a proprietary

study determining the best ways to optimize combined cycle operation at a

plant using GE 7FA turbines. Though proper optimization procedures will vary

from plant to plant and depend on operational profiles, the EPRI study found

that a tradeoff between lower exhaust gas temperature and higher exhaust flow

would allow lower-load operation without damage to the HRSG and without

causing NOx emissions to spike.

Making it work requires careful monitoring of NOx and CO emission levels,

combustion dynamics, attemperator performance, main steam-line superheater

level, and inlet-guide vane position, in order to determine the minimum

generation load at the lowest possible turbi0ne-exhaust temperature.

Though there are trade-offs with nearly any performance enhancement, plant

operators have more options these days than ever.

— Thomas W. Overton, JD is a POWER associate editor.

Quickly Boost Your Combustion Turbine

Response

10/01/2014 | Dr. Robert Peltier, PE

Page 8: Options for optimizing combined cycle plants

Morris Cogeneration, a combined cycle cogeneration plant near Chicago, has

installed TurboPHASE, a fast-responding, modular “turbocharger” installed to

boost capacity and PJM regulation revenue. How does it perform?

Twice this year, PJM flirted with blackouts when brutal winter storms (dubbed

a polar vortex) struck the Eastern U.S. in January. The cold weather set a new

winter peak demand record of 141,500 MW on Jan. 7, busting the record set in

February 2007 by nearly 5,000 MW. In fact, the five biggest demands ever

placed on the PJM grid, and eight of the 10 largest, occurred between Jan. 7 and

Jan. 30. PJM reported that at one point, 36,000 MW was out of service due to

forced outages, which amounts to 20% of its installed capacity. Adam Keech,

director of wholesale market operations, is reported by RTO Insider as saying—

the morning after setting the winter peak record—“We really exhausted every

megawatt we had on the system.” Peaking capacity and fast unit response is a

necessity during summer and winter peaks, and many regional transmission

organizations (RTOs) are willing to pay well for the service.

A solid majority of new plant construction in PJM is gas fired, led by simple or

combined cycle plants. Simple cycle combustion turbine (CT) plants are less

efficient than combined cycle plants but are able to start more rapidly and add

valuable power to the grid in minutes, which is extremely valuable to a system

like PJM as synchronized reserve, fast grid regulation, or black start service. In

fact, ancillary service payments often justify the cost of constructing a simple

cycle peaking plant.

A New Option

Jupiter, Florida–based PowerPhase LLC has successfully demonstrated a new

technology called TurboPHASE that may allow an existing simple cycle CT or

combined cycle plant to add as much as 10% to 20% more power to the grid in

seconds, depending on plant configuration, addressing the quick-start and fast-

response needs of the modern grid.

The TurboPHASE system consists of a multistage intercooled centrifugal

compressor that delivers hot compressed air to the CT’s compressor discharge

section, thereby allowing the CT to operate at its rated capacity irrespective of

Page 9: Options for optimizing combined cycle plants

the ambient conditions (5C to 50C) or altitude (Figure 1). The system takes

advantage of the CT operating below its limits during hot weather much like an

inlet chiller or evaporative cooling system, although TurboPHASE can also

operate in conjunction with either of those inlet cooling options.

1. Turbocharging combustion turbines. TurboPHASE consists of four main components:

engine, gearbox, compressor, and recuperator. A gas-fired engine-compressor set

produces compressed air that is added to the combustion turbine’s compressor discharge

section to negate the effect of a high ambient temperature performance derate.

Courtesy: PowerPhase LLC

A separately fueled reciprocating engine direct drives the compressor. The heat

from the exhaust of the engine is used to heat the compressed air in the

recuperator before entering the CT compressor section. On an operating CT,

TurboPHASE is said to be able to ramp to full load in 60 seconds or less and

from part load to full load in 10 seconds or less. This design feature is sure to

be of interest to grid dispatchers anxious to have the ability to quickly backfill

lost capacity during a system emergency or to quickly respond to the

intermittency of renewable resources.

Field Tests Completed

Two prototype TurboPHASE modules (TPMs) were tested in August, and the

data and test results were provided to POWER on an exclusive basis. The tests

Page 10: Options for optimizing combined cycle plants

were conducted at Atlantic Power Corp.’s Morris Cogeneration Plant (Morris),

located just outside Chicago (Figure 2). The gas-fired 177-MW combined cycle

facility is located within the Equistar Chemicals petrochemical plant in Morris,

Ill. All of the steam (after passing through a steam turbine) and a portion of the

electricity produced by the plant is sold to Equistar, and the remainder of the

power is sold into the PJM West market. Morris is configured with three gas-

fired General Electric Frame 6B CTs, each with a heat-recovery steam

generator (HRSG).

2. Demonstration plant. Two TurboPHASE modules (TPMs) were installed at

Atlantic Power Corp.’s Morris Cogeneration Plant (lower left of photo) and

were recently performance tested. The TPMs each added over 3 MW of quick

response capacity to a Frame 6B combustion turbine and steam turbine system.

Courtesy: PowerPhase LLC

PowerPhase engineers ran a series of predictive performance models using

ThermoFlow in advance of the field tests. The models predicted that the CT

full-load performance would increase ~2.63 MW and the steam turbine by

~0.43 MW, for a total power increase of ~3.06 MW. The cost of the increased

Page 11: Options for optimizing combined cycle plants

output is the additional fuel burned by the CT (~10 MMBtu/hr) and the fuel

burned by the engine (~16.3 MMBtu/hr). Therefore, the incremental heat rate

of the unit with one TPM in service was expected to be on the order of 26.3

MMBtu/hr/3.06 MW = 8,650 Btu/kWh.

The demonstration test was conducted in two parts. The first test was designed

to demonstrate the increase in output capacity when using a single TPM. The

second test measured the response or ramping speed of the plant with one or

two TPMs injecting air into the plant’s CT1. Each of the TPMs used at Morris

is powered by MTU 20V4000L32 gas-fired engines, each rated at 2 MW.

Morris is also equipped with inlet chilling and HRSG duct-firing capability, and

both were in operation during the demonstration tests. The tests were conducted

with the CT at full power at an ambient temperature that averaged ~85F. At no

time during the tests were the operating limits of the CT exceeded.

Day One Tests. On the first day of testing, compressed air from TPM2 was

injected into CT1 as the system cycled off and on three times. Data was

collected at one-second intervals and then averaged. CT fuel flow

measurements were taken from plant instruments, and TPM fuel flow was

measured (at the inlet to the engine) at 16.3 MMBtu/hr as expected. TPM air

injection flow rate was measured by an annubar-type flow meter on the main

air header prior to entering the CT. The airflow from each TPM was measured

as 11.5 lb/sec at ~156 psi.

The measured test results at Morris showed that the average CT power boost

was 2.74 MW and that the steam turbine produced an additional 0.32 MW, for

a total power increase of 3.06 MW per TPM, very close to the prediction. As an

additional benefit, the TPM compressor intercoolers produced an average of 1.2

gallons per minute of clean water during the tests.

The second test of the day was measurement of the plant response to a demand

signal. The test procedure was to first ramp up TPM2 to full speed, no load. No

compressed air was produced by TPM2 while the system was idling. When

warmed up, TPM2 was ramped up to 75% load while venting the compressed

air produced to the atmosphere through a vent valve, bypassing the CT.

Page 12: Options for optimizing combined cycle plants

Simulating receipt of a demand signal with TPM2 at 75% load, the vent valve

was closed and the injection valve was opened, thereby sending compressed air

to the CT compressor discharge. The air injection quickly produced an

incremental power increase of about 1.5 MW, ramping up to ~2 MW when the

vent valve was fully closed and injection valve was fully open. Next, TPM2

was ramped to full power, and the CT responded by producing an increase of

~2.74 MW, with the steam plant power increase following. The test ended with

the load on TPM2 reduced to 75%, followed by opening the vent valve and

closing the air inject valve to the CT. Figure 3 shows the results of the response

testing completed on day one. The TPM was able to add much, although not all,

of the incremental power from the CT within the 60-second goal set by the

company.

3. Day one tests. Results of the first day of TurboPHASE demonstration tests

are illustrated. The blue line represents the temperature at the inlet to the

combustion turbine. The orange line shows the response of the combined cycle

plant to full air injection. Courtesy: PowerPhase LLC

Page 13: Options for optimizing combined cycle plants

Day Two Tests. The response tests were repeated on the second day of testing

using TPM1. Figure 4 illustrates the data collected during these tests, which

were very consistent with the previous day’s tests.

4. Day two tests. The test results of the second day of TurboPHASE demonstration tests

are illustrated. The last test of the day was with both TurboPHASE systems in operation

followed by a trip of one system. Courtesy: PowerPhase LLC

The second test of the day was to run both TPMs in parallel and inject the

produced compressed air into CT1. The final test simulated an unexpected trip

of a TPM. When the air supply from TPM2 ceased, a check valve in the TPM

prevented reverse flow, and TPM1 continued supplying compressed air to the

CT as expected.

The piping system pressure drop between the TPMs and the CT was ~11 psi

with one TPM operating (flowing 11.5 lb/sec) rising to ~40 psi with two TPMs

operating, so the airflow into the CT was slightly less than double (22 lb/sec).

The pressure drop effect is apparent in Figure 4 where a single TPM produces

Page 14: Options for optimizing combined cycle plants

~3 MW while two TPMs produce slightly under ~6 MW. A line size increase

from 6 inches to 8 inches would solve this problem, but since Morris doesn’t

anticipate operating the plant in this manner, the cost of the pipe size increase

isn’t justified.

Pluses and Minuses

Before assessing the results of the testing, it’s best to remember that this was

the first full-scale demonstration test of the TurboPHASE and we were privy to

only an overview of the testing and the performance results. That said, we are

still able to reflect on the performance of the system in relation to the important

ancillary services PJM and other RTOs desire: synchronized reserve, fast grid

regulation, and black start service.

Synchronized Reserve. A single TPM consists of a single MTU gas-fired

engine that will produce 2 MW were it fitted with a generator and operated

standalone, which is the obvious competitor to the TurboPHASE system.

Further, according to data on the MTU website, this model gas engine with a

generator operates at a heat rate of ~8,000 Btu/kWh, which is a very efficient

engine, and more efficient than the CT. This class engine, in “hot start

conditions” (usually defined as lubricating oil preheated, engine bearing

prelubricated, and cooling water preheated) can be started and synchronized to

the grid in ~60 seconds or less and reach full load in ~90 to 180 seconds. The

downside is the extra cost of the generator and switchgear.

The 60-second response of the TPM is based on the engine operating at 75%

load with compressed air bypassing the CT. A “start” signal puts the

compressed air into the CT and increased power is achieved in ~60 seconds in

the CT, about 2.75 MW. The capacitance in the HRSG and steam turbine

system brings the remaining ~0.25 MW along well after the 60-second goal.

Although the data provided did not state the time period, the two figures are

suggestive that the time lag is several minutes, as one would expect.

The report suggested that the average incremental heat rate of the TPM (8,650

Btu/kWh predicted) was 8,495 Btu/kWh based on the full ~3 MW power

increase. However, the fuel flow data taken from station instruments showed

Page 15: Options for optimizing combined cycle plants

significant variation, so it’s best to consider the incremental heat rate as

anecdotal rather than a hard number. Also, for comparison purposes, a more

appropriate incremental heat rate should be based on the CT output alone rather

than the CT plus steam turbine output because of the several-minute time lag of

the steam system.

How does the TurboPHASE stack up against using the same engine in a

standby package for synchronized reserve power? Both packages must be

running, in standby mode, and synchronized to the grid to qualify. However,

the engine-generator can be synchronized, kept at minimum load (lower fuel

consumption), and can take on 2 MW of load within ~30 seconds or so. The

TPM must also be running but held at 75% load in order to add 2.75 MW to the

grid within 60 seconds, but it does so at a higher heat rate than the engine-

generator alone. The economics are very CT and site specific.

Fast Grid Regulation. Once the TurboPHASE is operating, then its response

to rapid changes in grid demand must be considered. Although the specific data

wasn’t available, the TPM response to a step increase in load demand can be

estimated from Figures 3 and 4. The data does confirm that TurboPHASE

responds quickly, with the nearly vertical lines representing the CT response

followed by the slower steam turbine. The data also shows the CT responds in

about 2 to 3 minutes, with the additional steam turbine power available within

10 minutes. The standard PJM response requirement for grid regulation power

is 10 minutes. Regardless, adding the TPM did improve the grid response of the

Morris plant and may allow the plant to move into a grid response category

with a higher payment.

The competitive 2-MW gas-fired engine-generator could also be started,

synchronized, and at maximum load in less than the 10 minutes standard to

supply grid regulation power. But then again, a simple cycle Frame 7FA (227

MW) can start and reach 50% load within 10 minutes and then ramp up at 40

MW/min. Aeroderivative engines start and synchronize even faster.

Black Start Service. The TurboPHASE has the potential to become an

interesting black start option for some utilities with combined cycle plants.

However, it’s difficult to compete with a diesel engine when the weather gets

Page 16: Options for optimizing combined cycle plants

very cold (see “Prepare Your Gas Plant for Cold Weather Operations” in this

issue), particularly when natural gas supplies are limited for power generation

at some gas plants. The best black start systems will be an independent system

that can supply power to just the critical plant systems needed for restart. On

the other hand, a TPM can be installed in two to three months while a new

engine-generator will likely take six months or longer.

Final Analysis

TurboPHASE has the potential for reinvigorating existing combined cycle or

simple cycle plants with additional peaking capacity, especially during warmer

days when the output of the CT is otherwise limited. The response of the

TurboPHASE, from the limited information we have reviewed, is on the same

order as a gas-fired reciprocating engine. Efficiency leans toward the engine-

generator because the combined cycle plant has a higher heat rate. This balance

point could easily change should the TPM be installed on a more efficient CT,

although there aren’t many that CTs with a heat rate less than 8,000 Btu/kWh

(for example, the 60-Hz 7FA is 8,680 Btu/kWh).

On the other hand, the cost of a TPM is likely less than a bank of centrifugal

chillers and coils that are often used to increase CT power output during warm

weather. Also, since the TPM produces compressed air at 300 psi, the system

can be used on any CT with a compressor discharge pressure of 290 psi or less,

which includes many E-, F-, and G-class CTs and some aeroderivative engines,

assuming there is a suitable open port on the casing at the compressor

discharge.

The response of the TurboPHASE does meet the PJM requirements for grid

regulation power but only when the unit is running and the compressor is

charged and ready to dump compressed air into the CT. A potential owner must

consider the economics of balancing the regulation payments from PJM against

the cost of the TPM and the added fuel costs. Also, it probably goes without

saying that potential adopters must be located within an RTO that has a grid

fast regulation payment scheme.

Page 17: Options for optimizing combined cycle plants

What do the OEMs think about an owner adding compressed air into the engine

casing for peaking power or fast regulation purposes? General Electric’s GER-

3567H states, “GE [heavy duty] gas turbines are designed to allow up to 5% of

the compressor airflow for steam injection to the combustor and compressor

discharge.” If superheated steam injection is acceptable to GE, as it has been

for over 30 years, then one would expect that compressed air in like mass flow

will also be acceptable. Also, it seems to me that injecting clean compressed air

upstream of the combustor is certainly preferable to wet compression resulting

from the use of evaporative coolers. ■

— Dr. Robert Peltier, PE is POWER’s consulting editor.