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Combustion
Repowering  AES Greenidge Units 3 and 4 with APFBC

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Contents:

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Summary
Units 3 and 4 are the last steam turbines installed at AES Greenidge steam power plant.  These units are the focus of this DOE APFBC repowering evaluation.  Information relating to the station and studies includes the following:

  • Space is available to the west, and in the power house.

  • Greenidge Unit 4, on left, is the main focus.  It is a 106.3 MW unit built in 1953.

  • It has a 665,000 pph, 1450 psig / 1000ºF / 1000ºF reheat boiler.

  • The present station heat rate is excellent, 9,676 Btu/kWh HHV (35.3% net plant efficiency).  No scrubber and deep-lake circulating water for condenser cooling.

  • It is one of the earliest dispatched coal units in New York, with a 60.0% average annual capacity factor.

  • Unit 3, a 55.0 MW, 850 psig / 900ºF 1950 non-reheat unit will be considered for use if added output is attractive.

  • Results of the APFBC repowering are reported in Parsons Infrastructure & Technology Group Report No. EJ-9703.

Advanced circulating pressurized fluidized-bed combustion combined cycle (APFBC) technology is a coal-fired technology now under test in large-scale demonstrations, which will be ready for commercial repowering installations around year 2005.  This paper describes a conceptual design evaluation effort that assessed the merits of APFBC repowering the AES Greenidge electric generation plant.  This steam power plant is located near Dresden, New York. The focus of the study is Unit 4 at the station.  Unit 4 is a 108,000 kWe reheat unit that sits on Seneca Lake, one of New York's Finger Lakes.

Earlier APFBC repowering concept evaluations show that APFBC has some important advantages for the power generating company owner.  Output is nearly doubled, environmental performance is excellent, and energy efficiency increases from 4 to 10 percentage points.

For AES Greenidge Unit 4, instead of the large frame gas turbine used in earlier studies, a modified aeroderivative gas turbine, the Rolls-Royce Industrial Trent, is evaluated.  This gas turbine has a significantly higher overall pressure ratio compared to the frame type machines evaluated in the previous studies.  The concept evaluation here considered a 2 x Trent configuration for the repowering of Greenidge Unit 4.

The existing AES Greenidge Unit 4 steam turbine has high flow in its low-pressure section.  This proves a particular challenge for an APFBC repowering, which operates best with most of the feedwater heaters out of service for highest energy efficiency.  However, the existing Unit 4 has a rather high steam turbine exhaust velocity, about 1,264 feet per second, in the exhaust hood in normal operations, so taking feedwater heaters out of service has the undesirable consequence of further increasing exhaust velocity.  Even with significant steam turbine back-end flow limitations, APFBC repowering boosts Unit 4 output from 106,310 kW to 206,300 kW, and the unit is expected to move from its present 34.6 percent HHV net plant energy efficiency to operate at 39.8 percent HHV energy efficiency with APFBC.  Environmental performance is excellent.   Different APFBC integration options can overcome the steam turbine limitations, and produce even higher energy efficiency.  This web site discusses the actions taken to maintain acceptable exhaust conditions.  Different APFBC integration options can overcome the steam turbine limitations and produce even higher energy efficiency.

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Key Features of AES Greenidge APFBC Repowering Project

The photo at the beginning of this web page shows a view of the power plant facing northeast.  Turbine generator Unit 4, a 108 MWe output reheat unit at the left in the photo, is supplied by Boiler No. 6, which uses the stack to the left.  With APFBC repowering, Boiler No. 6 would be replaced by the APFBC equipment, but the turbine/generator and other plant equipment would be retained.

AES Greenidge  is interested in APFBC repowering for the following reasons:

  • APFBC repowering affords the opportunity to increase generation capacity
    and improve heat rate.

  • In a competitive business environment, low price wins.

  • Coal remains an important fuel for AES Greenidge.

  • APFBC is a clean technology, has good cycle efficiency, and has the technology test programs in place to prove its feasibility.

  • Should gas prices increase above projections, coal projects could become more favorable.

AES Greenidge wants to understand this technology better to determine the feasibility of APFBC as a possible next coal-fired unit generation expansion option.

While the concept assessment is still underway, some preliminary observations can be made about possible locations for the APFBC equipment at the site:

  • The APFBC equipment could be placed at the west of the existing equipment, adjacent to Unit 4, to the left of the power house in the photo.

  • There is adequate level space to the west, but several small structures would need to be relocated.

  • The high-energy steam pipe run lengths would be acceptable.

  • Coal delivery could make use of much of the existing coal delivery system.

  • The length of transmission wire to get to the switchyard would be acceptable, and the yard has adequate capacity to distribute the added generation to the high lines.

  • The west end of the coal yard might be used for limestone delivery.

A west-end arrangement is tentatively chosen for APFBC.

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Operating Conditions

The operating conditions for APFBC repowering Greenidge Unit 4 are as follows:

  • Carbonizer temperature: 1700ºF.

  • Fuel gas temperature to filters: 1430ºF.

  • Circulating PFBC bed temperature: 1600ºF.

  • Vitiated air temperature to filters: 1450ºF.

  • Heat recovery steam generator stack temperature: 280ºF.

The estimated performance of the AES Greenidge Unit 4 (Case 2, Unit 3 and Unit 4) repowered in the seven configurations evaluated with APFBC is listed below.  Case 1 was selected as the primary evaluation focus.

 
 

Existing Unit 4

Case 1
Repower
Unit 4
Steam Turbine
SELECTED

 
Gas Turbine Gross Power --- 110,000 kWe
Unit 4 Steam Turbine Gross Power 112,209 105,160 kWe
New Unit 4 Steam Turbine Gross Power --- --- kWe
Unit 3 Steam Turbine Gross Power --- --- kWe
Total Steam Turbine Gross Power 112,209 105,160 kWe
Auxiliary Load -5,899 -7,700 kWe
Net Plant Power 106,310 207,460 kWe
Net Plant Efficiency (HHV) 34.6% 39.9%  
Net Plant Efficiency (LHV) 36.1% 41.7%  
Net Plant Heat Rate (HHV) 9,850 8,536 Btu/kWh
Coal Feed Flow Rate 79,880 134,921 lb/h
Percent of Coal to Carbonizer --- 100%
Percent of Coal to PFBC --- 0%  
Mole % O2 in Vitiated Air --- 12.7%  
Unit 3 Throttle Steam Flow --- --- lb/h
Unit 4 Throttle Steam Flow 745,000 632,000 lb/h
New Unit 4 Throttle Steam Flow --- --- lb/h
Unit 3 Throttle Flow Ratio --- ---  
Unit 4 Throttle Flow Ratio 1.00 0.85  
New Unit 4 Throttle Flow Ratio --- ---  
Unit 3 Steam Turbine Exhaust Velocity --- --- ft/sec
Unit 4 Steam Turbine Exhaust Velocity 1,254 1,247 ft/sec
New Unit 4 Steam Turbine Exhaust Velocity --- --- ft/sec
New 3rd Back End Exhaust Velocity --- --- ft/sec
Unit 4 Feedwater Heaters

No. 1, 2, 3, 4, 5, 6, 7

No. 1

 
Unit 3 Feedwater Heaters

No. 1, 2, 3, 4, 5

---

 
Boost Compressor Driver

N/A

Turbine

 
         
 

Case 2
Repower
Units 3 & 4

Case 3
New Unit 4 LPT

Case 4
Add New
Auxiliary Steam Turbine

 
Gas Turbine Gross Power 110,000 110,000 110,000 kWe
Unit 4 Steam Turbine Gross Power 100,300 106,730 116,630 kWe
New Unit 4 Steam Turbine Gross Power --- --- --- kWe
Unit 3 Steam Turbine Gross Power 14,450 --- --- kWe
Total Steam Turbine Gross Power 114,750 106,730 116,630 kWe
Auxiliary Load -13,460 -7,720 -12,900 kWe
Net Plant Power 211,290 209,020 213,730 kWe
Net Plant Efficiency (HHV) 38.8% 40.3% 41.2%  
Net Plant Efficiency (LHV) 40.4% 41.9% 42.9%  
Net Plant Heat Rate (HHV) 8,802 8,472 8,285 Btu/kWh
Coal Feed Flow Rate 141,695 134,921 134,921 lb/h
Percent of Coal to Carbonizer 95% 100% 100%  
Percent of Coal to PFBC 5% 0% 0%  
Mole % O2 in Vitiated Air 11.8% 12.7% 12.7%  
Unit 3 Throttle Steam Flow 137,730 --- --- lb/h
Unit 4 Throttle Steam Flow 560,000 632,000 665,600 lb/h
New Unit 4 Throttle Steam Flow --- --- --- lb/h
Unit 3 Throttle Flow Ratio 0.24 --- ---  
Unit 4 Throttle Flow Ratio 0.75 0.85 0.89  
New Unit 4 Throttle Flow Ratio --- --- ---  
Unit 3 Steam Turbine Exhaust Velocity 490 --- --- ft/sec
Unit 4 Steam Turbine Exhaust Velocity 1,250 998 635 ft/sec
New Unit 4 Steam Turbine Exhaust Velocity --- --- --- ft/sec
New 3rd Back End Exhaust Velocity --- --- 888 ft/sec
Unit 4 Feedwater Heaters

No. 1, 2, 3

No. 1

No. 1, 2, 3, 4

 
Unit 3 Feedwater Heaters

No. 1, new 2, 3

---

---

 
Boost Compressor Driver

Motor

Turbine

Motor

 
 
         
 

Case 5
New 1800 psig/ 1000oF/1000oF Steam Turbine

Case 6
New 1800 psig/ 1050oF/1050oF Steam Turbine

Case 7
New 1450 psig/ 1000oF/1000oF Steam Turbine

 
Gas Turbine Gross Power 110,000 110,000 110,000 kWe
Unit 4 Steam Turbine Gross Power --- --- --- kWe
New Unit 4 Steam Turbine Gross Power 127,850 129,870 125,900 kWe
Unit 3 Steam Turbine Gross Power --- --- --- kWe
Total Steam Turbine Gross Power 127,850 129,870 125,900 kWe
Auxiliary Load -13,520 -13,420 -13,260 kWe
Net Plant Power 224,330 226,450 222,670 kWe
Net Plant Efficiency (HHV) 41.2% 41.6% 40.9%  
Net Plant Efficiency (LHV) 42.9% 43.3% 42.6%  
Net Plant Heat Rate (HHV) 8,290 8,212 8,352 Btu/kWh
Coal Feed Flow Rate 141,695 141,695 141,695 lb/h
Percent of Coal to Carbonizer 95% 95% 95%  
Percent of Coal to PFBC 5% 5% 5%  
Mole % O2 in Vitiated Air 11.8% 11.8% 11.8%  
Unit 3 Throttle Steam Flow --- --- --- lb/h
Unit 4 Throttle Steam Flow --- --- --- lb/h
New Unit 4 Throttle Steam Flow 715,390 695,100 709,600 lb/h
Unit 3 Throttle Flow Ratio --- --- ---  
Unit 4 Throttle Flow Ratio --- --- ---  
New Unit 4 Throttle Flow Ratio 1.00 1.00 1.00  
Unit 3 Steam Turbine Exhaust Velocity --- --- --- ft/sec
Unit 4 Steam Turbine Exhaust Velocity --- --- --- ft/sec
New Unit 4 Steam Turbine Exhaust Velocity 1,200 1,185 1,204 ft/sec
New 3rd Back End Exhaust Velocity --- --- --- ft/sec
Unit 4 Feedwater Heaters

No. new 1,
new 2, new 3

No. new 1,
new 2, new 3

No. 1, 2, 3

 
Unit 3 Feedwater Heaters

---

---

---

 
Boost Compressor Driver

Motor

Motor

Motor

 

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APFBC Repowered AES Greenidge Unit 4 Plant Process Decisions

A 2 x Trent Configuration Selected
The selected repowering option was to use two APFBC-modified Rolls-Royce Trent gas turbines to repower AES Greenidge Unit 4.

Other Configurations Rejected
A single Trent proved too small to effectively repower AES Greenidge Unit 4.   A 2 x Trent configuration is feasible, and was selected.  It was felt that this made good use of the existing equipment, and had a configuration with good prospects for being cost effective for AES Greenidge.

A 3 x Trent repowering would also be feasible, and in a more detailed concept assessment would deserve consideration.  It was not chosen because it increased complexity and capital costs.  However, if additional coal-fired power were desired, the 3 x Trent configuration would merit further study.

Avoiding Too Much Back-End Steam
The existing Unit 4 steam turbine has high flow in its low-pressure section.   This proves a particular challenge for an APFBC repowering.

For this repowering case, with a 2 x Trent APFBC, it is preferable for best energy efficiency if all feedwater heaters (excepting perhaps the deaerator) are taken out of service.  This makes best use of the low-temperature recovery of heat from the APFBC island and gas turbine heat recovery system.  However, the existing Unit 4 has a rather high steam turbine exhaust velocity, about 1,264 feet per second, in the exhaust hood in normal operations.   If throttle flow were held, and feedwater heaters were taken out of service with APFBC repowering, additional steam would flow through the low-pressure sections, increasing velocity even more, which is undesirable.

Two actions are taken here to avoid overloading the main Unit 4 low-pressure steam turbine:

  • Reduce the total amount of steam passing through the steam turbine by setting the front-end main Unit 4 high-pressure turbine throttle flow ratio to 81 percent.

  • Use extraction steam from the IP/LP crossover to drive an auxiliary condensing steam turbine, which drives the APFBC boost compressor.

These two actions, reducing the throttle flow ratio, and diverting steam to the steam turbine boost compressor driver, reduce the back-end steam hood velocity for the Unit 4 low-pressure turbine to an acceptable value of 1,228 feet per second.

As part of this evaluation process, several alternative uses and integration choices for best use of the steam are under investigation.

Low Vitiated Air Oxygen Percentage Precludes Added Steam Generation
Often it is possible to generate added steam output by supplying additional coal to the PFB combustor.  In this 2 x Trent configuration, however, all of the needs of the PFB combustor are met completely with char from the carbonizer.  The oxygen levels in the topping combustor exhaust are already low (4.5 mole percent) in this configuration, so added steam generation capability would not prove practical.

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Gas Turbine

Two APFBC-modified Rolls-Royce (R-R) industrial Trent engines are used in the DOE conceptual designs to APFBC-repower Greenidge Unit 4.   This gas turbine is an industrial electric power generating aeroderivative of the aircraft Trent engine that powers Airbus and Boeing aircraft.  The first production industrial Trent was delivered in September 1996.  The Trent power generation package is offered by Rolls-Royce as a self-contained electric power generation system that can be used in either simple cycle or heat recovery applications.

Modifications Are Needed for a Natural-Gas-Fueled Gas Turbine Design
for It to Operate in APFBC Service

A natural-gas-fueled gas turbine design will not work in an APFBC system without modification.  Several modifications are needed to the Trent, including the following:

  • Modification is required for collecting and exporting warm compressor discharge air to the APFBC system.

  • The materials, valves, and burners must be modified to accept the import hot syngas and hot vitiated air while supporting the stable low-NOx combustion of these gases throughout the load range.

  • The topping combustor burners need to be capable of startup on natural gas, with a smooth transition to syngas operations as the APFBC system comes online.

  • The system controls must interact reliably and safely with the boost compression system and the APFBC system.

  • While not significantly different from natural gas operations, the materials in the unit must tolerate the low dust, sulfur, and alkali loadings from the APFBC during normal and upset conditions.

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Environmental and Licensing Issues

The table below shows the gaseous emissions comparison for the existing Greenidge Unit 4, and the expected operation with APFBC repowering.  The improvements shown for APFBC repowering are representative of those expected from APFBC.

APFBC-Modified Greenidge Emissions Comparison

Existing Unit: 106,310 kWe / Unit Repowered with APFBC 206,300 kWe

Output

Unmodified Unit 4  

106,310 kW

 
  Repowered with APFBC  

206,300 kW

 
SO2 Unmodified Unit 4

3.52 lb/106 Btu

11,296 tons/y

34.63 lb/MWh

  Repowered with APFBC

0.18 lb/106 Btu

1,158 tons/y

1.51 lb/MWh

NOx Unmodified Unit 4

0.33 lb/106 Btu

1,060 tons/y

3.25 lb/MWh

  Repowered with APFBC

0.30 lb/106 Btu

1,628 tons/y

2.57 lb/MWh

 

APFBC with SNCR

0.10 lb/106 Btu

543 tons/y

0.86 lb/MWh

Particulate Unmodified Unit 4

0.04 lb/106 Btu

128.5 tons/y

0.394 lb/MWh

  Repowered with APFBC

0.002 lb/106 Btu

10.9 tons/y

0.017 lb/MWh

CO2 Unmodified Unit 4

202 lb/106 Btu

648,647 tons/y

1989 lb/MWh

  Repowered with APFBC

202 lb/106 Btu

1,095,572 tons/y

1731 lb/MWh

† Annual emissions are based on an assumed 70 percent capacity factor.