BCHP_UMASS
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Transcript of BCHP_UMASS
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Building Cooling Heating & Power
Presented By – Nitin Pathakji
Broad USA Inc.
Onsite Generation, Distributed Generation, IES/CHP/CCHP
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BCHP – Unbeatable EfficiencyTaking 30% Efficient Generators to 70% Efficient BCHP Systems
Reducing Building Fossil Energy Requirements by 50%
Peaker, Reliabilityand BCHP
Energy Management, future BCHP and Sell to Grid
Base-load, and Industrial Cooling, Heat and Power
Power Quality and BCHP
Grid Ancillary Services
Remote Power and BCHP
e-
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Bulk Power
e-
A Distributed Energy Future
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Triple-Effect Absorption Chiller
Thermally-Activated HVAC
Technologies
Distributed Generation Technologies
I.C. Engine
Double-Effect AbsorptionWater-Cooled Chiller
Micro-turbine
Solid Oxide Fuel Cell
Commercial Phosphoric Acid Fuel Cell
Single-Effect Absorption Chiller
Residential PEM Fuel Cell
Desiccant Technology
Recoverable Energy Quality (Temperature) and HVAC Technology Match
Gas-turbine
180ºF
360ºF
800ºF
600ºF
Thermally-Activated HVAC Technologies are Key to Improving Overall Efficiency of DG
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CO-GEN CONCEPT
OTHER LOSSES 4.8%
INP
UT
100%
LOSSES25.8%
EXHAUSTLOSSES 21%
THERMALOUTPUT
44.5%
ELECTRICALOUTPUT 29.7%
USEFUL ENERGY74.2%
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Generator Choices & Issues
Design Principle:
“A Generator is a 70% Efficient Boiler with Free Electricity”
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Two Stage Hi-Temp Exhaust Fired
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2-Stage Exhaust Fired Absorber Exhaust from the Gas turbine is taken directly in to the Absorber –
eliminates HRSG and increases capacity.
Concept combines the criteria for HRSG design and LiBr technology.
Major portion of the absorber is standard commercial product design.
Design, development and construction focused on High Stage
Generator and controls.
Primary control of Chiller is leaving Chilled water temperature.
Exhaust flow to the machine is controlled by damper or fan.
Safety Shut down incorporates an inlet damper.
All other machine safeties and control remain same as standard
machine.
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Two Stage Exhaust Fired CT Based CHP P&ID
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Gas Fired Simple Cycle CT BCHP
Generator Model: Taurus 60Exhaust:
Generator Out (C) 486Absorber Out (C) 200
Flow (kg/hr) 79,284Recovered Energy (kcal/hr) 6,054,126
HR Chiller:# Stages 2
Chiller COP 1.3Chiller Capacity % 100
Output (Tons) 2,603Elec Chiller kW/ton 0.6
Effective kW Generated 1562Generator:
Generator Output (kW) 5500Cost per kWh $0.07
BCHP System:Chiller Effective kW 1562
Total Effective kW 7062Effective Cost per kWh $0.05
Waste heat fired absorbers are used to displace electric chiller load.
Typically for multi-MW gas fired simple cycle turbines:
tonnage per MW of exhaust varies from 550 to 700 tons per MW.
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• Burns and McDonnell (Kansas City) teamed with:
– Solar Turbines Inc (San Diego – turbine generator).
– Broad USA (New Jersey – absorption chiller).
• Design and construct a 5.2 MW CHP system.
– Electricity from a Taurus 5,200 kW turbine generator.
– Up to 2,500 refrigeration tons (RT) of free waste heat driven absorption cooling.
– Up to 17,000 RT of additional supplemental gas-fired cooling.
DOE/ORNLBCHP Program
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• Honeywell Laboratories (Minneapolis)
• Developing and field testing a large CHP packaged system.
• A 5 MW turbine generator will be combined with a 1,000 RT absorption chiller.
• The prototype will be tested at Fort Bragg, N.C.
DOE/ORNLBCHP Program
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IFA HSG
DFA HSG
Boiler plant(by others)
Generator
Turbine
Exhaust 1060 0F50,935 lbs/hr
Exhaust 374 0F50,935 lbs/hr
Exhaust
5 kW
Gas in
44/54 0F / 170/150 0F1000 tons / 9,500 MBH
Broad BCHP
Gas in
Exhaust
TRIPLE FUELED BCHP ABSORBER
DOE/ORNL BCHP Program
The absorber is fired with exhaust when the CT is operational and with natural gas or oil if the CT is off. Applications include peaker plants.
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Chiller Performance
IAT (F) 50 70 90 110
Cooling Capacity (TR) 992
Exhaust Flow Available (Lb/hr) 172999 166919 158673 149102
Exhaust Temp (F) 955 966 981 1001 Exhaust flow Required For Chiller (lb/hr)
59485 58449 57049 55280
Estimated P “WC 7.2
Predicted performance only.
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Turbine Inlet Air Cooling
Evaporative Cooling + 3.7 MW
With Inlet Air @ 50 0F Electric Centrifugal + 8.9 MW
Absorption + 11.4 - 11.6 MW
Industrial Turbine 83.5 MW @ Ambient 95 0F
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Integration Schematic of a Microturbine and LiBr Absorption Chiller
127°C (260°F) Flue Gas
Cooling Tower
Absorption Chiller
Microturbine Exhaust Fan
Microturbine
288°C (550°F) Exhaust Gas
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Single Stage Lo-Temp Exhaust Fired
Microturbine
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SS Exhaust Fired Absorber
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Single Stage Exhaust Fired MT Based CHP Layout
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Single Stage Exhaust Fired MT Based CHP P&ID
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BCHP Test Case Profile
University of Maryland
DOE/ORNL
Microturbine/Absorber/Desiccant
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•Turbine efficiency 25.6 %, with chiller 63.5 %, and with desiccant 79.2%
•Single effect absorption chiller with COP of 0.7
67 kW Electric Power
MICRO TURBINE100 kW (340,000*) Exhaust Air@ 500 F
ABSORPTION CHILLER
70 kW (20 tons) Chilled Water
Solid Desiccant System40 kW
(140,000*) Exhaust Air @ 225 F
3000 CFMof Dry Air
* Btu/hr
262 kW(895,000*)
Natural Gas
Air to Zone 1
UMD BCHP System 2Single Stage Lo-Temp Exhaust
Fired
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Equipment
MicroturbineAbsorberCooling Tower
Exhaust Fan
Desiccant on roof
Pumps, Filter, etc.
Single Skid
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Absorption Chiller Data
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Comparative Effects
30% Reduction
Not including input from
Microturbine
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Natural Gas/Exhaust Co-Fired w/HEX
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Installed IES with 60 kW Microturbine and 300 RT Co-fired Double Effect Absorption Chiller
60 kW microturbineExhaust gas duct
High stage generator of 300 RT co-fired double-effect absorption chiller
Natural gas train for co-firing
Flue gas exhaust
Exhaust gas recirculation for ultra low emissions
Exhaust Duct to hot water heat exchanger
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Co-fired Burner Exhaust, FRG (return exhaust for LoNOx) and Fresh Air Intake
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IC Engine BCHP30% Electrical Output, 44% Thermal (jacket & exhaust) HR, 21% Exhaust, 5% Other
OutputSimple HR
185 F
Boost w/ Exhaust
205 F
400 kW
IC Engine
20 Tons
(.05 Tons /kW)
120 Tons
(.30 Tons /kW)
Hot water fired single stage chiller w/ COP = .5 to .7
Dump radiator included
Cooling tower required
Boiler for back-up
Single Stage HW Absorber: Simple & Cost Effective
Two Stage Steam Absorber: Requires HRSG and high pressure steam system. High efficiency but expensive.
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Reciprocating Engine with Jacket Water and Exhaust Recovery and Single-Effect Absorption Chiller
Hot Water “Fired” Single Effect Absorption Water Chiller
81.1 °C (178 °F)
95 °C (203 °F)
93 °C (200 °F)
82 °C (180 °F)
~ 593 °C (~1,100 °F)Exhaust Gas Temp
Exhaust Gas Recovery Heat Exchanger
Jacket Water Heat Recovery Heat Exchanger
86 °C (187 °F)
~ 150 °C (~300 °F)Exhaust Gas to Atmosphere
Hot Water System
Engine Jacket Water System
Engine Exhaust System
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Single Stage HW Fired ICE Based CHP P&ID
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Fuel Cell Characteristics
Fuel Cell Type PAFC SOFC MCFC PEMFC
Commercially Available Yes No No No
Size Range 100-200 kW 1 kW - 10 MW 250 kW - 10 MW 3-250 kW
Efficiency, LHV 36% 45-60% 45-55% 30-40%
CHP Characteristics
(hot water)(hot
water/steam)(hot water,
steam)60°C (140°F)
water
Emissions
Nearly zero Nearly zero Nearly zero Nearly zero
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Fuel Cell BCHP
New technology
High electrical efficiency
Environmentally friendly
Low heat recovery potential
Large footprint
High cost
Hi-Temp FC
0.16 Tons /kW
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IESExhaust Fired or Hot Water Fired
Sites: 20 Ton SS Exhaust Fired w/ Microturbine
25 Ton 2S Exhaust Fired w/ Microturbine
330 Ton 2S Co-Fired w/ Microturbine
2,000 Ton 2S Exhaust Fired w/ Simple Cycle Gas Turbine
130 Ton SS Hot Water Fired w/ 375 kW IC Engine
BCHP Package > Total Components