Michael Burke - Director of Process Engineering, Enerfab, Inc.
Transcription
Michael Burke - Director of Process Engineering, Enerfab, Inc.
Kentucky Association of Manufacturers Energy Conference May 14, 2014 Case Study – Executing a 200 kW Combined Heat and Power Project Michael Burke, Andrew Koenig and Mark Linsberg Case Study Overview • • • • • • • • • • • • Project Summary Combined Heat and Power (CHP) Background Concept Development CHP Development Resources Project Timeline Project Site System Design Equipment Construction Completed System Lessons Learned Questions Project Summary • 6 Cylinder 1800 RPM Natural gas reciprocating engine • Energy Input 2,100,000 Btu/hour • Electrical Output 200 kW • Usable hot water output 1,000,000 Btu/hour • Installed at manufacturing facility in Cincinnati, Ohio • Projected 3.5 year payback Combined Heat and Power (CHP) • Also referred to as “Co-Generation” • Combined Heat and Power (CHP) is an efficient and reliable approach to generating electrical and thermal energy from one fuel source. • By recovering the waste heat from electricity production and using it in a facility, fuel utilization efficiencies are greatly increased. 85% - 90% for CHP versus 55% - 60% for conventional generation. • CHP is not a specific technology but an application of technologies to meet an energy users needs. Efficiency Advantage of CHP Typical CHP System Flow Concept Development • 2008 – Ohio SB 221 Enacted – Set Alternative Energy, Renewable Energy and Energy Efficiency Goals • July 2012 – Ohio SB 315 – CHP can be used to meet SB 221 Energy Efficiency Goals • August 2012 Presidential Executive Order – Set Goal 40 gigawatts of new CHP by 2020 • Experience developing, installing and operating a 360 kW packaged natural gas distributed generation unit • Brighton fabrication facility interested in reducing energy costs • Abundance of natural gas from US shale plays North American Shale Plays CHP Development Resources • DSIRE – Database of State Incentives for Renewables and Efficiency – www.dsireusa.org • EPA Combined Heat and Power Partnership – www.epa.gov/chp • USDOE Midwest Clean Energy Application Center – www.midwestcleanenergy.org Project Timeline October 2012 – Developed CHP Project Concept November 2012 – Presented Concept to Executives December 2012 – Received approval to proceed with facility energy audit March 2013 – Completed energy audit supports 210 kW CHP System – Project funding approved April 2013 – Located and acquired packaged CHP unit – began final design, permitting and utility interconnection processes May 2013 – Located and acquired auxiliary equipment Project Timeline - Continued June 2013 – Completed design, obtained building permit, started construction July 2013 – Completed interconnection agreement, completed civil construction August 2013 – Received air permit, completed mechanical construction September 2013 – Completed electrical construction and System Commissioning December 2013 – Ribbon cutting event with proclamation from Ohio Governor Project Site System Design – Electric Load System Design – Thermal Load • Acid Passivation Process in Plant • 1,000,000 Btu water heater used to maintain tank temperature. Project ROI • • • • • • • Facility Electric Cost - $0.095/kWh Facility Gas Cost - $5.00 / MMBtu Minimum Electrical Requirement – 200 KW/h Thermal Demand – 900,000 Btu/h Annual Operating Hours – 8,000 hrs Project Installed Cost - $300,000 Simple Payback – 3.5 yrs Equipment – 210 KW CHP Unit CHP Unit Specifications GridFox 210 Technical Information GridFox 210 Emissions Unit Weight 16,060 lbs NOx 0.15 g/bhp-hr Engine Liebherr TBG 926 CO 0.60 g/bhp-hr Generator Stamford HC 434 E NMCH 0.15 g/bhp-hr Speed 1800 rpm Exhaust Flow 1,750 lbs/hr Fuel Natural Gas Noise Level 70 dBA Voltage / Frequency 480 volts / 60 hz Electric Power 100% Load 210 kW / 252 kVA Energy Input 100% Load 2,100,000 Btu/hr Engine Power 100% Load 295 bhp Hot water out Temperature 185 Deg. F Usable Hot Water Thermal Output 1,100,000 Btu/hr Hot water return Temperature 158 Deg. F Exhaust Gas Temperature 248 Deg. F Inlet Gas Pressure 0.29 - 0.725 psi Equipment - Auxiliary Equipment - Auxiliary Project Construction Project Construction – Cont. Project Construction – Cont. Completed System Completed System – Cont. Project Takeaways • • • • • • • Size the CHP system to match the heating load Do not base project economics on selling electricity back to the utility unless there are attractive net metering tariffs Select equipment suppliers capable of providing field and technical support The CHP project team needs to understand electric supply contracts, gas supply contracts, utility interconnection, air permitting, local permitting, available incentives, project financing, project economics, plc control systems and civil, mechanical and electrical design and construction Be prepared to educate internal and external stakeholders about CHP benefits and limitations Verify existing contracts for electricity allow CHP installation Start the interconnection design and application process as soon as possible Questions? Enerfab 4955 Spring Grove Avenue Cincinnati, Ohio 45232 513-482-7616 www.enerfab.com Michael Burke – [email protected] Andrew Koenig – [email protected]