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HomeMy WebLinkAboutCity of Russian Mission Heat Recovery Project Feasibility Study - Jul 2011 - REF Grant 7050844RUSSIAN MISSION, ALASKA HEAT RECOVERY STUDY PREPARED FOR: ALASKA NATIVE TRIBAL HEALTH CONSORTIUM Project ANTHC-09-P52187 PREPARED BY: Alaska Energy and Engineering, Inc. Mailing Address - P.O. Box 111405 Anchorage, AK 99511-1405 (907) 349-0100, 349-8001 FAX e0F De'gC.gS��l &)e * ' 491H On D Devoe. Dee veei e .v a r�ssa ss : ME BB01 00 July 25, 2011 ANTHC-Russian Mission Heat Recovery Analysis July 25, 2011 Alaska Energy and Engineering EXECUTIVE SUMMARY The Water Treatment Plant (WTP) in Russian Mission was evaluated for heat recovery potential. Total estimated annual heating fuel provided by ANTHC is approximately 2,200-gallons. Estimated fuel savings realized by implementing a heat recovery system is 2,200-gallons. The estimated cost for the heat recovery project is $351,929. The AVEC power plant is capable of providing nearly double the amount of recovered heat the Water Treatment Plant requires. Additional facilities near AVEC or the Water Treatment Plant should be evaluated for potential to receive recovered heat to better utilize the available resource. 1.0 INTRODUCTION Alaska Energy and Engineering, Inc. was retained by the Alaska Native Tribal Health Consortium (ANTHC) to review the feasibility of providing available recovered heat from the existing AVEC power plant to the existing water plant in Russian Mission, and provide a budgetary project cost estimate based on Force Account Construction, including Design Engineering and Construction Administration. Additional assumptions have been made in the development of this report including but not limited to the proposed arctic piping routes, building heating loads, and flow rates and pressure drops of the existing power plant cooling system and WTP heating system. It is anticipated that refinements in pipe size and routing, pump and heat exchanger sizing, and other design elements will be required as the project progresses to final design. Available information was obtained from the Alaska Village Electric Cooperative (AVEC) regarding the existing generation equipment. End -user annual fuel use was provided by ANTHC. No site visits were made to confirm accuracy of information obtained. 2.0 OVERVIEW The purpose of this study is to provide an estimate of the heat that can be recovered from the jacket water of the AVEC power plant diesel engines and used to offset heating oil consumption at the WTP. Useable recovered heat is quantified in gallons of heating fuel saved using a gross heating value of 134,000 BTU per gallon of #1 arctic diesel fuel and an overall boiler efficiency of 75% for a net heating value of 100,000 BTU per gallon. The Water Treatment Plant is located 600-feet east of the AVEC power plant. This analysis evaluates the estimated recovered heat available to the Water Treatment Plant. The estimated average annual heating fuel consumption for the WTP is 2200- gallons. 3.0 ESTIMATED RECOVERED HEAT UTILIZATION A heat recovery utilization spreadsheet has been developed to estimate the recoverable heat based on monthly total electric power production, engine heat rates, building heating demand, heating degree days, passive losses for power plant heat and piping, and arctic piping losses. The spreadsheet utilizes assumed time -of -day variations for electric power production and heat demand. Power Cost Equalization data for fiscal year 2009 was used in the spreadsheet. The estimated heat rejection rate for the lead power plant genset, a Detroit Diesel Series 60 DDEC4 1800 rpm genset installed summer of 2010, is used to estimate available recovered heat. Heating degree-days for Russian Mission were used for this site. All exterior power ANTHC-Russian Mission Heat Recovery Analysis July 25, 2011 _ Alaska Energy and Engineering plant hydronic piping is assumed to be 3" pipe with 1" of fiberglass insulation and installed above grade. The AVEC power plant consists of six uninsulated 20-foot connexes arranged in two rows of 3 with a deck between. One row contains the generator module. It is assumed that the radiant heat from the online generator is sufficient to maintain space temperature in the generation module. The other row contains the crew quarters, storage/shop and switchgear controls. This module is heated using recovered heat from the online generator. The heat load of these three uninsulated connexes exceeds the power plant available recovered heat during cold winter months, therefore; to provide useable recovered heat to the water plant, the storage/control/quarters module needs to be insulated. The spreadsheet uses monthly heating degree-days to distribute annual fuel consumption by month. The monthly heat load is then allocated by hour of day using an estimated daily temperature variation (diurnal cycle). The end -user hourly heat load is compared to the hourly available heat from the power plant, less power plant heating loads and parasitic piping losses, and the net delivered heat to the end -user is determined. Following is a summary of annual fuel use and estimated heat utilization in equivalent gallons of fuel for each building: Facility Estimated Annual Estimated Heat * Fuel Use Gallons Delivered Gallons Water Plant 2200 2200 Total 2200 2200 Does not account for peak DHW loads 4.0 HEAT RECOVERY SYSTEM DESCRIPTION AND OPERATION: The heat recovery system captures jacket water heat generated by the AVEC power plant that is currently rejected to the atmosphere by the radiators. Recovered heat is transferred via below grade arctic piping to the Water Plant. The objective is to reduce the consumption of expensive heating fuel by utilizing available recovered heat. Although heat recovery is an excellent method of reducing heating fuel costs, recovered heat is a supplementary heat source and it is imperative that the end - user facility heating systems are operational at all times. Hot engine coolant is piped through a plate heat exchanger located at the power plant. Heat is transferred from the engine coolant to the recovered heat loop without mixing the fluids. The recovered heat fluid is pumped through arctic pipe to the water plant and is tied into the heating system using a plate heat exchanger. AVEC PLANT TIE-IN: No modifications to the AVEC power plant cooling system are included, except those required to tie a new heat exchanger into the plant hydronic system, provide circulating pumps, and install instrumentation. All piping will be insulated with a minimum of 1" insulation and have an aluminum jacket where exposed to the weather. All valves will be either bronze ball valves, or lug style butterfly valves with seals compatible with 50150 glycol/water mixtures at ANTHC-Russian Mission Heat Recovery Analysis July 25, 2011 Alaska Energy and Engineering 200F. Air vents, thermometers, pressure gauges, drain valves and pressure relief valves will also be provided. ARCTIC PIPING (Recovered Heat Loop): The proposed arctic piping is a pre -insulated buried piping system. The piping will be routed from the AVEC plant within existing rights -of -way to the end -user building. The arctic piping system is a pre -insulated, bonded PEX piping system. The pipes consist of Cross -Linked Polyethylene carrier pipe and LDPE outer jacket bonded to polyurethane foam insulation. The carrier piping uses hydraulically pressed bronze or steel couplings, similar to those used in high-pressure hydraulic hoses. The system comes complete with all fittings, tools and accessories required for assembly. The recovered heat fluid will be a 50/50 Propyiene Glycol/Water solution to provide freeze protection to the piping. END -USER BUILDING TIE-INS: End -user building tie-ins typically consist of either brazed plate heat exchangers or cabinet unit heaters. Plate heat exchangers located in the end -user mechanical rooms will be tied into the boiler return piping to pre -heat the boiler water prior to entering the boiler. Where Toyo-style heaters are used, cabinet unit heaters will be located in the occupied space. The maximum anticipated delivered recovered heat supply temperature is about 180F. When there is insufficient recovered heat to meet the building heating load, the building heating system (boiler or heater) will fire and add heat. Typical piping will be type L copper tube with solder joints. Isolation valves will be solder end bronze ball valves or flanged butterfly valves. All piping will be insulated with a minimum of 1" insulation with an all -service jacket. Flexibility will be provided where required for thermal expansion and differential movement. Air vents, thermometers, pressure gauges, drain valves and pressure relief valves will also be provided. RIGHTS -OF -WAY ISSUES: It appears the arctic piping route between the power plant and the WTP is entirely within existing road rights -of -ways, and on City and AVEC property. A Heat Sales / Right -of -Entry Agreement will be required between AVEC and the Alaska Rural Utilities Collaborative (ARUC) to define the parties' responsibilities, the cost of recovered heat, and to authorize the renovation of the power plant heat recovery equipment. 5.0 PRELIMINARY EQUIPMENT SELECTIONS The following initial equipment selections are sized and selected based on preliminary data and will require minor modifications to reflect final design. 3 ANTHC-Russian Mission Heat Recovery Analysis July 25, 2011 Alaska Energy and Engineering 5.1 Heat Exchangers Based on initial selected flow rates, brazed plate heat exchangers appear to be adequate for all locations. Initial heat exchanger selections are as follows. HX-1: (Power Plant). 400 MBH capacity (see note) Primary: 92 GPM 190F EWT (50% ethylene glycol), 2.0 PSI max WPD Secondary: 60 GPM 18OF LWT (50% propylene glycol) 1.0 PSI max WPD HX-2: (Water Treatment Plant). 70 MBH capacity. Primary: 11 GPM 180F EWT (50% propylene glycol), 1.0 PSI max WPD Secondary: 14 GPM 175F LWT (50% propylene glycol) 1.5 PSI max WPD Note: the power plant heat exchanger is sized for future system expansion 5.2 Arctic Piping The length of heat recovery loop piping between the power plant and Water Treatment Plant is approximately 1200-feet, round trip. The arctic piping utilizes 2" PEX to minimize pressure drop and reduce pumping energy. 5.3 Circulating Pumps P-HR1: Heat recovery loop to end -user buildings Flow = 11 GPM, Head = 27' Initial Selection: Grundfos UPS 40-16012. 11 GPM at 27' TDH, 1-112 HP 5.4 Expansion Tank Total heat recovery loop volume is approximately 150-gallons. Pressure relief at the power plant heat exchanger will be 50 PS1G and the maximum normal operating pressure will be 90% of maximum (45 PSIG). ET-1: System requirements: 17.3 gallon tank and 10.6 gallon acceptance Select: Extrol AX-40V, 21.7 gallon tank and 11.3 gallon acceptance 6.0 CONCLUSIONS AND RECOMMENDATIONS Estimated construction costs were determined based on prior recent heat recovery project experience, and include materials, equipment, freight, labor, design, construction management, and startup and testing. All work at the power plant and water treatment plant, and design and construction management/administration for the project is included (refer to attached cost estimate). The estimated project cost for is $351,929. Estimated fuel savings are about 2,200- gallons. Using an assumed fuel price of $5.001galion results in estimated savings of $11,000 for a simple payback of 32-years. The AVEC power plant has the capability of providing nearly double the amount of recovered heat the Water Treatment Plant requires. 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