HomeMy WebLinkAboutWood Heat Copper Center Kenny Lake Preliminary Feasibility Assessment DanielParrent JEDC AWEDTG 03-01-2006
Preliminary Feasibility Assessment for High
Efficiency, Low Emission Wood Heating
In Copper Center and Kenny Lake, Alaska
Prepared for:
James Elliott, PhD., Superintendent
Copper River School District
Glennallen, Alaska
Prepared by:
Daniel Parrent,
Wood Utilization Specialist
Juneau Economic Development Council
Notice
This Preliminary Feasibility Assessment for High Efficiency, Low Emission Wood Heating was prepared by
Daniel Parrent, Wood Utilization Specialist, Juneau Economic Development Council for James Elliott, PhD,
Superintendent, Copper River School District. This report does not necessarily represent the views of the
Juneau Economic Development Council (JEDC). JEDC, its Board, employees, contractors, and
subcontractors make no warranty, express or implied, and assume no legal liability for the information in this
report; nor does any party represent that the use of this information will not infringe upon privately owned
rights. This report has not been approved or disapproved by JEDC nor has JEDC passed upon the accuracy
or adequacy of the information in this report.
Funding for this report was provided by USDA Forest Service, Alaska Region,
Office of State and Private Forestry
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Table of Contents
Abstract
Section 1. Executive Summary
1.1 Goals and Objectives
1.2 Evaluation Criteria, Project Scale, Operating Standards, General Observations
1.3 Assessment Summary and Recommended Actions
1.3.1 Copper River School
1.3.2 Kenny Lake School
Section 2. Evaluation Criteria, Implementation, Wood Heating Systems
2.1 Evaluation Criteria
2.2 Successful Implementation
2.3 Classes of Wood Heating Systems
Section 3. The Nature of Wood Fuels
3.1 Wood Fuel Forms and Current Utilization
3.2 Heating Value of Wood
Section 4. Wood Fueled Heating Systems
4.1 Low Efficiency High Emission Cordwood Boilers
4.2 High Efficiency Low Emission Cordwood Boilers
4.3 Bulk Fuel Boiler Systems
Section 5. Selecting the Appropriate System
5.1 Comparative Costs of Fuels
5.2(a) Cost per MMBtu Sensitivity – Cordwood
5.2(b) Cost per MMBtu Sensitivity – Bulk Fuels
5.3 Determining Demand
5.4 Summary of Findings
Section 6. Economic Feasibility of Cordwood Systems
6.1 Initial Investment Cost Estimates
6.2 Operating Parameters of HELE Cordwood Boilers
6.3 Hypothetical OM&R Cost Estimates
6.4 Calculation of Financial Metrics
6.5 Simple and Modified Simple Payback Period for Small and Large HELE Cordwood Boilers
6.6 Present Value, Net Present Value and Internal Rate of Return Values for Small and
Large HELE Cordwood Boilers
6.7 Life Cycle Cost Analysis
6.7.1 Copper Center School
6.7.2 Kenny Lake School
Section 7. Economic Feasibility of Bulk Fuel Systems
7.1 Capital Cost Components
7.2 Generic OM&R Cost Allowances
7.3 Calculation of Financial Metrics
7.4 Simple and Modified Simple Payback Period for Generic Bulk Fuel Boilers
7.5 Present Value, Net Present Value and Internal Rate of Return Values for Bulk Fuel Boilers
Section 8. Conclusions
8.1 Small Applications – Copper River School
8.2 Large Applications – Kenny Lake School
Footnotes
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Appendix A AWEDTG Evaluation Criteria
Appendix B Recoverable Heating Value Determination
Appendix C List of Abbreviations and Acronyms
Appendix D Wood Fuel Properties
Appendix E Financial Metrics
Appendix F Operational Parameters of HELE Cordwood Boilers
Appendix G Calculation of Present Value, Net Present Value and Internal Rate of Return
Appendix H Garn Boiler Specifications
Appendix I Copper River School Field Inspection Report
Appendix J Kenny Lake School Field Inspection Report
List of Tables and Figures
Table 4-1 HELE Cordwood Boiler Suppliers
Table 4-2 Emissions from Wood Heating Appliances
Table 4-3 Bulk Fuel Boiler System Vendors
Table 4-4 Bulk Fuel Boilers in Alaska
Table 5-1 Comparative Cost of Fuel Oil vs. Wood Fuels
Figure 5-1 Effect of White Spruce Cordwood (MC30) Cost on Cost of Delivered Heat
Figure 5-2 Effect of White Spruce Bulk Fuel (MC40) Cost on Cost of Delivered Heat
Table 5-2 Reported Annual Fuel Oil Consumption, CRSD Facilities
Table 5-3 Estimate of Heat Required in Coldest 24 Hr Period
Table 5-4 Estimate of Total Wood Consumption, Comparative Costs and Potential Savings
Table 6-1 Initial Investment Cost Scenarios for Hypothetical Cordwood Systems
Table 6-2 Labor/Cost Estimates for HELE Cordwood Systems
Table 6-3 Summary of Total Annual OM&R Cost Estimates
Table 6-4 Simple and Modified Simple Payback Period Analysis for HELE Cordwood Boilers
Table 6-5 PV, NPV and IRR Values for HELE Cordwood Boilers
Table 6-6 Life Cycle Costs of Copper Center School Project Alternatives
Table 6-7 Life Cycle Costs of Kenny Lake School Project Alternatives
Table 7-1 Initial Investment Cost Components for Bulk Fuel Systems
Table 7-2 Darby, MT Public School Wood Chip Boiler Costs
Table 7-3 Characteristics of Biomass Boiler Projects
Table 7-4 Cost Breakdown for the Least Expensive Wood Chip Boiler System Installed in a New Free-
Standing Building
Table 7-5 Total OM&R Cost Allowances for a Bulk Fuel System
Table 7-6 Simple and Modified Simple Payback Period Analysis
Table 7-7 PV, NPV and IRR Values for Bulk Fuel Systems
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Key words: HELE, LEHE, bulk fuel, cordwood
ABSTRACT
The potential for heating the school facilities at Copper Center and Kenny Lake with high
efficiency, low emission (HELE) wood boilers is evaluated for the Copper River School District
(CRSD).
Early in 2006, organizations were invited to submit a Statement of Interest (SOI) to the Alaska
Wood Energy Development Task Group (AWEDTG). Task Group members reviewed all the SOIs
and selected projects for further review based on the selection criteria presented in Appendix A.
AWEDTG representatives visited Copper Center and Kenny Lake during the summer of 2006 and
information was obtained for each facility. Preliminary assessments were made and challenges
identified. Potential wood energy systems were considered for each project using AWEDTG,
USDA and AEA objectives for energy efficiency and emissions. Preliminary recommendations are
made for each facility.
SECTION 1. EXECUTIVE SUMMARY
1.1 Goals and Objectives
• Identify CRSD school facilities in Copper Center and Kenny Lake as potential candidates
for heating with wood
• Evaluate the suitability of the facility(s) and site(s) for siting a wood-fired boiler
• Assess the type(s) and availability of wood fuels
• Size and estimate the capital costs of suitable wood-fired system(s)
• Estimate the annual operation and maintenance costs of a wood-fired system
• Estimate the potential economic benefits from installing a wood-fired heating system
1.2 Evaluation Criteria, Project Scale, Operating Parameters, General Observations
• All projects meet the AWEDTG objectives for petroleum fuel displacement, use of
hazardous forest fuels or forest treatment residues, sustainability of the wood supply,
project implementation, operation and maintenance, and community support
• Wood-fired systems are not feasible for very small applications. These may be satisfied
with domestic wood appliances, such as wood stoves or pellet stoves/furnaces
• Facilities consuming less than 2,000 gallons per year represent minimal savings with
wood-fired systems unless such systems can be enclosed in an existing structure, and wood
and labor are very low cost or free
• Marginal economic metrics (such as those associated with small installations) can be
improved with low-cost buildings and piping systems
• Medium and large energy consumers have the best potential for feasibly implementing a
wood energy system and deserve detailed engineering analysis
• Efficiency and emissions standards for Outdoor Wood Boilers (OWB) changed in
October 2006, which could increase costs for small systems
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1.3 Assessment Summary and Recommended Actions
1.3.1 Copper Center School
• Overview. The Copper Center School was built in 1985 and provides instruction for
students in grades K through 6. The facility consists of one main building and two small
satellite classrooms immediately adjacent to the main building. All facilities appeared to
be well-maintained and in good condition.
In the main building heat is provided by a pair of Weil-McLain hot air furnaces (located in
a mechanical room in the mezzanine above the first floor) capable of delivering a
maximum of 526,000 Btu/hr (net, combined). Each of the satellite buildings has a small
hot air furnace rated at about 112,000 Btu/hr (net). None of the buildings has a hydronic
heating system.
The topography around the school is gentle, presenting no readily apparent physical
impediments to an external boiler installation. There are several potential sites for a wood-
fueled boiler within reasonable distances to the school buildings.
• Fuel consumption. Altogether, the reported total fuel consumption estimate is 6,000
gallons of fuel oil per year.
• Potential savings. At $2.90 per gallon and 6,000 gallons of fuel oil per year, CRSD pays
$17,400 per year for fuel oil. The high-efficiency, low-emission (HELE) fuel equivalent of
6,000 gallons of fuel oil is about 60 cords, and at $100/cord represents a potential gross
annual fuel cost savings of about $11,400.
• Required boiler capacity. The estimated required boiler capacity (RBC) to heat the
Copper Center School is 207,500 Btu/hr during the coldest 24-hour period. It would appear
that a single HELE cordwood boiler could supply 100% of that RBC with a margin similar
to that of oil and/or gas fired furnaces or boilers.
• Recommended action regarding a bulk fuel wood system. Due to its small heating
demand, a “bulk fuel” system is not feasible for the CRSD Copper Center School.
• Recommended action regarding a cordwood system. Two hypothetical boiler
installations were compared: one medium boiler (Garn WHS 2000, rated at 425,000
Btu/hr) and one large boiler (Garn WHS 3200, rated at 950,000 Btu/hr). Under the stated
assumptions and estimated costs, neither option was cost-effective; net present value was
still negative at 20 years and internal rates of return, while positive, were low at
approximately 0.5% and 1% respectively. However, this is a preliminary assessment; fuel
oil prices are not static and annual savings are therefore likely to increase. Closer scrutiny
by a professional engineer is warranted.
1.3.2 Kenny Lake School
• Overview. The Kenny Lake School (slab on grade construction) underwent extensive
remodeling in 2006 and provides K through 12 instruction for 135 students. The facility
consists of one large main building and several utility “outbuildings”. The community
library is also located nearby.
Heat is provided by two oil-fired Burnham boilers rated at 1.87 million Btu/hr (net, each),
located in a single mechanical room at the rear of the main building. Heat is delivered via
a hydronic heating system, with some supplemental hot air.
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The topography around the school is gentle, presenting no apparent physical impediments
to an external boiler installation. There are two potential sites for a wood-fueled boiler
within reasonable distances to the school buildings.
• Fuel Consumption. The Kenny Lake School can be considered a relatively large energy
consumer, given a reported annual fuel consumption estimate of 20,000 gallons of fuel oil.
• Potential Savings. At $2.90 per gallon and 20,000 gallons of fuel oil per year, the school
pays $58,000 per year for fuel oil. The HELE cordwood fuel equivalent of 20,000 gallons
of fuel oil is 200 cords, and at $100/cord represents a potential gross annual fuel cost
savings of $38,000.
• Required boiler capacity. The estimated required boiler capacity (RBC) to heat the Kenny
Lake School is 690,400 Btu/hr during the coldest 24-hour period. A single 950,000 Btu/hr
HELE cordwood boiler operated at maximum capacity could, theoretically, supply 100%
of that RBC and provide a significant annual economic benefit.
• Recommended action regarding a bulk fuel wood system. A “bulk fuel” system is not
financially feasible for the Kenny Lake School, given the likely cost and projected savings.
• Recommended action regarding a cordwood system. The financial metrics of installing a
single large HELE cordwood boiler are strongly positive, with a simple payback period
under 6 years. Net present value becomes positive at year 10 and the internal rate of return
at 20 years is 10.63%.
The financial metrics of installing two large HELE cordwood boilers was also considered
for reasons of practicality. Under this scenario, the simple payback period is about 8 years.
Net present value becomes positive at year 14, and the internal rate of return at 20 years is
6.64%
Further Design and Engineering for a HELE cordwood system for the Kenny Lake School
is warranted.
SECTION 2. EVALUATION CRITERIA, IMPLEMENTATION, WOOD HEATING SYSTEMS
The approach being taken by the Alaska Wood Energy Development Task Group (AWEDTG)
regarding biomass energy heating projects follows the recommendations of the Biomass Energy
Resource Center (BERC), which advises that, “[T]he most cost-effective approach to studying the
feasibility for a biomass energy project is to approach the study in stages.” Further, BERC advises
“not spending too much time, effort, or money on a full feasibility study before discovering whether
the potential project makes basic economic sense” and suggests, “[U]ndertaking a pre-feasibility
study . . . a basic assessment, not yet at the engineering level, to determine the project's apparent
cost-effectiveness”. Biomass Energy Resource Center, Montpelier, Vermont. www.biomasscenter.org
2.1 Evaluation Criteria
The AWEDTG selected projects for evaluation based on the criteria listed in Appendix A. Both of
the Copper River School District projects meet the AWEDTG criteria for potential petroleum fuel
displacement, use of forest residues for public benefit, use of local residues (though limited),
sustainability of the wood supply, project implementation, operation and maintenance, and
community support.
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In the case of cordwood boiler applications, the wood supply from forest fuels or local processing
residues appears adequate and matches the applications. Currently, “bulk fuel” (chips, bark,
sawdust, etc.) supplies are very limited.
2.2 Successful Implementation
In general, three aspects of project implementation have been important to wood energy projects in
the past: clear identification of a sponsoring agency/entity, dedication of personnel, and a reliable
and consistent supply of fuel.
In situations where several organizations are responsible for different community services, it must
be clear which organization would sponsor or implement a wood-burning project. (NOTE: This is
not necessarily the case with either of the CRSD facilities, but the issue must be addressed.)
Boiler stoking and/or maintenance is required for approximately 9-15 minutes per boiler several
times a day (depending on the heating demand) for manual wood-fueled systems, and dedicating
personnel for the operation is critical to realizing savings from wood fuel use. For this report, it is
assumed that new personnel would be hired or existing personnel would be assigned as necessary,
and that “boiler duties” would be included in the responsibilities and/or job description of facilities
personnel.
The forest industry infrastructure in the Copper River Valley is small, but appears to be stable. For
this report, it is assumed that wood supplies are sufficient.
2.3 Classes of Wood Energy Systems
There are, basically, two classes of wood energy systems: manual cordwood systems and
automated “bulk fuel” systems. Cordwood systems are generally appropriate for applications
where the maximum heating demand ranges from 100,000 to 1,000,000 Btu per hour, although
smaller and larger applications are possible. “Bulk fuel” systems are systems that burn wood chips,
sawdust, bark/hog fuel, shavings, pellets, etc. They are generally applicable for situations where the
heating demand exceeds 1 million Btu per hour, although local conditions, especially fuel
availability, can exert strong influences on the feasibility of a bulk fuel system.
Usually, an automated bulk fuel boiler is tied-in directly with the existing oil-fired system. With a
cordwood system, glycol from the existing oil-fired boiler system would be circulated through a
heat exchanger at the wood boiler ahead of the existing oil boiler. A bulk fuel system is usually
designed to replace 100% of the fuel oil used in the oil-fired boiler, and although it is possible for a
cordwood system to be similarly designed, they are usually intended as a supplement, albeit a large
supplement, to an oil-fired system. In either case, the existing oil-fired system would remain in
place and be available for peak demand or backup in the event of a failure or other downtime
(scheduled or unscheduled) in the wood system.
One of the objectives of the AWEDTG is to support projects that would use energy-efficient and
clean burning wood heating systems, i.e., high efficiency, low emission (HELE) systems.
SECTION 3. THE NATURE OF WOOD FUELS
3.1 Wood Fuel Forms and Current Utilization
Wood fuels in south-central Alaska are most likely to be in the form of cordwood and/or large,
unprocessed sawmill residues, primarily slabwood. Sawdust and planer shavings currently supply
the limited demand for bulk fuel in the immediate area. Other than sawdust and shavings, there is
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relatively little bulk fuel available. In the recent past, a whole tree harvesting and chipping
operation took place near Glennallen, but that is no longer the case. And while there has been some
discussion of building a pellet plant in the area, it does not currently exist and therefore pellets
were not considered as a viable fuel option.
3.2 Heating Value of Wood
Wood is a unique fuel whose heating value is quite variable, depending on species of wood,
moisture content, and other factors. There are also several ‘heating values’ (high heating value
(HHV), gross heating value (GHV), recoverable heating value (RHV), and deliverable heating
value (DHV)) that may be assigned to wood at various stages in the calculations.
For this report, white spruce cordwood at 30 percent moisture content (MC30) and white spruce
bulk fuel at 40 percent moisture content (MC40), calculated on the green wet weight basis (also
called wet weight basis), are used as benchmarks.
The HHV of white spruce at 0% moisture content (MC0) is 8,890 Btu/lb1. The GHV at 30%
moisture content (MC30) is 6,223 Btu/lb, and the GHV at 40% moisture content (MC30) is 5,334
Btu/lb.
The RHV for cordwood (MC30) is 14,860,000 Btu per cord, and the DHV, which is a function of
boiler efficiency (assumed to be 75%), is 11,145,000 Btu per cord. The delivered heating value of
1 cord of white spruce cordwood (MC30) equals the delivered heating value of 101 gallons of #2
fuel oil when burned at 75% conversion efficiency.
The RHV for bulk fuel (MC40) is 7,360,000 Btu per ton, and the DHV, which is a function of
boiler efficiency (assumed to be 70%), is 5,150,000 Btu per ton. The delivered heating value of
1 ton of white spruce bulk fuel (MC40) equals the delivered heating value of 46.7 gallons of #2
fuel oil when burned at 70% conversion efficiency.
A more thorough discussion of the heating value of wood can be found in Appendix B and
Appendix D.
SECTION 4. WOOD-FUELED HEATING SYSTEMS
4.1 Low Efficiency High Emission (LEHE) Cordwood Boilers
Most manual outdoor wood boilers (OWBs) that burn cordwood are relatively low-cost and can
save fuel oil but have been criticized for low efficiency and smoky operation. These could be called
low efficiency, high emission (LEHE) systems and there are dozens of manufacturers. The State of
New York recently instituted a moratorium on new LEHE OWB installations due to concerns over
emissions and air quality5. Other states are also considering regulations6,7,8,9. Since there are no
standards for OWBs (“boilers” and “furnaces” were exempted from the 1988 EPA regulations10),
OWB ratings are inconsistent and can be misleading. Standard procedures for evaluating wood
boilers do not exist, but test data from New York, Michigan and elsewhere showed a wide range of
apparent [in]efficiencies and emissions among OWBs.
In 2006, a committee was formed under the American Society for Testing and Materials (ASTM)
to develop a standard test protocol for OWBs11. The standards included uniform procedures for
determining performance and emissions. Subsequently, the ASTM committee sponsored tests of
three common outdoor wood boilers using the new procedures. The results showed efficiencies as
low as 25% and emissions more than nine times the standard for industrial boilers. Obviously,
these results were deemed unsatisfactory and new standards were called for.
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In a news release dated January 29, 200712, the U.S. Environmental Protection Agency announced
a new voluntary partnership agreement with 10 major OWB manufacturers to make cleaner-
burning appliances. The new phase-one standard calls for emissions not to exceed 0.60 pounds of
particulate emissions per million Btu of heat input. The phase-two standard, which will follow 2
years after phase-one, will limit emissions to 0.30 pounds per million Btus of heat delivered,
thereby creating an efficiency standard as well.
To address local and state concerns over regulating OWB installations, the Northeast States for
Coordinated Air Use Management (NeSCAUM), and EPA have developed model regulations that
recommend OWB installation specifications, clean fuel standards and owner/operator training.
(http://www.epa.gov/woodheaters/ and http://www.nescaum.org/topics/outdoor-hydronic-heaters)
Implementation of the new standard will improve air quality and boiler efficiency but will also
increase costs as manufacturers modify their designs, fabrication and marketing to adjust to the
new standards. Some low-end models will no longer be available.
4.2 High Efficiency Low Emission (HELE) Cordwood Boilers
In contrast to low efficiency, high emission cordwood boilers there are a few units that can
correctly be considered high efficiency, low emission (HELE). These systems are designed to burn
cordwood fuel cleanly and efficiently.
Table 4-1 lists four HELE boiler suppliers, two of which have units operating in Alaska. HS Tarm
Co./Tarm USA, Inc. has a number of residential units operating in Alaska, and a Garn boiler
manufactured by Dectra Corporation is used in Dot Lake, AK to heat several homes and the
washeteria, replacing 7,000 gallons per year (gpy) of #2 fuel oil.14 Two Garn boilers were recently
installed in Tanana, AK to provide heat to the washeteria and water plant.
Table 4-1. HELE Cordwood Boiler Suppliers
Btu/hr ratings Supplier
EKO-Line 85,000 to 275,000 New Horizon Corp
www.newhorizoncorp.com
Tarm 100,000 to 198,000 HS Tarm/Tarm USA
www.tarmusa.com/wood-gasification.asp
Greenwood 100,000 to 300,000 Greenwood
www.GreenwoodFurnace.com
Garn 350,000 to 950,000 Dectra Corp.
www.dectra.net/garn
Note: Listing of any manufacturer, distributor or service provider does not constitute an endorsement.
Table 4-2 shows the results for a Garn WHS 1350 boiler that was tested at 157,000 to 173,000
Btu/hr by the State of Michigan using the new ASTM testing procedures, compared with EPA
standards for wood stoves and boilers. It is important to remember that wood fired boilers are not
entirely smokeless; even very efficient wood boilers may smoke for a few minutes on startup.4,15
10
Table 4-2. Emissions from Wood Heating Appliances
Appliance Emissions (grams/1,000 Btu delivered)
EPA Certified Non Catalytic Stove 0.500
EPA Certified Catalytic Stove 0.250
EPA Industrial Boiler (many states) 0.225
GARN WHS 1350 Boiler* 0.179
Source: Intertek Testing Services, Michigan, March 2006.
Note: *With dry oak cordwood; average efficiency of 75.4% based upon the high heating value (HHV) of wood
Cordwood boilers are suitable for applications from 100,000 Btu/hr to 1,000,000 Btu/hr, although
both larger and smaller applications are possible.
4.3 Bulk Fuel Boiler Systems
Commercial bulk fuel systems are generally efficient and meet typical federal and state air quality
standards. They have been around for a long time and there is little new technological ground to
break when installing one. Efficient bulk fuel boilers typically convert 70% of the energy in the
wood fuel to hot water or low pressure steam when the fuel moisture is less than 40% moisture
content (MC40, calculated on a wet basis).
Most vendors provide systems that can burn various bulk fuels (wood chips, sawdust, wood pellets
and hog fuel), but each system, generally, has to be designed around the predominant fuel form. A
system designed to burn clean chips will not necessarily operate well on a diet of hog fuel, for
example. And most vendors will emphasize the need for good quality wood fuel and a consistent
source of wood fuel, i.e., fuel with consistent size and moisture content from a common source is
considerably more desirable than variations in chip size or moisture content. Table 4-3 presents a
partial list of bulk fuel boiler system vendors.
Table 4-3. Bulk Fuel Boiler System Vendors
Decton Iron Works, Inc
Butler, WI
(800) 246-1478
www.decton.com
New Horizon Corp.
Sutton, WV
(877) 202-5070
www.newhorizoncorp.com
Messersmith Manufacturing, Inc.
Bark River, MI
(906) 466-9010
www.burnchips.com
JMR Industrial Contractors
Columbus, MS
(662) 240-1247
www.jmric.com
Chiptec Wood Energy Systems
South Burlington, VT
(800) 244-4146
www.chiptec.com
Note: Listing of any manufacturer, distributor or
service provider does not constitute an endorsement
Bulk fuel systems are available in a range of sizes between 300,000 and 60,000,000 Btu/hr.
However, the majority of the installations range from 1 MMBtu/hr to 20 MMBtu/hr. Large energy
consumers, consuming at least 40,000 gallons of fuel oil per year, have the best potential for
installing bulk fuel boilers and may warrant detailed engineering analysis. Bulk fuel systems with
their storage and automated fuel handling conveyances are generally not cost-effective for smaller
applications.
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Although there are several options, bulk fuel (chips, sawdust, bark, shavings, etc.) is best delivered
in self-unloading tractor-trailer vans that hold about 22 to 24 tons of material. A facility such as
the Kenny Lake School, replacing 20,000 gallons of fuel oil with white spruce bulk fuel (MC40)
would use an estimated 428 tons per year, or about 20 tractor-trailer loads spread out over the
school year.
There are three known bulk fuel boilers in Alaska (Table 4-4), all of which are installed at
sawmills. The most recent was installed in Hoonah in 2006. A 4 MMBtu/hr wood chip boiler is
under construction at the Craig Aquatic Center to replace the equivalent of 36,000 gallons of fuel
oil per year. It is similar in size to boilers recently installed in Montana schools.
Table 4-4. Bulk Fuel Boilers in Alaska
Installation Boiler
Horsepower* MMBtu/hr Heating
Degree Days** Supplier
Craig Aquatic Center
Craig, AK 120 4 7,209a Chiptek
Icy Straits Lumber & Milling
Hoonah, AK 72 2.4 8,496b Decton
Regal Enterprises
Copper Center, AK N/A N/A 13,486c Messersmith
Logging & Milling Associates
Delta Junction, AK N/A 2 12,897d Decton
Notes:
* Heat delivered as hot water or steam. 1 Boiler Horsepower = 33,475 Btu/hr or 34.5 pounds of water at a temperature of
100°C (212°F) into steam at 212°F
** assumes base = 65o F
a NOAA, July 1, 2005 through June 30, 2006, Ketchikan data
b NOAA, July 1, 2005 through June 30, 2006, Average of Juneau and Yakutat data
c NOAA, July 1, 2005 through June 30, 2006, Gulkana data
d NOAA, July 1, 2005 through June 30, 2006, Big Delta data
ftp://ftp.cpc.ncep.noaa.gov/htdocs/products/analysis_monitoring/cdus/degree_days/archives/Heating%20degree%20Days/Monthly%20City/2006/jun%202006.txt
Bulk fuel systems are discussed in greater detail in Section 7.
SECTION 5. SELECTING THE APPROPRIATE SYSTEM
Selecting the appropriate heating system is, primarily, a function of heating demand. It is generally
not feasible to install automated bulk fuel systems in/at small facilities, and it is likely to be
impractical to install cordwood boilers at very large facilities. Other than demand, system choice
can be limited by fuel (form) availability, labor, financial resources, and limitations of the site.
The selection of a wood-fueled heating system has an impact on fuel economy. Potential savings
in fuel costs must be weighed against initial investment costs and ongoing operating, maintenance
and repair (OM&R) costs. Wood system costs include the initial capital costs of purchasing and
installing the equipment, non-capital costs (engineering, permitting, etc.), the cost of the fuel
storage building and boiler building (if required), the financial burden associated with loan interest,
the fuel cost, and the other costs associated with operating and maintaining the heating system,
especially labor.
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5.1 Comparative Costs of Fuels
Table 5-1 compares the cost of #2 fuel oil to white spruce cordwood (MC30) and white spruce bulk
fuel (MC40). In order to make reasonable comparisons, costs are calculated on a “per million Btu
(MMBtu)” basis.
Table 5-1. Comparative Cost of Fuel Oil vs. Wood Fuels
FUEL RHVa (Btu) Conversion
Efficiencya DHVa (Btu) Price per unit
($)
Cost per MMBtu
(delivered, ($))
3.00/gal 27.17
3.50 31.70 Fuel oil, #2,
1 gallon 138,000 80% 110,400
per gallon 4.00 36.23
100/cord 8.97
125 11.22 White spruce,
1 cord, MC30 14,860,000 75% 11,145,000
per cord 150 13.46
30/ton 5.82
40 7.76 White spruce
1 ton, MC40 7,360,000 70% 5,152,000
per ton 50 9.70
Notes:
a from Appendix D
5.2(a) Cost per MMBtu Sensitivity – Cordwood
Figure 5-1 on the next page illustrates the relationship between the price of white spruce cordwood
(MC30) and the cost of delivered heat, (the slanted line). For each $10 per cord increase in the
price of cordwood, the cost per million Btu increases by about $0.90. The chart assumes that the
cordwood boiler delivers 75% of the RHV energy in the cordwood to useful heat and that oil is
converted to heat at 80% efficiency. The dashed lines represent fuel oil at $3.00, $3.50 and $4.00
per gallon ($27.17, $31.70 and $36.23 per million Btu respectively).
At high efficiency heat from white spruce cordwood (MC30) at $302.80 per cord is equal to the
cost of oil at $3.00 per gallon, before considering the cost of the equipment and operation,
maintenance and repair (OM&R) costs. At 75% efficiency and $125 per cord, a high-efficiency
cordwood boiler will deliver heat at about 41% of the cost of fuel oil at $3.00 per gallon ($11.22
versus $27.17 per MMBtu). Figure 5-1 indicates that, at a given efficiency, savings increase
significantly with decreases in the delivered price of cordwood and/or with increases in the price of
fuel oil.
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Cost ($) per MMBtu as a Function of
Cordwood Cost
0.00
5.00
10.00
15.00
20.00
25.00
30.00
35.00
40.00
100 125 150 175 200 225 250 275 300 325 350 375 400
Cordwood cost, $ per cordCost ($) per MMBtu
Fuel Oil at $4.00 per gallon
Fuel Oil at $3.50 per gallon
Fuel Oil at $3.00 per gallon
Figure 5-1. Effect of White Spruce Cordwood Price on Cost of Delivered Heat
5.2(b) Cost per MMBtu Sensitivity – Bulk Fuels
Figure 5-2 on the next page illustrates the relationship between the price of white spruce bulk fuel
(MC40) and the cost of delivered heat, (the slanted line). For each $10 per ton increase in the price
of bulk fuel, the cost per million Btu increases by about $1.94. The chart assumes that the bulk
fuel boiler converts 70% of the RHV energy in the wood to useful heat and that fuel oil is
converted to heat at 80% efficiency. The dashed lines represent fuel oil at $3.00, $3.50 and $4.00
per gallon ($27.17, $31.70 and $36.23 per million Btu respectively).
At high efficiency, heat from white spruce bulk fuel (MC40) at $140 per ton is equal to the cost of
oil at $3.00 per gallon, before considering the investment and OM&R costs. At 70% efficiency and
$40/ton, an efficient bulk fuel boiler will deliver heat at about 28.6% of the cost of fuel oil at $3.00
per gallon ($7.76 versus $27.17 per MMBtu), before considering the cost of the equipment and
OM&R. Figure 5-2 shows that, at a given efficiency, savings increase significantly with decreases
in the delivered price of bulk fuel and/or with increases in the price of fuel oil.
14
Cost ($) per MMBtu as a Function of
Bulk Fuel Cost
0.00
5.00
10.00
15.00
20.00
25.00
30.00
35.00
30 45 60 75 90 105 120 135 150 165
Bulk fuel cost, $ per tonCost ($) per MMBtu
Fuel Oil at $4.00 per gallon
Fuel Oil at $3.50 per gallon
Fuel Oil at $3.00 per gallon
Figure 5-2. Effect of White Spruce Bulk Fuel Price on Cost of Delivered Heat
5.3 Determining Demand
Table 5-2 shows the reported approximate amount of fuel oil used by the CRSD Copper Center
School and Kenny Lake School.
Table 5-2. Reported Annual Fuel Oil Consumption, CRSD Facilities
Reported Annual Fuel Consumption Facility Gallons Cost ($) @ $3.00/gallon
Copper Center School 6,000 18,000
Kenny Lake School 20,000 60,000
TOTAL 26,000 78,000
Wood boilers, especially cordwood boilers, are often sized to displace only a portion of the heating
load since the oil system will remain in place, in standby mode, for “shoulder seasons” and peak
demand. Fuel oil consumption for the Copper Center School and Kenny Lake School was
compared with heating demand based on heating degree days (HDD) to determine the required
boiler capacity (RBC) for heating only on the coldest 24 hour day (Table 5-3). While there are
15
many factors to consider when sizing heating systems it is clear that, in most cases, a wood system
of less-than-maximum size could still replace a substantial quantity of fuel oil.
Typically, installed oil-fired heating capacity at most sites is two to four times the demand for the
coldest day, and this appears to be the case at Copper Center. It appears that the installed capacity
at Kenny Lake is more than five times the maximum RBC.
Manual HELE cordwood boilers, equipped with special tanks for extra thermal storage, can supply
heat at higher than their rated capacity for short periods. While rated at 950,000 Btu/hr, the Garn
WHS 3200 can store more than 2 million Btu, which would be enough to heat the Copper Center
School during the coldest 24-hour period for nearly 10 hours (2,064,000 ÷ 207,500).
Table 5-3. Estimate of Heat Required in Coldest 24 Hr Period
Facility Fuel Oil Used
gal/yeara Heating
Degree Daysd Btu/DDc Design
Tempd F
RBCe
Btu/hr
Installed
Btu/hra
Copper Center
School 6,000 14,004 47,301 -40 207,500 750,000
Kenny Lake School 20,000 14,004 157,669 -40 690,400 3,746,000
Table 3-7 Notes:
a From SOI and site visit; net Btu/hr
b NOAA, July 1, 2005 through June 30, 2006:
ftp://ftp.cpc.ncep.noaa.gov/htdocs/products/analysis_monitoring/cdus/degree_days/archives/Heating%20degree%20Days/Monthly%20City/2006/jun%202006.txt
c Btu/DD= Btu/year x oil furnace conversion efficiency (0.85) /Degree Days
d Alaska Housing Manual, 4th Edition Appendix D: Climate Data for Alaska Cities, Research and Rural Development
Division, Alaska Housing Finance Corporation, 4300 Boniface Parkway, Anchorage, AK 99504, January 2000.
e RBC = Required Boiler Capacity for the coldest Day, Btu/hr= [Btu/DD x (65 F-Design Temp)+DD]/24 hrs
According to these calculations (Table 5-3):
• It appears that the Copper Center School could supply 100% of its heating needs
(207,500 Btu/hr during the coldest 24-hour period) with a medium Garn boiler rated at
425,000 Btu/hr. The Garn WHS 2000 can store more than 1¼ million Btu, which,
theoretically, would be enough to heat the facility for more than 6 hours (1,272,000 ÷
207,500). NOTE: This need to be confirmed by a qualified engineer.
• It appears that the Kenny Lake School could supply 100% of its heating needs (690,400
Btu/hr during the coldest 24-hour period) with an extra-large Garn boiler rated at 950,000
Btu/hr. The Garn WHS 4400 can store nearly 3 million Btu, which, theoretically, would be
enough to heat the facility for more than 4¼ hours (2,932,000 ÷ 690,400). Note: installing
multiple large boilers might be a better option than a single extra-large boiler. Consultation
with a qualified engineer is recommended.
5.4 Summary of Findings Table 5-4 summarizes the findings thus far: annual fuel oil usage, range of annual fuel oil costs, estimated annual wood fuel requirement, range of estimated annual wood fuel costs, and potential gross annual savings for the Copper Center School and the Kenny Lake School. [Note: potential gross annual fuel cost savings do not consider capital costs and non-fuel operation, maintenance and repair (OM&R) costs.] Table 5-4. Estimate of Total Wood Consumption, Comparative Costs and Potential Savings Facility Fuel Oil Used gal/yeara Annual Fuel Oil Cost (@ $ ___ /gal) Approximate Wood Requirementb Annual Wood Cost (@ $ ___ /unit) Potential Gross Annual Fuel Cost Savings ($) POTENTIAL CORDWOOD SYSTEMS 3.00 3.50 4.00 White spruce, MC30, CE 75% 100/cord 125/cord 150/cord Low Medium High Copper Center School 6,000 18,000 21,000 24,000 60 6,000 7,500 9,000 9,000 13,500 12,000 Kenny Lake School 20,000 60,000 70,000 80,000 200 20,000 25,000 30,000 30,000 45,000 60,000 Total 26,000 78,000 91,000 104,000 260 26,000 32,500 39,000 39,000 58,500 72,000 POTENTIAL BULK FUEL SYSTEMS White spruce, MC40, CE 70% 30/ton 40/ton 50/ton Kenny Lake School 20,000 60,000 70,000 80,000 428 12,840 17,120 21,400 38,600 52,880 67.160 NOTES: a From Table 5-3; used the numerical average where a range was indicated b From Table D-3, Fuel Oil Equivalents
SECTION 6. ECONOMIC FEASIBILITY OF CORDWOOD SYSTEMS
6.1 Initial Investment Cost Estimates
DISCLAIMER: Short of having an actual Design & Engineering Report prepared by a team of
civil and mechanical engineers, actual costs for any particular system at any particular site cannot
be positively determined. Such a report is beyond the scope of this preliminary assessment.
However, two hypothetical system scenarios are offered as a means of comparison. Actual costs,
assumptions and “guess-timates” are identified as such, where appropriate. Recalculations of
financial metrics, given different/updated cost estimates, are easily accomplished.
Wood heating systems include the cost of the fuel storage building (if necessary), boiler building
(if necessary), boiler equipment (and shipping), plumbing and electrical connections (including
heat exchangers and electrical service to integrate with existing distribution systems), installation,
and an allowance for contingencies.
Before a true economic analysis can be performed, all of the costs (investment and OM&R) must
be identified, and this is where the services of qualified experts are necessary.
Table 6-1 (next page) presents hypothetical scenarios of initial investment costs for cordwood
systems in small and large heating demand situations. Two options are presented for each.
Building(s) and plumbing/connections are the most significant costs besides the boiler(s). Building
costs deserve more site-specific investigation and often need to be minimized to the extent
possible. Piping from the wood-fired boiler is another area of potential cost saving. Long
plumbing runs and additional heat exchangers substantially increase project costs. The cost of hard
copper pipe normally used in Alaska now precludes its use in nearly all applications. If plastic or
PEX piping is used significant cost savings may be possible.
Allowance for indirect non-capital costs such as engineering and contingency are most important
for large systems that involve extensive permitting and budget approval by public agencies. This
can increase the cost of a project by 25% to 50%. For the examples in Table 6-1, a 25%
contingency allowance was used.
NOTE: With the exception of the list prices for Garn boilers, all of the figures in Table 6-1
are gross estimates.
18
Table 6-1. Initial Investment Cost Scenarios for Hypothetical Cordwood Systems
Copper Center School
(small facility)
Kenny Lake School
(large facility)
Fuel oil consumption
(gallons per year) 6,000 20,000
Required boiler capacity (RBC),
Btu/hr 207,500 690,400
Cordwood boiler Model
Rating - Btu/hr
Garn WHS 2000
425,000
Garn WHS 3200
950,000
(1) Garn WHS 4400
950,000
(2) Garn WHS 4400
1,900,000
Building and Equipment (B&E) Costs (for discussion purposes only)
Fuel storage buildinga
(fabric bldg, gravel pad, $20 per sf)
$24,000
(60 cords;1,200 sf)
$80,000
(200 cords; 4,000 sf)
Boiler building @ $100 per sf
(minimum footprint, concrete pad)b
$12,800
(16’ x 8’)
$20,000
(20’ x 10’)
$22,000
(22’ x10’)
$44,000
(22’ x 20’)
Boilers
Base pricec
Shippingd
$14,460
$3,500
$27,700
$5,000
$32,700e
$5,500
$65,400
$10,000
Plumbing/connectionsd $20,000 $35,000 $40,000
Installationd $7,500 $10,000 $15,000
Subtotal - B&E Costs $82,260 $ 104,200 $185,200 $254,400
Contingency (25%)d $20,565 $ 26,050 $ 46,300 $ 63,600
Grand Total $102,825 $130,250 $231,500 $318,000
Notes:
a A cord occupies 128 cubic feet. If the wood is stacked 6½ feet high, the area required to store the wood is 20 square feet per cord.
b Does not allow for any fuel storage within the boiler building
c List price, Dectra Corp, May 2006
d “guess-timate”; for illustrative purposes only
e Published list price not available; this represents list price for WHS 3200 + $5,000
6.2 Operating Parameters of HELE Cordwood Boilers
A detailed discussion of the operating parameters of HELE cordwood boilers can be found in
Appendix F.
6.3 Hypothetical OM&R Cost Estimates
The primary operating cost of a cordwood boiler, other than the cost of fuel, is labor. Labor is
required to move fuel from its storage area to the boiler building, fire the boiler, clean the boiler
and dispose of ash. For purposes of this analysis, it is assumed that the boiler will operate every
day for 210 days (30 weeks) per year between mid-September and mid-April.
Table 6-2 presents labor/cost estimates for various HELE cordwood systems. A detailed analysis of
labor requirement estimates can be found in Appendix F.
19
Table 6-2. Labor/Cost Estimates for HELE Cordwood Systems
Facility Small
(60 cords/yr)
Single Large
(200 cords/yr)
Double Large
(200 cords/year)
System (Garn Model) WHS 2000 WHS 3200 (1) WHS 4400 (2) WHS 4400
Total Daily labor (hrs/yr)a
(hrs/day X 210 days/yr) 198.5 105 351.75 281.4
Total Periodic labor (hrs/yr)b
(hrs/wk X 30 wks/yr) 90 90 180 180
Total Annual labor (hrs/yr)b 20 20 20 40
Total labor (hrs/yr) 308.5 215 551.75 501.4
Total annual labor cost ($/yr)
(total hrs x $20) 6,170 4,300 11,035 10,028
Notes:
a From Table F-2
b From Appendix F
There is also an electrical cost component to the boiler operation. An electric fan creates the
induced draft that contributes to boiler efficiency. One estimate predicted that, at $0.30 per kWh,
the cost of operating the fan would be approximately $100-$200 per year4. The cost of operating
circulation pumps and/or blowers would be about the same as it would be with the oil-fired boiler
or furnace in an existing heating system.
Lastly there is the cost of wear items, such as fire brick, door gaskets, and water treatment
chemicals. This has been suggested at $300-$500 per year4.
Table 6-3. Summary of Total Annual Non-Fuel OM&R Cost Estimates
Cost/Allowance ($)
Small
(60 cords/yr) Item
WHS 2000 WHS 3200
Single Large
(200 cords/yr)
(1) WHS 4400
Double Large
(200 cords/yr)
(2) WHS 4400
Labor 6,170 4,300 11,035 10,028
Electricity 100 100 200 300
Maintenance/Repairs 300 300 400 500
Total non-fuel OM&R ($) 6,570 4,700 11,635 10,828
6.4 Calculation of Financial Metrics
Biomass heating projects are viable when, over the long run, the annual fuel cost savings generated
by converting to biomass are greater than the cost of the new biomass boiler system plus the
additional operation, maintenance and repair (OM&R) costs associated with a biomass boiler
(compared to those of a fossil fuel boiler or furnace).
20
Converting from an existing boiler to a wood biomass boiler (or retrofitting/integrating a biomass
boiler with an existing boiler system) requires a greater initial investment and higher annual
OM&R costs than for an equivalent oil or gas system alone. However, in a viable project, the
savings in fuel costs (wood vs. fossil fuel) will pay for the initial investment and cover the
additional OM&R costs in a relatively short period of time. After the initial investment is paid off,
the project continues to save money (avoided fuel cost) for the life of the boiler. Since inflation
rates for fossil fuels are typically higher than inflation rates for wood fuel, increasing inflation rates
result in greater fuel savings and thus greater project viability.17
The potential financial viability of a given project depends not only on the relative costs and cost
savings, but also on the financial objectives and expectations of the facility owner. For this reason,
the impact of selected factors on potential project viability is presented using the following metrics:
Simple and Modified Simple Payback Period
Present Value (PV)
Net Present Value (NPV)
Internal Rate of Return (IRR)
Life Cycle Cost (LCC)
Total initial investment costs include all of the capital and non-capital costs required to design,
purchase, construct and install a biomass boiler system in an existing facility with an existing
furnace or boiler system.
A more detailed discussion of Simple Payback Period, Present Value, Net Present Value and
Internal Rate of Return can be found in Appendix E.
6.5 Simple and “Modified Simple” Payback Period for Small and Large HELE
Cordwood Boilers
Table 6-4 presents a Payback Period analysis for hypothetical small and large HELE cordwood
boiler installations.
Table 6-4. Simple and “Modified Simple” Payback Period Analysis for HELE Cordwood Boilers
Facility Small Single Large Double Large
Fuel (6,000 gpy; 60 cds/yr) (20,000 gpy; 200 cords/yr)
Boiler model WHS 2000 WHS 3200 (1) WHS 4400 (2) WHS 4400
Fuel oil cost
($ per year @ $3.00 per gallon) 18,000 60,000
Cordwood cost
($ per year @ $100 per cord) 6,000 20,000
Gross annual fuel cost savings ($) 12,000 40,000
Annual, non-fuel OM&R costsa 6,570 4,700 11,635 10,828
Net Annual Savings ($) 5,430 7,300 28,365 29,172
Total Investment Costs ($)b 102,825 130,250 231,500 318,000
Simple Payback (yrs)c 8.57 10.85 5.79 7.95
Modified Simple Payback (yrs)d 18.94 17.84 8.16 10.9
Notes:
a From Table 6-3
b From Table 6-1
c Total investment costs divided by Gross annual fuel cost savings
d Total Investment Costs divided by Net Annual Savings
21
6.6 Present Value (PV), Net Present Value (NPV) and Internal Rate or Return (IRR) Values
for Small and Large HELE Cordwood Boilers
Table 6-5 presents PV, NPV and IRR values for hypothetical small and large HELE cordwood
boilers.
Table 6-5. PV, NPV and IRR Values for HELE Cordwood Boilers
Facility Small Single Large Double Large
Fuel (6,000 gpy; 60 cds/yr) (20,000 gpy; 200 cords/yr)
Boiler model WHS 2000 WHS 3200 (1) WHS 4400 (2) WHS 4400
Discount Ratea 3%
Time, “t”, (years) 20
Initial Investment ($)b 102,825 130,250 231,500 318,000
Annual Cash Flow ($)c 5,430 7,300 28,365 29,172
Present Value
(of expected cash flows, $ at “t” years) 80,785 108,606 422,000 434,006
Net Present Value ($ at “t” years) -22,040 -21,644 190,500 116,006
Internal Rate of Return (% at “t” years) 0.53 1.11 10.63 6.64
See Note # _ below 1 2 3 4
Notes:
a real discount (excluding general price inflation) as set forth by US Department of Energy, as found in NIST publication NISTIR 85-3273-22, Energy
Price Indices and Discount Factors for Life Cycle Cost Analysis – April 2007
b From Table 6-1
c Equals annual cost of fuel oil minus annual cost of wood minus annual non-fuel OM&R costs (i.e. Net Annual Savings)
Note #1. With a real discount rate of 3.00% and after a span of 20 years, the projected cash flows are worth $80,785
today (PV), which is less than the initial investment of $102,825. The resulting NPV of the project is -$22,040,
which means that the project, given the stated assumptions and cost estimates, will not achieve the stated return
[i.e., 3%] at the end of 20 years.
Given the assumptions and cost estimates for this example, this project does not appear to be financially
feasibility. However, the initial investment cost estimates could be too high. Furthermore, annual cash flows
will increase if oil prices continue to increase above the general rate of inflation and/or disproportionately to the
cost of wood fuel.
Note #2. With a real discount rate of 3.00% and after a span of 20 years, the projected cash flows are worth $108,606
today (PV), which is less than the initial investment of $130,250. The resulting NPV of the project is -$21,644,
which means that the project, given the stated assumptions and estimates, will not achieve the stated return [i.e.,
3%] at the end of 20 years.
Given the assumptions and cost estimates for this example, this project does not appear to be financially
feasibility. However, the initial investment cost estimates could be too high. Furthermore, annual cash flows
will increase if oil prices continue to increase above the general rate of inflation and/or disproportionately to the
cost of wood fuel.
NOTE: In this hypothetical example, it appears that the labor savings associated with the larger, more costly
boiler provides improved financial metrics over the less costly, more labor-intensive smaller boiler. As a
practical matter, having to fire the boiler 2 times per day versus 6 times per day could be the deciding factor.
22
Note #3. With a real discount rate of 3.00% and after a span of 20 years, the projected cash flows are worth $422,000
today (PV), which is greater than the initial investment of $231,500. The resulting NPV of the project is
$190,500, and the project achieves an internal rate of return of 10.63% at the end of 20 years. (NPV becomes
positive at year 10.)
Given the assumptions and cost estimates for this example, the project appears feasible. However, the cost
estimates could be low. Areas where significant cost increases could be incurred include the fuel storage
building, the boiler building, the plumbing and connections, and the contingency allowance.
Note #4. With a real discount rate of 3.00% and after span of 20 years, the projected cash flows are worth $434,006
today (PV), which is greater than the initial investment of $318,000. The resulting NPV of the project is -
$116,006, and the project achieves an internal rate of return of 6.64% at the end of 20 years. (NPV becomes
positive at year 14.)
Given the assumptions and cost estimates for this example, the project appears feasible. However, the cost
estimates could be low. Areas where significant cost increases could be incurred include the fuel storage
building, the boiler building, the plumbing and connections, and the contingency allowance.
NOTE: In this hypothetical example, it appears that the labor savings associated with installing 2 boilers has a
negative impact on the overall financial metrics. However, as a practical matter, having to fire the boiler 3
times per day versus 7 times per day could be the deciding factor.
6.7 Life Cycle Cost Analysis
The National Institute of Standards and Technology (NIST) Handbook 135, 1995 edition, defines
Life Cycle Cost (LCC) as “the total discounted dollar cost of owning, operating, maintaining, and
disposing of a building or a building system” over a period of time. Life Cycle Cost Analysis
(LCCA) is an economic evaluation technique that determines the total cost of owning and
operating a facility over a period of time. Alaska Statute 14.11.013 directs the Department of
Education and Early Development (EED) to review capital projects to ensure they are in the best
interest of the state, and AS 14.11.014 stipulates the development of criteria to achieve cost
effective school construction.19
While a full-blown life cycle cost analysis is beyond the scope of this preliminary feasibility
assessment, an attempt is made to address some of the major items and run a rudimentary LCCA
using the Alaska EED LCCA Handbook and spreadsheet.
According to the EED LCCA Handbook, the life cycle cost equation can be broken down into three
variables: the costs of ownership, the period of time over which the costs are incurred
(recommended period is 20 years), and the discount rate that is applied to future costs to equate
them to present costs.
There are two major cost categories: initial expenses and future expenses. Initial expenses are all
costs incurred prior to occupation (or use) of a facility, and future expenses are all costs incurred
upon occupation (or use) of a facility. Future expenses are further categorized as operation costs,
maintenance and repair costs, replacement costs, and residual value. A comprehensive list of
items in each of these categories is included in the EED LCCA Handbook.
The discount rate is defined as, “the rate of interest reflecting the investor’s time value of money”,
or, the interest rate that would make an investor indifferent as to whether he received payment now
or a greater payment at some time in the future. NIST takes the definition a step further by
separating it into two types: real discount rates and nominal discount rates. The real discount rate
excludes the rate of inflation and the nominal discount rate includes the rate of inflation.19 The
23
EED LCCA Handbook and spreadsheet focuses on the use of real discount rates in the LCC
analysis.
To establish a standard discount rate for use in the LCCA, EED adopted the US Department of
Energy’s (DOE) real discount rate. This rate is updated and published annually in the Energy Price
Indices and Discount Factors for Life Cycle Cost Analysis – Annual Supplement to NIST
Handbook 135 (www1.eere.energy.gov/femp/pdfs/ashb07.pdf). The DOE discount and inflation rates for
2007 are as follows:
Real rate (excluding general price inflation) 3.0%
Nominal rate (including general price inflation) 5.0%
Implied long term average rate of inflation 1.9%
Other LCCA terms
Constant dollars: dollars of uniform purchasing power tied to a reference year and exclusive of
general price inflation or deflation
Current dollars: dollars of non-uniform purchasing power, including general price inflation or
deflation, in which actual prices are stated
Present value: the time equivalent value of past, present or future cash flows as of the beginning of
the base year.
NOTE: When using the real discount rate in present value calculations, costs must be expressed in
constant dollars. When using the nominal discount rate in present value calculations, costs must be
expressed in current dollars. In practice, the use of constant dollars simplifies LCCA, and any
change in the value of money over time will be accounted for by the real discount rate.
LCCA Assumptions
As stated earlier, it is beyond the scope of this pre-feasibility assessment to go into a detailed life
cycle cost analysis. However, a limited LCCA is presented here (for each of the schools) for
purposes of discussion and comparison.
Time is assumed to be 20 years, as recommended by EED
The real discount rate is 3%
Initial expenses as per Table 6.1
Future expenses as per Table 6.3
Replacement costs – not addressed
Residual value – not addressed
6.7.1 Copper Center School
Alternative 1 represents the existing oil-fired furnaces. The initial investment was assumed
(arbitrarily) to be $50,000. The operation costs included 6,000 gallons of fuel oil at $3.00 per
gallon and 40 hours of labor per year at $20 per hour. The annual maintenance and repairs costs
were assumed to be $1,000 and no allowances were made for replacement costs or residual value.
Alternative 2 represents the existing oil-fired furnaces, which would remain in place, plus the
installation of a Garn WHS 2000 wood fired boiler. The initial investment was assumed to be
24
$152,825, which includes the value of the existing oil-fired furnaces (valued at $50,000, as above)
plus the initial investment cost of the Garn boiler ($102,825, as per Table 6-1). The operation costs
include 60 cords of fuelwood at $100 per cord and 308.5 hours of labor per year at $20 per hour.
The annual maintenance and repairs costs were assumed to be $400 and no allowances were made
for replacement costs or residual value.
Alternative 3 represents the existing oil-fired furnaces, which would remain in place, plus the
installation of a Garn WHS 3200 wood fired boiler. The initial investment was assumed to be
$180,250, which includes the value of the existing oil-fired furnaces (valued at $50,000 as above)
plus the initial investment cost of the Garn boiler ($130,250, as per Table 6-1). The operation costs
include 60 cords of fuelwood at $100 per cord and 215 hours of labor per year at $20 per hour.
The annual maintenance and repairs costs were assumed to be $400 and no allowances were made
for replacement costs or residual value.
The EED LCCA results for the Copper Center School are presented in Table 6-6.
Table 6-6. Life Cycle Costs of Copper Center School Project Alternatives
Alternative #1 Alternative #2 Alternative #3
Initial Investment Costs $50,000 $152,825 $180,250
Operation Costs $282,672 $207,838 $180,017
Maintenance & Repair Costs $14,877 $5,951 $5,951
Replacement Costs $0 $0 $0
Residual Values $0 $0 $0
Total Life Cycle Cost $347,549 $366,614 $366,218
6.7.2 Kenny Lake School
Alternative 1 represents the existing oil-fired boiler system. The initial investment was assumed
(arbitrarily) to be $50,000. The operation costs included 20,000 gallons of fuel oil at $3.00 per
gallon and 40 hours of labor per year at $20 per hour. The annual maintenance and repairs costs
were assumed to be $1,000 and no allowances were made for replacement costs or residual value.
Alternative 2 represents the existing oil-fired furnaces, which would remain in place, plus the
installation of a single Garn WHS 4400 wood fired boiler. The initial investment was assumed to
be $281,500, which includes the value of the existing oil-fired furnaces (valued at $50,000 as
above) plus the initial investment cost of the Garn boiler ($231,500, as per Table 6-1). The
operation costs include 200 cords of fuelwood at $100 per cord and 551.75 hours of labor per year
at $20 per hour. The annual maintenance and repairs costs were assumed to be $600 and no
allowances were made for replacement costs or residual value.
Alternative 3 represents the existing oil-fired furnaces, which would remain in place, plus the
installation of two Garn WHS 4400 wood fired boilers. The initial investment was assumed to be
25
$368,000, which includes the value of the existing oil-fired furnaces (valued at $50,000 as above)
plus the initial investment cost of the Garn boilers ($318,000, as per Table 6-1). The operation
costs include 200 cords of fuelwood at $100 per cord and 501.4 hours of labor per year at $20 per
hour. The annual maintenance and repairs costs were assumed to be $800 and no allowances were
made for replacement costs or residual value. 501.4
The EED LCCA results for the Kenny Lake School are presented in Table 6-7.
Table 6-7. Life Cycle Costs of Kenny Lake School Project Alternatives
Alternative #1 Alternative #2 Alternative #3
Initial Investment Cost $50,000 $281,500 $368,000
Operations Cost $904,550 $461,722 $446,741
Maintenance & Repair Cost $14,877 $8,926 $11,902
Replacement Cost $0 $0 $0
Residual Value $0 $0 $0
Total Life Cycle Cost $969,428 $752,149 $826,643
SECTION 7. ECONOMIC FEASIBILITY OF BULK FUEL SYSTEMS
A typical bulk fuel boiler system includes bulk fuel storage, a boiler building, wood-fuel handling
systems, combustion chamber, boiler, ash removal, cyclone, exhaust stack and electronic controls.
The variables in this list of system components include the use of silos of various sizes for wood
fuel storage, chip storage areas of various sizes, boiler buildings of various sizes, automated versus
manual ash removal and cyclones for particulate removal.17
7.1 Capital Cost Components
As indicated, bulk fuel systems are larger, more complex and more costly to install and integrate
with existing boiler and distribution systems. Before a true economic analysis can be performed,
all of the costs (capital, non-capital and OM&R) must be identified, and this is where the services
of architects and civil and mechanical engineers are necessary.
Table 7-1 outlines the various general components for a hypothetical, small bulk fuel system;
however it is beyond the scope of this report to offer estimates of costs for those components. As
an alternative, a range of likely total costs is presented and analyzed for comparison purposes.
26
Table 7-1. Initial Investment Cost Components for Bulk Fuel Systems
Facility Kenny Lake School
(20,000 gallons/year; 428 tons/year)
Capital Costs: Building and Equipment (B&E)
Fuel storage building
Material handling system
Boiler building
Boiler: base price
shipping
Plumbing/connections
Electrical systems
Installation
Total Capital (B&E) Costsa
Non-capital Costs
Engineering , Contingency,
Permitting, etc.
Initial Investment Total ($) $500,000 to $2,000,000
The investment cost of bulk fuel systems can range from $500,000 to $2 million, with about
$350,000 to $900,000 in equipment costs. Fuel handling and boiler equipment for an 8 MMBtu/hr
(300 BHP) system was recently quoted to a school in the northeast USA for $900,000. The cost of
a boiler and fuel handling equipment for a 3 to 4 MMBtu/hr system is about $350,000 to $500,000.
The 2.4 MMBtu/hr system in Hoonah was installed at a sawmill for $250,000, but an existing
building was used and there were significant economies in fuel preparation and handling that
would be unacceptable in a non-industrial, institutional setting. Fuel and boiler equipment for a 1
MMBtu per hour system is estimated at $250,000 to $300,000 (buildings are extra). Several
schools in New England have been able to use existing buildings or boiler rooms to house new
equipment and realize substantial savings, but recent school projects in Montana were all installed
in new buildings.4
The Craig Schools and Aquatic Center project in Craig, AK was originally estimated at less than $1
million to replace propane and fuel oil equivalent to 36,000 gallons of fuel oil, but the results of a
January 2007 bid opening brought the cost to over $1.8 million. The fuel storage and boiler
building, and system integration costs for the pool and two schools increased the project costs.
Table 7-2 shows the total costs for the Darby School (Darby, MT) project at $1,001,000 including
$268,000 for repairs and upgrades to the pre-existing system. Integration with any pre-existing system
will likely require repairs and rework that must be included in the wood system cost. Adding the indirect
costs of engineering, permits, etc. to the equipment cost put the total cost at Darby between $716,000 and
$766,000 for the 3 million Btu/hr system to replace 47,000 gallons of fuel oil per year. (NOTE: although
the Darby School replaces more than twice the amount of fuel used at the Kenny Lake School, it would
not be safe to estimate the cost of a 50% smaller bulk fuel system at half the cost.) Since the boiler was
27
installed at Darby, building and equipment costs have increased from 10% to 25%. A new budget price
for the Darby system might be closer to $800,000 excluding the cost of repairs to the existing system.4
Table 7-2. Darby, MT Public School Wood Chip Boiler Costs a
Boiler Capacity 3 MMBtu/hr
Fuel Oil Displaced 47,000 gallons
Heating Degree Days 7,186
System Costs:
Building, Fuel Handling $ 230,500
Boiler and Stack $ 285,500
Boiler system subtotal $ 516,000
Piping, integration $ 95,000
Other repairs, improvements $ 268,000
Total, Direct Costs $ 879,000
Engineering, permits, indirect $ 122,000
Total Cost $1,001,000
a Biomass Energy Resource Center, 2005 4
The following is an excerpt from the Montana Biomass Boiler Market Assessment17:
“To date, CTA [CTA Architects and Engineers, Billings, MT] has evaluated more than 200
buildings throughout the northwestern United States and designed 13 biomass boiler projects, six of
which are now operational. Selected characteristics of these projects, including total project cost,
are presented in Table 1 [7-3]. As can be seen from Table 1 [7-3], total costs for these projects do
not correlate directly with boiler size. The least expensive biomass projects completed to date cost
$455,000 (not including additional equipment and site improvements made by the school district)
for a wood chip system in Thompson Falls, Montana. The least expensive wood pellet system is
projected to cost $269,000 in Burns, Oregon. The general breakdown of costs for these two projects
is presented in Tables 2 [7-4] and 3.”
NOTE: Information related to wood pellet systems was not included in this report as wood pellets
are not available as a fuel in south-central Alaska.
28
Table 7-3. Characteristics of Biomass Boiler Projects17
Facility
Name Location Boiler Size
(MMBtu/hr output) Project Type
Wood
Fuel
Type
Total
Project
Cost
Thompson
Falls School
District
Thompson
Falls, MT 1.6 MMBtu Stand-alone boiler building
tied to existing steam system Chips $ 455,000
Glacier High
School
Kalispell,
MT 7 MMBtu
New facility with integrated
wood chip and natural gas
hot water system
Chips $ 480,000
Victor School
District Victor, MT 2.6 MMBtu Stand-alone boiler building
tied to existing steam system Chips $ 615,000
Philipsburg
School District
Philipsburg,
MT 3.87 MMBtu
Stand-alone boiler building
tied to existing hot water
system
Chips $ 684,000
Darby School
District Darby, MT 3 MMBtu
Stand-alone boiler building
tied to existing steam & hot
water system
Chips $ 970,000
City of Craig Craig, AK 4 MMBtu
Stand-alone boiler building
tied to existing hot water
systems
Chips $1,400,000
UM Western Dillon, MT 14 MMBtu Addition to existing steam
system Chips $1,400,000
Table 7-4. Cost Breakdown for the Least Expensive Wood Chip Boiler System Installed in a
New Free-Standing Building 17
System Component Cost % of Total
Wood Boiler System Equipment $136,000 30%
Building $170,000 38%
Mechanical/Electrical $100,000 22%
Mechanical Integration $15,000 3%
Fees, Permits, Printing, Etc. $34,000 7%
Total* $455,000* 100%
* not including additional equipment and site improvements made by the school district
7.2 Generic OM&R Cost Allowances
The primary operating cost is fuel. The estimated bulk fuel cost for the Kenny Lake School is
$12,840 (428 tons @ $30/ton). NOTE: $30 per ton is probably unrealistically low. Higher wood
fuel costs would only serve to have a more negative impact on project feasibility.
Other O&M costs would include labor, electricity and maintenance/repairs. For purposes of this
analysis, it is assumed that the boiler will operate every day for 210 days (30 weeks) per year
between mid-September and mid-April.
29
Daily labor would consist of monitoring the system and performing daily inspections as prescribed
by the system manufacturer. It is assumed that the average daily labor requirement is ½ hour. An
additional 1 hour per week is allocated to perform routine maintenance tasks. Therefore, the total
annual labor requirement is (210 x 0.5) + 30 = 135 hours per year. At $20 per hour, the annual
labor cost would be $2,700.
There is also an electrical cost component to the boiler operation. Typically, electrically-powered
conveyors of various sorts are used to move fuel from its place of storage to a metering bin and into
the boiler. There are also numerous other electrical systems that operate various pumps, fans, etc.
The Darby High School system in Darby, MT, which burned 755 tons of bulk fuel in 2005, used
electricity in the amount of $2,035,18 however the actual kWh or cost per kWh were not reported.
Another report17 proffered an average electricity cost for Montana of $0.086 per kWh. If that rate
is true for Darby, then the electrical consumption would have been about 23,663 kWh. The Kenny
Lake School is projected to use 428 tons of bulk fuel (57% of the amount used at Darby). If it is
valid to apportion the electrical usage based on bulk fuel consumption, then Kenny Lake would use
about 13,414 kWh per year. At $0.30 per kWh, the annual electrical consumption would be
$4,024.
Lastly, there is the cost of maintenance and repair. Bulk fuel systems with their conveyors, fans,
bearings, motors, etc. have more wear parts. An arbitrary allowance of $2,000 is made to cover
these costs.
Total annual operating, maintenance and repair cost estimates for a bulk fuel boiler at the Kenny
Lake School are summarized in Table 8-2
Table 7-5. Total OM&R Cost Allowances for a Bulk Fuel System
Item Cost/Allowance
Non-Fuel OM&R
Labor ($) 2,700
Electricity ($) 4,024
Maintenance ($) 2,000
Total, non-fuel OM&R 8,724
Wood fuel ($) 12,840
Total OM&R ($) 21,564
7.3 Calculation of Financial Metrics
A discussion of Simple Payback Period can be found in Appendix E.
A discussion of Present Value can be found in Appendix E.
A discussion of Net Present Value can be found in Appendix E.
A discussion of Internal Rate of Return can be found in Appendix E.
7.4 Simple and “Modified Simple” Payback Period for Generic Bulk Fuel Boilers
Table 7-6 presents Payback Period analysis for a range of initial investment cost estimates for
generic bulk fuel boiler systems.
30
Table 7-6. Simple and “Modified Simple” Payback Period Analysis
Facility Kenny Lake School
(20,000 gpy; 428 tons/yr)
Fuel oil
($ per year @ $3.00 per gallon 60,000
Bulk wood fuel
($ per year @ $30 per ton) 12,840
Gross Annual Savings ($)
(fuel cost savings) 47,160
Net Annual Savings ($)
(Gross savings minus non-fuel OM&R
Costs)
38,436
Total Investment Costs ($) 750,000 900,000 1,050,000 1,200,000 1,350,000 1,500,000
Simple Payback (yrs)a 15.9 19.08 22.26 25.45 28.63 31.81
Modified simple payback (yrs)b 19.51 23.42 27.32 31.22 35.12 39.03
a Simple payback equals total investment cost divided by gross annual savings
b Modified simple payback equals total investment cost divided by net annual savings
While simple payback has its limitations in terms of project evaluations, one of the conclusions of
the Montana Biomass Boiler Market Assessment was that viable projects had simple payback
periods of 10 years or less.17
7.5 Present Value (PV), Net Present Value (NPV) and Internal Rate or Return (IRR)
Values for a Hypothetical Bulk Fuel Boiler Installed at the Kenny Lake School
Table 7-7 presents PV, NPV and IRR values for hypothetical bulk fuel boilers.
Table 7-7. PV, NPV and IRR Values for Bulk Fuel Systems
Discount Rate 3
Time, “t”, (years) 20
Initial Investment ($)a 750,000 900,000 1,050,000 1,200,000 1,350,000 1,500,000
Annual Cash Flow ($)b 38,436
Present Value (of expected cash
flows), ($ at “t” years) 571,831
Net Present Value ($ at “t” years) -178,169 -328,169 -478,169 -628,169 -778,169 -928,169
Internal Rate of Return (%) 0.24 -1.46 -2.80 -3.91 -4.85 -5.67
Notes:
a from Table 7-6
b Equals annual cost of fuel oil minus annual cost of wood minus annual non-fuel OM&R costs
31
SECTION 8. CONCLUSIONS
This report discusses conditions found “on the ground” at the Copper River School District school
facilities at Copper Center and Kenny Lake, AK in south-central Alaska, and attempts to
demonstrate, by use of realistic, though hypothetical examples, the feasibility of installing high
efficiency low emission cordwood and/or bulk fuel wood boilers for heating these facilities.
Wood is a viable heating fuel in a wide range of institutional applications, however, below a certain
minimum and above a certain maximum, it may be impractical to heat with wood, or it may require
a different form of wood fuel and heating system. The difference in the cost of heat derived from
wood versus the cost of heat derived fuel oil is significant, as illustrated in Table 5-1. It is this
difference in the cost of heat, resulting in monetary savings, that must “pay” for the substantially
higher investment and OM&R costs associated with wood-fuel systems.
8.1 “Small” Applications – Copper Center School
The Copper River School District owns, operates and manages the K-6 school in Copper Center,
AK, which consists of one large primary building and two smaller satellite buildings. These
facilities are in close proximity to one another, and each has its own heating system.
The individual fuel oil consumption for each of these buildings was not reported, but taken all
together, these buildings consume a reported 6,000 gallons of fuel oil per year. Physically, it
appears very possible that these buildings could be served by one cordwood boiler. Although
connective plumbing is not cheap, the distances between buildings and the prospective sites for a
boiler do not appear excessive. These buildings do not already have hydronic heating systems, so
some additional expenses will have to be incurred to retrofit the existing hot air systems.
In the hypothetical examples presented in Section 6 for a small facility with a cordwood boiler, the
gross annual (fuel cost) savings would amount to $12,000. Two scenarios were then presented:
1. With a small boiler (Garn WHS 2000) being fired approximately 6 times per day, the
simple payback period would be 8.57 years (given a cordwood boiler installation costing
an estimated $102,825). However, when annual OM&R costs are considered, modified
simple payback period is nearly 19 years and the present value, net present value and
internal rate of return after 20 years, assuming a real discount rate of 3%, are $80,785,
-$22,040 and 0.53% respectively.
2. With a large boiler (Garn WHS 3200) being fired twice per day, the simple payback
period would be 10.85 years (given a cordwood boiler installation costing an estimated
$130,250). However, when annual OM&R costs are considered, modified simple payback
becomes 17.84 years and the present value, net present value and internal rate of return
after 20 years, assuming a discount rate of 3%, are $180,606, -$21,644 and 1.11%
respectively.
While neither of these scenarios presents a positive outcome given the stated assumptions and cost
estimates, the net present value becomes positive at year 20 if the initial project cost is reduced by
approximately $22,000 (in either case). Furthermore, the financial metrics (simple payback period
notwithstanding) appear to favor scenario 2, with the larger boiler and the labor savings associated
with fewer firings per day. Closer scrutiny of this project by qualified professionals would be
justified.
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8.2 “Large Applications – Kenny Lake School
The Kenny Lake School provides K through 12 instruction for 135 students. The facility consists
of one large main building and several utility “outbuildings”. Heat is provided by two oil-fired
Burnham boilers rated at 1.87 million Btu/hr (net, each), located in a single mechanical room at the
rear of the main building. Heat is delivered via a hydronic heating system, with some supplemental
hot air. The Kenny Lake School could be considered “large” in terms of its fuel oil consumption
(20,000 gpy), but it is not large enough to justify the installation of a bulk fuel wood heating
system.
The topography around the school is gentle, presenting no apparent physical impediments to an
external boiler installation. There are at least two potential sites for a wood-fueled boiler within
reasonable distances to the school buildings.
Cordwood Systems:
To replace 20,000 gallons of fuel oil per year would require approximately 200 cords of reasonably
dry (MC30) white spruce cordwood and/or large sawmill residues (i.e., slabwood).
In the example presented in Section 6 for a “large” facility, with a single large cordwood boiler
(Garn WHS 4400), requiring 6.7 firings per day, the gross annual (fuel cost) savings would amount
to $40,000, and yield a simple payback of 5.79 years (given a cordwood boiler installation costing
$231,500). When annual OM&R costs are considered, the modified simple payback period
becomes 8.16 years and the present value, net present value and internal rate of return after 20
years, assuming a discount rate of 3%, are $422,000, $190,500 and 10.63% respectively. These
results indicate that, under the assumed conditions, the project is economically viable.
In the example presented in Section 6 for a “large” facility, with two large cordwood boilers (2
Garn WHS 4400), requiring 3.35 firings per day, the gross annual (fuel cost) savings would amount
to $40,000, and yield a simple payback of 7.95 years (given a cordwood boiler installation costing
$318,000). When annual OM&R costs are considered, the modified simple payback period is 10.9
years, and the present value, net present value and internal rate of return after 20 years, assuming a
discount rate of 3%, are $434,006, $116,006 and 6.64% respectively. These results indicate that,
under the assumed conditions, the project is also economically viable.
Bulk Fuel System:
To replace 20,000 gallons of fuel oil per year would require approximately 428 tons
(approximately twenty 40-foot tractor trailer loads) of bulk fuel (chips, sawdust, bark, shavings,
etc.), assuming such fuel runs 40% moisture content (MC40).
Although it is beyond the scope of this assessment to delve into the costs associated with bulk fuel
systems, it is not unrealistic to say that, at 20,000 gallons of fuel oil per year, it is unlikely that a
bulk fuel system would be cost-effective for the Kenny Lake School. To be cost-effective, a bulk
fuel system would have to be designed, engineered and installed for less than $575,000, which is
highly improbable. While such systems exist in Alaska, they do so in industrial settings that can
tolerate the noise, fugitive dust and vehicle traffic that would be unacceptable in an institutional
setting such as a school or hospital. Furthermore, supplies of bulk fuels within reasonable
proximity to Kenny Lake are limited at best or non-existent altogether, and the bulk fuel cost
estimate used in this report ($30 per ton) is probably unrealistically low.