ND
Biodiesel Task Force
Feasibility of Biodiesel Production in
Area of Fargo, North Dakota
Pat Downs, ND
Bio-Diesel Task Force
Biodiesel: The Specifications
Advantages Compared to Petroleum Based Diesel
Fuel
4 Biodiesel blends require essentially no engine
modifications up to B20 while providing similar BTU content, fuel economy and
performance
4 Specific advantages include superior lubricity, higher
flash point, no sulfur or aromatics, higher cetane number and higher oxygen
Biodiesel Processing
Production Methods
4 The
production processes for biodiesel are well known. The three basic methods
are:
• Base
catalyzed transesterification of the oil
• Direct
acid catalyzed transesterification of the oil
• Conversion
of the oil to its fatty acids and then to biodiesel
4 Most
biodiesel produced today used the base catalyzed reaction because:
• It
is low temperature and pressure
• It
yields high conversion (98%) with minimal side reactions and reaction time
• It
is a direct conversion to biodiesel with no intermediate compounds
• No
exotic materials of construction are need
Biodiesel Processing
Base Catalyzed Transesterification
4 Generally
100 pounds of fat or oil are reacted with 10 pounds of methanol (a short chain
alcohol) in the presence of about 1 pound of a catalyst (usually sodium or
potassium hydroxide)
Biodiesel Processing
Methanol vs. Ethanol
4 A rule of
organic chemistry: the shorter the carbon chain length, the more reactive the
alcohol
4 Methanol
is a single carbon alcohol while ethanol has two carbon atoms
4 For this
reason, it takes about 1.8 gallons of ethanol to produce 10 gallons of
biodiesel vs. 1.0 gallon of methanol
4 Assuming
ethanol at $1.25 / gallon and methanol at $0.75 / gallon, use of ethanol will
increase production costs by a minimum of $0.15 per gallon of biodiesel!
4 In
addition, ethanol holds 5% water that cannot be removed via the less expensive
method of distillation
Biodiesel Processing
Preprocessing (Refining)
4 Biodiesel
can be produced from any type of vegetable oil or animal fat
4 However,
all of these feedstocks require some level of pre-processing to remove
materials that reduce the yield of biodiesel and increase the processing costs
to achieve the ASTM specifications
4 In
integrated production facilities, this is generally known as “refining”
4 Crude or
unrefined oils contain free fatty acids (FFAs), gums and other impurities that
must be removed
4 Pre-processing
including esterification to remove FFAs involves:
• Filtering:
typically used as a first step with yellow greases
• Degumming:
mixing 3-5% water with the feedstock to precipitate the gums
• Refining:
use of sodium hydroxide to form a soap that is separated
Biodiesel Processing
Free Fatty Acid and Impurities in Feedstocks
4 The quality of available fats and oils will vary
depending upon the % of free fatty acids (FFA) and the % moisture, insolubles
& unsaponifiables (MIU moisture along with other impurities) among other
factors. One measure of these impurities is indicated below:
Biodiesel Processing
Pre-Processing Costs by Feedstock
4 There are three components to supplemental costs
associated with required pre-processing of biodiesel feedstocks:
•
Added operating costs;
•
Implied amortized capital
requirements; and
•
Lowered conversion rates to
biodiesel from remaining “purified” feedstocks
4 The biodiesel industry is too young to have yet
established broadly accepted supplemental cost numbers for the necessary
pre-processing
4 SJH estimates of supplemental costs are directional in
nature and shown on the next slide based upon the following assumptions:
•
Operating costs: based upon the mid-point of a range estimated by
Frazier Barnes.
•
Capital costs: roughly equivalent to supplemental operating costs on
a per pound basis
•
Lowered conversion rates: based upon levels of FFA’s and MIU’s as indicated on
the previous slide for different feedstocks (note that the level of these
impurities can vary widely)
Biodiesel Processing
Pre-Processing Costs by Feedstock
4 Actual
effective feedstock costs can vary greatly with time, feedstock costs and
process technologies
Biodiesel Processing
Opportunities for Increased Processing
Efficiencies
4 Process design / construction firms such as PSI Lurgi,
Bratney and Crowne are unable or unwilling to identify specific quantitative
cost advantages from their proprietary technologies
4 USDA ERRC cost model calculates non-feedstock
processing costs at $0.25 / gal for the base catalyzed transesterification
process, assuming a $0.12 / gal co-product credit and cost of methanol at $0.75
/ gal
4 The variable processing cost for biodiesel, excluding
purchase costs for feedstock and methanol, is approximately $0.30 per gallon
4 An extremely efficient production process might achieve
up to a 15% reduction in process cost, reflecting a savings of up to 4.5 cents
per gal.
4 Process cost savings of up to $0.045 per gallon ARE
significant in terms of competitive advantage vs. other production facilities,
but the assumption is that competitive
facilities will also perform their due diligence!!!! (Cost to compete, not an advantage!!!!)
4 The same potential for savings are NOT significant in
terms of establishing overall operational profitability when feedstock costs
can vary by as much as $0.90 per gallon of biodiesel!!!
Biodiesel Characteristics
Measures of Cold Flow Properties
4 Cloud
Point (CP): the temperature at which a cloud
of wax crystals that might plug the fuel filter first appears (ASTM D2500)
4 Pour
Point (PP): the lowest temperature at which
movement can be observed when the sample container is tilted (ASTM D97)
4 Low
Temperature Flow Test (LTFT): is designed to
determine if a fuel can be expected to pass through an engine fuel filtration
system (ASTM D4539)
4 Cold
Filter Plugging Point (CFPP): similar in
design and intent to LTFT (ASTM D6371-99)
Feedstock Availability
ADM – Enderlin and Mankato
4 Enderlin
crushes a mix of canola, sunflower, and soybean
4 Enderlin
crush mix changes depending upon availability and economics of oilseeds
4 Close to
two-thirds of Enderlin crude soy oil is shipped to the west coast, with the
remainder refined at Mankato
4 Sale of all product is determined daily by the central trading desk in Decatur
4 ADM
expressed willingness to supply a local or regional, independent biodiesel
plant with feedstock
4 A recent
feasibility study for biodiesel production in Minnesota reflects the mix of
ADM’s short and long-term interest in biodiesel production
Feedstock Availability
Canola Oil
4 Canola
has traditional maintained a price premium to soy oil of approximately 15%,
although that has been inverted several times over the past ten years
4 From a
horticultural perspective, canola appears to make sense: 42% oil content and
potential for almost twice the oil per acre
4 However,
macro trends in concerns for diet, along with pending labeling of trans-fats
will likely further drive the historic price differential between canola and
soy oils
4 Although
a case could be made for an integrated canola crush facility in the Mandan region (or further west), it is difficult to overcome the obstacle of higher market
costs for the oil
Feedstock Availability
Summary
4 Short to
mid-term, it appears that an independent biodiesel producer will be able to
source sufficient soy oil to support a 10 – 15M gpy facility, the minimum size
required to attain the efficiency of scale from use of a continues production
process
4 However,
it appears likely that if the biodiesel market becomes positive in terms of
both volume and margin, every source of feedstock in the tri-state region is
likely to produce biodiesel
4 Long-term,
an independent producer faces a number of competitive challenges in competition
with an integrated operation:
• Cost
of feedstock will inevitably include a small upside to provide margin to the
crush facility;
• Pre-processing
(otherwise known as refining) results in residuals – soap stocks and other
“bottoms” that must be marketed; and
• Access
to a secure, long-term supply of required feedstock is not secure
Feedstock Availability
Implications from Feedstock Availability
4 Independent
biodiesel production is unlikely to be viable: there are very few independent
refiners remaining in the U.S.
4 Options
NDBDT appear to include either a substantial long-term relationship with an
existing market player or construction of new crush capacity
4 SDSP and
West Central Soy have expressed interest in long term management relationships
4 However,
no one expressed willingness to “put skin in the game,” without “looking
closely at the numbers”
4 There
appears to be no real advantage for existing crush facilities to participate in
production of biodiesel off-site, although most would not dismiss consideration
out of hand
Viability of New Crush Capacity
Soybean Production vs. Crush Capacity
4 Regional crush capacity, particularly in North Dakota, handles only a fraction of local soybean production
4 But local / regional consumption of soybean meal is a
better measure of future venture viability
Feedstock Availability
Soybean Crushing Facilities
Feedstock Availability
Implications for New Crush Capacity
4 U.S.
crush capacity has declined by 14% over the past two years, despite new
capacity in Minnesota
4 Declining
demand for soybean meal has been driven by
• Domestic
livestock numbers are not increasing;
• World
production, particularly in Brazil and Argentina, has increased
• China is buying NO soybean meal on the international market
• Recent
high market prices (driven by tight supplies) have created some product
switching
4 North Dakota soybean meal consumption is small compared to existing state crush capacity
(and not increasing)
Feedstock Availability
Implications for New Crush Capacity
4 New MN
crush capacity has created significant disruption to historic meal markets
• All
players report more difficult market conditions
• Basis
and freight rate pressures have created problems with unit car rail shipments
to Mexico
4 There is
little competitive advantage for a new crush facility in North Dakota except by
looking north
4 To
proceed, NDBDT needs to understand the long-term opportunity of a Canada export market
4 It will
also be necessary to carefully weigh the trade-offs between size required to
support biodiesel production and efficiencies of scale
• 12M
gpy biodiesel uses oil from approximately 800 tpd soy crush
• All
other crush facilities in the tri-state region are about three times that size!