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5. Short-Term Impacts on ULSD
Supply
Background
This chapter addresses the transition to ultra-low sulfur diesel fuel (ULSD)
when the ULSD Rule takes effect in 2006. Whether there will be adequate
supply was one of the key questions raised by the House Committee on Science
in its request for analysis. The Charles Rivers Associates/Baker and OBrien
(CRA/BOB) study done for the American Petroleum Institute (API) estimated
a shortfall of 320,000 barrels per day when the regulation is introduced
in 2006. The issue of future supply of highway diesel fuel received considerable
attention during the comment period on the Notice of Proposed Rulemaking
(NPRM) published by the U.S. Environmental Protection Agency (EPA).96 The
EPA noted that numerous commenters to the proposed rule indicated that
they believed that the 15 ppm sulfur cap would cause shortages in highway
diesel fuel supply but that a number of commenters also thought otherwise
(i.e., that future supplies would be adequate).97
While it is possible that some refiners may decide to shut down altogether
because of this regulation, others might just abandon the highway diesel
market. Few refineries can operate without producing gasoline because gasoline
is a high-margin, high-volume product that provides significant revenue
to refiners. On the other hand, it may be possible for some refineries
to operate without producing ULSD. Some refineries could sell higher sulfur
distillate products into the non-road, rail, ship, or heating oil markets.
Some refiners could also decide to export distillate products if they are
in the right location.
Because there are other markets for distillate products, some refiners
may opt to delay upgrading their facilities to produce ULSD. Refiners
recent experiences with investing to meet new fuel standards have not been
encouraging. As the EPA pointed out in the Regulatory Impact Analysis for
this regulation, both the 500 ppm diesel fuel and reformulated gasoline
standards resulted in overinvestment and oversupply of the fuels, and of
late, relatively poor refining margins have not allowed refiners to recoup
the full cost of environmental standards.98 Overly aggressive expansion
to produce ULSD could result in similar oversupply of product and reduced
margins, and some refiners may therefore wait to see whether adequate margins
develop.
Another uncertainty is possible regulation of non-road diesel fuel. In
addition, some States are proposing their own regulations for highway diesel
fuel, which may add to the EPA requirements. Some refiners may wait to
see whether additional requirements are established for highway or non-road
diesel before investing to upgrade their refineries to produce ULSD.
The EPA has taken steps to monitor the ULSD supply situation. Its Final
Rulemaking requires refiners and importers to submit a variety of information
to ensure a smooth transition, and to evaluate compliance once the program
begins. Refiners and importers expecting to produce highway diesel in 2006
are required to register with the EPA by December 31, 2001. Annual precompliance
reports are required from 2003 through 2005, containing estimates of ULSD
and 500 ppm sulfur fuel that will be produced at each refinery and projections
of the numbers of credits that will be generated or needed by each refinery.
A time line for compliance is also required, as well as other information.
The EPA will produce an annual report summarizing information from the
precompliance reports without disclosing individual company plans. This
information will give refiners a better indication of the potential market
for credits and the availability of credits in each region. The EPA will
also require annual reports after the program takes effect, in order to
monitor production of ULSD and 500 ppm sulfur diesel fuel.99 In addition,
an independent advisory panel will be set up to look at issues of diesel
supplies and related technologies, and to report to the EPA annually on
the progress being made by industry to comply with the ULSD Rule.100
Cost Analysis
To assess the supply situation during the transition to ULSD in 2006, estimates
of ULSD costs and supply were developed based on refinery-specific analysis
of investment requirements. The relative costs can provide insights into
whether refiners will make the investments to produce ULSD and give an
indication of possible supply. Four scenarios describing investment behavior
under different assumptions were developed to provide a range of possible
responses to the ULSD Rule.
Using refinery-specific data collected by the Energy Information Administration
(EIA), the ULSD product costs are estimated for each refinery based on
its size, the sulfur content of the feeds, the fraction of cracked stocks
in the feed, the boiling range of the feed, and the fraction of highway
diesel produced. Cost curves were then developed in a three-step process.
In the first step the cost of producing ULSD for each refinery was estimated
for several strategies of ULSD production, based on refinery operation
data for 1999. The strategies start by maintaining ULSD production at current
highway diesel production levels. Then they consider both reductions and increases
from current production to find the most economical level of production
for individual refineries. In the second step the cost and volume information
for individual refineries is used to construct cost curves for the U.S.
refining industry using a variety of scenario assumptions about how refiners
may respond with refinery investment in preparation for summer 2006, when
ULSD requirements for highway diesel begin. The third step consists of
adjusting the cost curves to reflect changes in refinery capacity from
1999 to 2006.
Appendix D describes in detail the refinery-by-refinery analysis and development
of the cost model used as the basis for developing the cost curves. Table
6 provides samples of the ULSD cost model results for cases representing
various refinery configurations and situations. The case descriptions in
the table indicate whether the refinery in that particular case falls within
the higher or lower part of the range in terms of hydrotreater unit capacity,
sulfur content of the hydrotreater feed, and the fraction of cracked stock
in the feed. The costs in this analysis assume a 5.2-percent after-tax
return on investment, which is estimated to be equivalent to the 7-percent before-tax
return on investment assumed in the EPAs analysis.
The cases in Table 6 were designed to represent the types of individual
refinery situations that lie behind the cost curve results. Cases A and
B represent refiners producing highway diesel fuel as a high fraction of
their distillate pool. These refineries run a higher sulfur crude oil,
do not have hydrocracking facilities, and have relatively large-scale highway
diesel production. Thirty-two percent of the highway diesel they produce
comes from cracked stock, which is about the average for Petroleum Administration
for Defense District II (PADD II) (see Appendix D, Table D1). The cost
of producing highway diesel at current production levels in the refineries
of Cases A and B is 6.0 cents per gallon if a new hydrotreater is required
and 5.0 cents per gallon if the current hydrotreater can be revamped. The
cost of the incremental hydrogen to produce ULSD represents 28 percent
of the added cost for Case A and 35 percent for Case B.
Cases C and D have the same volumes as A and B but use a lower sulfur crude
oil. The cost of the added hydrogen is similar to the result for Cases
A and B, because this analysis is estimating the cost to produce ULSD with
7 ppm sulfur rather than the current 500 ppm. Total costs, however, are
just 0.1 cents per gallon lower for a revamped unit (Case D compared to
Case B) and 0.6 cents per gallon lower for a new unit (Case C compared
to Case A).
Case E shows a refinery producing ULSD only from straight-run distillate
derived from a high-sulfur crude. The cost of production from a hydrotreater
that has been revamped is only 2.7 cents per gallon. This is slightly more
than half the cost of Case B, which has to handle 32 percent cracked stocks.
Cases G and H represent the same mix of hydrotreater feed as in Cases A
and B, but the total feedstock volume is only 10,000 barrels per day, compared
to 50,000 barrels per day in Cases A and B. This is the type of situation
represented by comparing ULSD production in PADD IV with that in PADD II
and PADD III. For a new hydrotreater unit, the ULSD cost would be 8.3 cents
per gallon (2.3 cents per gallon higher than in Case A). If the unit can
be revamped, the cost is 6.1 cents per gallon (1.1 cents per gallon higher
than in Case B).
Some refineries currently produce high volumes of distillate product but
no highway diesel. These refineries might consider entering the highway
diesel market when the ULSD Rule takes effect if they anticipate that the
price differential between ULSD and their other distillate products can
more than offset the added investment and operating costs they would incur.
Case I illustrates a non-road diesel producer converting to the production
of highway diesel. The refinery runs a moderately high-sulfur crude oil
and has substantial volumes of cracked distillates from the fluid catalytic
cracker (FCC) and coker units. Because of quality requirements for non-road
diesel products, cracked stocks still make up 45 percent of the feed to
the hydrotreater for highway diesel production. The large percent of cracked
stocks means a moderately high per-barrel investment and operating cost
for the hydrotreater. Additionally, the per-barrel cost for hydrogen is
quite high. Most of the refineries with high-volume distillate production
and no highway diesel production had costs of highway diesel production
in the higher portion of the cost range.
Cases J, K, and L provide an illustration of refineries achieving improved
economics by reducing the volume of ULSD diesel below current highway production
levels. As shown in Table 6, the cost of added hydrogen is generally a
large component of the cost of producing ULSD. The cost for hydrogen grows
as the fraction of cracked stocks increases, eventually requiring the construction
of new hydrogen production capacity. However, if there is only a modest
percent of cracked stock in the hydrotreater feed and the refiner reduces
the input to the hydrotreater, then the incremental hydrogen requirement
for ULSD production can be provided by existing refinery production sources.
Cases J and K show the costs for a new and revamped hydrotreater for a
refinery running a medium-sulfur crude and with 22 percent cracked stock
in the highway diesel production pool. Case L shows that if the input level
is reduced from 32,400 barrels per day to 20,700 barrels per day when the
unit is revamped, then the cost of ULSD production is reduced from 4.5
cents per gallon to 3.1 cents per gallon. Given the costs for Cases K and
L, the preferred option for the refiner would be Case K if the price differential
between highway and non-road diesel exceeds 6.9 cents per gallon and Case
L if the differential is less than 6.9 cents per gallon.101
These sample cases highlight several situations that can cause refineries
to have potentially high ULSD production costs and discourage them from
investing to produce ULSD. Small refineries with less than 10,000 barrels
per day of highway diesel production will have very high relative costs
unless they can revamp an existing unit. The fraction of cracked stocks
in the ULSD hydrotreater feed is extremely important. The need for hydrogen
increases with the fraction of cracked stocks and may require new hydrogen
production capability. If a refinery's other distillate products are primarily
non-road diesel fuels with cetane requirements that limit the volume of
cracked stocks, then it is often impossible for the refinery to reduce
the cracked stocks going into highway diesel. Thus, refineries with moderate
cracked stocks and a smaller scale will have high ULSD cost, and refineries
with high cracked stocks and a moderate to large scale may also have ULSD
costs that they view as uncompetitive.
Analysis of ULSD Production Decisions
Economic Considerations
Scenarios are analyzed to estimate the volumes of ULSD that refiners might
produce at the beginning of the ULSD requirement in the summer of 2006.
Each scenario defines a set of strategic principles that might characterize
the economic rationale behind investment decisions that may be commonly
made by refiners in this situation. Refiners have a choice as to how much
ULSD they produce. Some refiners may decide to produce no highway diesel
when the ULSD Rule comes into effect. While most refiners who are currently
producers of highway diesel will likely continue to produce it, they could
increase or decrease production from current levels. Because there is uncertainty
associated with refiners behavior, four supply scenarios were constructed,
any one of which may turn out to be closest to the actual behavior of the
refining industry in this situation.
In making the ULSD decision a refiner will look at the available options,
analyze the costs to produce various levels of ULSD, and determine the
impact on other distillate products. Then the refiner will try to estimate
his relative competitive position for producing ULSD. The competitive assessment
considers the cost of ULSD production for other refiners and looks at the
mid-term competition for market share, including an analysis of current
market share, regional market competition, the impact of new entrants that
may have a significant cost advantage, synergies with other refineries
within the same company, and potential changes in the price differential
between ULSD and non-road fuels on a mid-term basis.
In a number of past instances when refiners have been required to meet
new product specifications, they have not only made facility changes that
would enable them to meet the demand for the product with new specifications,
but have done so in such numbers and volumes that their ability to supply
the market has exceeded market demand. In the case of ULSD, refiners have
more choice in deciding to participate in the highway market or alternatively
to produce products only for non-road distillate markets. This choice becomes
a particular issue for refiners facing an expensive investment decision
and the likelihood that they would be at a significant competitive cost
disadvantage relative to other market competitors.
While most U.S. refiners look upon gasoline as an essential product, they
could operate in the refinery business without producing any highway diesel.
Thus, it is possible that some refiners will cease or significantly decrease
highway diesel production when ULSD specifications take effect in 2006.
This would create a transition market in which some refiners with higher
costs would decrease production and be replaced by more cost-competitive
refiners.
The set of more cost-competitive refiners falls into two categoriesthose
increasing production of highway diesel from current levels and those currently
producing little or no highway diesel. Will refiners in the second group
jump into the market because they recognize that they would have a competitive
position, or will they wait to see how the supply and margin picture unfolds
before making a large-dollar commitment? Later entrants into the market
could also be the beneficiaries of improved technologies that reduce the
cost of compliance.
Refiners who estimate that their costs to produce ULSD are on the high
end of the range will be far less likely to invest to produce ULSD. No
one wants to be the marginal supplier after making a large investment,
especially when the product is a secondary fuel product. The question is
what differential cost will be perceived to be too highis it 1 or 2 cents
per gallon above what the refiner perceives is the average cost in the
market? How does the refiner assess the possible competitive threats of
a large-volume refiner who has previously not been a highway diesel producer
but may now enter the market with better economics to produce highway diesel
and reduce market prices? Refiners will likely try to retain highway market
share, even if their relative competitive cost is modestly above the average
cost in the region, rather than shifting into new markets. Refining companies
with multiple refineries will view strategies in the context of their total
system and could rebalance production on a system basis.
One of the key decisions in preparing to produce ULSD is whether to build
a new hydrotreater or revamp an existing unit. This analysis assumes that
revamps are more likely if a refinery installed new distillate hydrotreating
units in the 1990s, or if the proportion of cracked stocks in the refinerys
hydrotreater feed is small. New units are assumed at refineries where current
hydrotreating capacity is less than highway diesel production. As shown
in Table 7, the estimates indicate that 46 percent of the refineries in
PADDs I-IV, accounting for 63 percent of highway diesel production capacity,
would revamp existing units. PADD IV has the lowest proportion of revamps
because of the larger amount of cracked stocks that refineries in that
region must process. PADD II has the highest percentage of revamps because
of the extensive upgrading that took place in the early 1990s and the moderate
levels of cracked stocks in the feed. The EPA assumed that 80 percent of
ULSD production capacity would be revamped units.
Supply Scenarios
The first of the four supply scenarios was developed based on the rationale
that there is a high probability that refiners will produce at least a
moderate level of ULSD. In the other three scenarios there is decreasing
probability that the additional volumes would be produced. The description
of the specific scenarios follows:
- Scenario 1Competitive Investment. The first scenario includes only those
refiners who are likely to prepare to produce ULSD in 2006. They currently
hold market share and are estimated to be able to produce ULSD at a competitive
cost. Refiners with highway diesel as a relatively low fraction of their
distillate production are assumed to abandon the market unless their cost
per unit of production is competitive at current highway diesel production
levels. Some refiners are assumed to reduce highway diesel production below
current levels when they have a more competitive ULSD production at a reduced
production rate.
- Scenario 2Cautious Expansion by Competitive Producers. In this scenario,
refiners base ULSD production decisions on the assumption that the price
differential between ULSD and non-road distillate products will remain
wide. Current producers with competitive cost structures for ULSD production
and high fractions of highway diesel production (greater than 70 percent
of total distillate production) are assumed to maintain current production
levels and may even push production of ULSD toward 100 percent of distillate
production if only minor increases in per unit production costs occur at
increased volume. Other refiners are also assumed to increase their fraction
of highway production if the economics are only slightly poorer at higher
volumes. Those whose current production is focused primarily on non-road
markets are assumed to stay with those markets.
- Scenario 3Moderate New Market Entry. While refineries that are currently
producing little or no highway diesel may be hesitant to jump into the
ULSD market, this scenario assumes that a select few will decide to take
the risk. This is based on the belief that a limited number of refineries
think they can gain market share without depressing the price differential
between ULSD and non-road diesel to the extent of ruining margins and return
on investment. These refiners are assumed to have favorable cost structures
for ULSD production (probably in the lower third).
- Scenario 4Assertive Investment. The fourth scenario assumes that a larger
number of refiners will compete to increase their shares of the ULSD market.
In this scenario, refiners believe that most of their competitors are overly
cautious, and that they can succeed by taking a contrary strategy (which
in reality is adopted by far more refiners than anticipated).
Imports
Historically, imports have been a small part of low-sulfur diesel supply.
The only significant volumes of low-sulfur diesel fuel have been imported
into PADD I, which totaled 123,000 barrels per day in 1999 then declined
slightly in 2000 to 106,000 barrels per day (Figure 4). Imports made up
5 percent of low-sulfur diesel product supplied for the United States as
a whole in 2000 and 14 percent of product supplied in PADD I. The PADD
I imports come from three main sources Canada, the Virgin Islands, and
Venezuela. Low-sulfur diesel imports from the Virgin Islands reached 62,000
barrels per day in 1996 and have fallen to 47,000 barrels per day in 2000.
Imports from Canada, which have been fairly constant for the past few years,
totaled 35,000 barrels per day in 2000. Imports from Venezuela grew sharply
in 1998 and 1999, to 22,000 barrels per day in 1999, before falling to
8,000 barrels per day in 2000.
Other countries are also planning to lower the sulfur content of diesel
fuel. Canada has announced plans to require a 15 ppm sulfur diesel fuel
in mid-2006, mirroring the U.S. regulation.102 A 50 ppm ULSD becomes mandatory
across Europe in 2005. The European Commission is also discussing a gradual
phase-in to 10 ppm sulfur, starting with a 10-percent supply requirement
in January 2007.103
Given these changes, Canadian refiners currently exporting to the United
States may make the investment to produce ULSD for the U.S. market. The
East Coast has been the main market for a large refinery in the Virgin
Islands that is jointly owned by Amerada Hess and PdVSA, Venezuelas national
oil company. Both of the plants owners see the United States as a strategic
market. Venezuela is planning to upgrade its domestic refineries, but because
it is also interested in expanding its presence in Latin American markets,104 it is not clear whether it would supply ULSD to the U.S. market.
Refineries worldwide will be investing to produce lower sulfur diesel fuel.
Even a refinery designed to produce diesel with 50 ppm sulfur could produce
some amounts at less than 15 ppm. Thus, it is conceivable that limited
amounts of ULSD could be imported from other sources. In the early part
of the transition to ULSD, imports beyond historical levels probably are
less likely and quantities less than historical levels probably are more
likely.105
Demand Issues
The number of vehicles that actually need ULSD when the regulation takes
effect in 2006 will be small. The EPA has mandated that 80 percent of the
refinery output of less than 500 ppm diesel fuel be ULSD in order to provide
retail availability for the trucks that need ULSD. As a result, the supply
of ULSD will be much larger than the demand provided by vehicles that need
ULSD. The concern is whether enough fuel will be available to supply all
highway diesel vehicles.
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Current production of low-sulfur diesel fuel is greater than what is required
by the market. Highway diesel fuel consumption accounted for 86 percent
of transportation distillate demand in 1999. Yet low-sulfur diesel product
supplied (a surrogate for demand) has nearly equaled transportation distillate
demand in recent years (Figure 5). Consequently, the amount of low-sulfur
diesel fuel currently being consumed in the market is more than 15 percent
higher than that required for highway vehicles. There are several reasons
for this. The logistics of the distribution system dictate in some areas
that only one type of fuel can be distributed. Because the price differential
between low-sulfur diesel and other distillate products has been only 2
to 3 cents per gallon or less in recent years, the incentive to maintain
separate product infrastructure has not been great. An important question
is the extent to which the demand for ULSD will remain above that required
for highway vehicles after the ULSD regulation takes effect in 2006. A
larger price differential between ULSD and higher sulfur distillate products
may provide some incentive to avoid consuming ULSD in markets where it
is not required, but in some areas it may continue to be impractical to
distribute more than one product.
It is also unclear how much 500 ppm sulfur diesel fuel will be in the market
after the regulation takes effect. Refiners will be investing for the long
term and not just to produce 80 percent ULSD in the transition period,
and many refiners (if they invest to produce ULSD at all) may be producing
100 percent ULSD in the transition period. Some refiners could continue
to supply 500 ppm diesel fuel by purchasing credits, and some small refiners could continue
to produce 500 ppm sulfur fuel until 2010 (see discussion on "500 ppm Diesel Supply Issues in 2006").
For the above reasons, the amount of ULSD actually needed to balance demand
in 2006 is highly uncertain. A range of demand estimates has been developed
to account for some of the uncertainty. In the mid-term analysis for this
study, transportation distillate demand in PADDs I-IV106 in the 2/3 Revamp
case (see Chapter 6) amounts to about 2.7 million barrels per day. At the
U.S. level, transportation distillate demand is projected to be 3.0 million
barrels per day in 2006, increasing by 3.2 percent per year from the 1999
level of 2.4 million barrels per day. This compares to an average rate
of increase of 3.5 percent per year from 1982 to 1999. Transportation distillate
demand rose sharply from 1982 to 1989 and again from 1991 to 1999, at annual
average growth rates of 4.7 and 4.0 percent, respectively, but fell in
1990 and 1991, at the time of the Iraqi invasion of Kuwait.
The probable downgrading of some ULSD to 500 ppm sulfur diesel in the distribution
system was not taken into account in this part of the analysis. The requirement
to produce 80 percent ULSD is at the refinery gate, and supplies that are downgraded to a higher sulfur level in the distribution
system can still be sold as highway diesel during the transition period.
Cost Curves and Demand Estimates for 2006
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Figure 6 shows the combined cost curves for PADDs I-IV for each of the
scenarios, together with four estimates of demand.107 The EPA estimates
that, under the small refiner option, up to 5 percent of the market could
delay making the transition to ULSD until 2010.108 In addition, the temporary
compliance option mandates that ULSD production must constitute 80 percent
of low-sulfur diesel production. Assuming the full extent of the small
refiner, temporary compliance, and credit trading provisions of the Rule,
ULSD demand is estimated at just over 2.0 million barrels per day (Demand
A). As indicated above, imports from the Virgin Islands and Canada are likely to continue. At their recent historical level of 80,000 barrels
per day, imports would reduce domestic demand for ULSD to 1.95 million
barrels per day (Demand B, which matches the demand projection in the mid-term
analysis described in Chapter 6). Demand C in Figure 6 is based on the
same assumptions as Demand B and, in addition, assumes that ULSD will be
used only for highway consumption (86 percent of transportation distillate
demand), resulting in a demand estimate of 1.7 million barrels per day.
Demand D assumes a higher estimate for imports116,000 barrels per daywhich
was the level for PADDs I-IV in 2000.
The cost curves in Figure 6 show the estimated volumes of ULSD that could
be produced at increasing cost levels. The curves show the wide range of
costs to produce ULSD across the population of U.S. refiners that might
choose to become ULSD producers. There are some refiners at the upper range
of the cost curves that would have much higher costs and could have concerns that margins in the marketplace
would not be high enough to provide a satisfactory rate of return.
The cost curves in Figure 6 were developed using capital cost and return
on investment assumptions consistent with those used in the EPAs analysis.
Those assumptions were used in order to provide a comparison with the EPAs
analysis results and should not be viewed as the assumptions that EIA considers
the most likely. However, concerns about the adequacy of ULSD supply are
based on the possible reluctance of higher cost producers to invest to
produce ULSD in 2006. Because of the uncertainty of these assumptions,
two additional sets of supply scenarios are provided, using higher capital
cost assumptions and a higher required return on investment, as discussed
later in this chapter.
Total ULSD production on the Scenario 1 (Competitive Investment) and Scenario
2 (Cautious Expansion) cost curves extends beyond the lower demand estimates
(C and D) and would meet the highway demand estimates even if no ULSD imports
were available. In Scenario 3 (Moderate New Market Entry), production just
reaches the mid-term analysis demand estimate that includes imports (Demand
B). In Scenario 4 (Assertive Investment), ULSD production surpasses the
mid-term analysis demand estimate that does not include imports. None of
the supply curves, however, provides enough supply to reach the demand
estimate that does not include the temporary compliance option (see Table
8 below). Some refiners may be able to produce ULSD with a cost of about
2.5 cents per gallon; however, at the volumes needed to meet demand, costs
are estimated at 5.4 to 6.8 cents per gallon.109 ULSD prices could show
an even higher differential if supply falls short of demand.
The four factors that have the strongest influence on the cost of producing
ULSD are the production volume of 500 ppm diesel, the fraction of cracked
stocks in the feedstock, the scale of the hydrotreater unit, and whether
a new or revamped unit is required. Twenty-nine refineries in Scenario
1 are in the cost range below 4 cents per gallon, and all are refineries
for which it is assumed that the existing unit could be revamped. Most
of these refineries have little or no cracked stocks in the hydrotreater
feed to produce ULSD. For the few that do have cracked stocks, a revamped
unit at a reduced throughput was found to obtain better economics of ULSD
production and put them in the cost range under 4 cents per gallon. Twenty-five
refineries are in the cost range from 4 to 5 cents per gallon. Thirteen
are assumed to construct new units, and most of these refineries have a
low percentage of cracked stocks in the hydrotreater feed. A couple of
units in this cost range are assumed to reduce throughput from current
highway diesel production levels. Above 5 cents per gallon, a couple of
refineries with a high percentage of cracked stocks are assumed to revamp
existing units. The rest, which have moderate levels of cracked stocks,
are assumed to build new units. The refineries above 5 cents per gallon
also include a number of smaller refineries with ULSD production under
10,000 barrels per day.
Regionally, PADD IV has the highest estimated costs for ULSD production.
The refineries in PADD IV are smaller on average, have more cracked stocks
to process, and have the lowest proportion of revamps. In PADD I, a large
heating oil market provides an outlet for some of the more difficult streams
to hydrotreat so it tends to show lower costs for producing ULSD. PADD
II refineries are also toward the lower end of the cost curve. They tend
to be more moderate in size (which gives better economies of scale), have
moderate levels of cracked stocks, and had extensive revamps in the early
1990s to put them in a better position to upgrade to produce ULSD. PADD
III has a mixture of small and large refineries with a variety of configurations
and as a result shows a wide range of lower and higher cost ULSD producers.
Some of the refineries in PADD III are among the highest as far as the
proportion of cracked stocks in the feedstock going to the hydrotreater.
Sixty-four percent of the refineries in PADD IV that are assumed to produce
ULSD in Scenario 4 have estimated costs greater than 5 cents per gallon
compared to 31 percent in PADD III, 22 percent in PADD II, and 17 percent
in PADD I.
Scenario 1 has the lowest production volume of the four scenarios but the
highest probability that production volumes of ULSD will at least reach
these estimates in 2006. Of the 87 refineries in PADDs I-IV that currently
produce highway diesel, only 66 are estimated to produce ULSD in Scenario
1. Of the 21 refineries that are estimated to terminate ULSD production
in Scenario 1, the cost of ULSD production ranges from 6 to 13 cents per
gallon.110 Two-thirds of these refineries currently produce less than 10,000
barrels per day of highway diesel. PADD IV refineries are disproportionately
in the higher cost range.
Scenario 2 assumes that the number of refineries that will produce ULSD
is the same as in Scenario 1, but that these refineries will increase production
if their competitive position is not greatly affected. Comparing Scenario
3 to Scenario 2, ULSD production is estimated to increase at nine refineries,
and one refinery that currently produces only non-road distillate product
is assumed to enter the ULSD market. All of these factors raise the estimated
production level in Scenario 3 by 129,000 barrels per day over that in
Scenario 2.
The probability of reaching the total volume production of Scenario 4 is
the lowest. In this scenario, refineries with higher costs of production
are assumed to enter the ULSD market in 2006. The added production volumes
in Scenario 4 come from three types of situations. First, some refineries
are assumed to expand production beyond the Scenario 3 level if unit costs
are only slightly higher. Second, five of the refineries entering the market
were viewed in Scenario 3 as having too high a cost. The third and largest
portion of additional volume comes from two refineries that currently are
not producers of highway diesel. All of the additional volume in Scenario
4 comes from refiners with costs of ULSD production higher than 5 cents
per gallon.
Table 8 shows the differences between the demand and supply estimates.
The largest shortfall, which occurs between Scenario 1 (assuming the most
cautious investment strategy) and the highest demand estimate, is estimated
at 770,000 barrels per day. The widest surplus, 517,000 barrels per day,
is under Scenario 4 (the most aggressive investment strategy) and the lowest
demand estimate that also accounts for import availability. Assuming the
mid-term analysis demand estimate, which is similar to the AEO2001 projection,
Scenarios 3 and 4 project sufficient supply.
Some analysts contend that demand could exceed the estimates in this analysis
that assume the temporary compliance option of 80 percent ULSD production.
Most refiners that invest to produce ULSD will plan to produce 100 percent
ULSD unless they have a market for the higher sulfur product after 2010.
Those producing 100 percent ULSD will generate credits which can then be
sold to those who decide to delay investing to produce ULSD. Credit trading
programs have been successful in the utility industry, but how well credit
trading will work in a less-regulated industry remains unclear. Refiners
may be less than enthusiastic about selling credits to their competitors
that would allow them to sell product produced at a lower cost in the same
market as ULSD, possibly at a price similar to the price of ULSD.111 Refiners
who wait to invest can also take advantage of improvements in technology
that could help them compete more effectively with those who invested early.
Credits could increase sharply in value if markets were tight, but they
would have less value if supplies were ample.
To provide a further range of demand estimates, Tables 9 and 10 show the
projections for high and low macroeconomic growth cases along with the
supply estimates from the cost curves. Transportation distillate demand
is projected to increase by 4.0 percent per year from 1999 to 2006 in the
high macroeconomic growth case and by 2.7 percent per year in the low macroeconomic
growth case.
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Two additional sets of the four supply scenarios are provided that vary
the hydrotreater capital cost assumptions and the return on investment
assumption. The capital costs assumed in the initial set of four scenarios
in this chapter are similar to those used in the EPA analysis (see Chapter
7 for a comparison of capital cost assumptions). Because of the uncertainty
associated with the cost of installing distillate hydrotreating capable
of producing diesel fuel containing less than 10 ppm sulfur, a second set
of scenarios was developed assuming capital costs for the hydrotreater
units that are about 40 percent higher than the initial set (Figure 7).
The higher capital costs in this scenario reduce the projected production
of ULSD by 25,000 to 55,000 barrels per day and increase the cost estimates
from 0.4 cents per gallon to 1.0 cents per gallon.
A third set of supply scenarios was developed assuming a 10-percent required
return on investment (Figure 8), rather than 5.2 percent assumed in the
initial set of scenarios. The higher assumed rate results in a reduction
in production of 40,000 to 66,000 barrels per day across the four scenarios.
The cost estimates increase by 0.8 to 1.2 cents per gallon from the first
set of scenarios. Because of the reduced volumes, estimated production
levels in Scenario 3 fall short of the demand level projected in the mid-term
analysis (Demand B) in both the higher capital cost and higher required
return on investment sensitivities (Tables 11 and 12).
Balancing Demand and Supply in 2006
These supply curves, along with the demand estimates for 2006, indicate
the possibility of a tight diesel market when the ULSD Rule is implemented.
Supply scenarios that assume more cautious investment indicate inadequate
supply compared with the demand levels projected in the Annual Energy Outlook
2001. Only more aggressive investment scenarios or lower demand cenarios
show adequate supply to meet estimated demand. This analysis compares supply
and demand at an aggregate level. Maintaining a balance of supply and demand
across regions and throughout the distribution system would be more difficult.
Improvements in supply could result if more refiners undertook investments
to produce ULSD, if capacity expansions by refiners were greater than anticipated
in this analysis, and/or if more imports were available. On the demand
side, slower growth in the highway diesel market than these demand estimates
and/or curtailing of ULSD consumption for non-road uses would also improve
the situation.
If supplies fall short of demand, sharp price increases could occur to
balance supply and demand. That type of situation could result in a number
of responses, some of which could begin to occur as soon as the price differential
between ULSD and other products started to widenpossibly even before it
became clear that a market supply problem existed. Refiners would attempt
to maximize ULSD production. Some additional production may be possible
by, for example, shifting some non-road distillate or jet fuel streams
into ULSD. This would be limited, however, because only the lower sulfur
streams could be used and additional hydrotreating may be necessary. Imports
of jet fuel or other products could then replace the lost production of
those fuels. Additional imports of ULSD could be forthcoming if there were
large price differentials between markets. Such responses would require
higher costs, however, because lower cost options would be exercised first.
Sharply higher prices would also curtail demand for diesel fuel. Truckers
would reduce consumption to the extent possible and try to pass higher
fuel costs to customers, who would then look for alternative means to transport
goods.
In 2006, the quantity of fuel actually needed for vehicles requiring ULSD
will be much less than the required 80 percent of diesel production. If
it becomes apparent that the supply is inadequate, or that markets are
becoming tight, additional low-sulfur diesel supplies could become available
if the required proportion of ULSD production were reduced. Allowing more
500 ppm diesel into the highway market could alleviate some of the stress
on the market. If the requirement were 70 percent instead of 80 percent,
for example, the demand estimates shown in Table 8 would be reduced by
217,000 to 253,000 barrels per day, enough to eliminate the shortfalls
indicated except for Demand A in Scenario 1 and the highest demand estimate across all scenarios. However, a lower requirement for
ULSD production would reduce retail availability for the vehicles that
require ULSD. Other responses providing greater flexibility, increasing
participation, and encouraging technological improvements would also help
to alleviate supply concerns.112
Given the variety of responses, it is difficult to know the magnitude or
duration of a possible tight market situation. Supply shifts and demand
responses would require time before the effect would be felt. It would
take time for additional imports to enter the market, and importers would
have to believe that prices would remain high enough for long enough to
make it worthwhile to divert supplies from other markets.
Summary
Whether there will be adequate supply is one of the key questions raised
by the House Committee on Science in its request for analysis. To assess
the supply situation during the transition to ULSD in 2006, cost curves
and estimates of ULSD supply are developed based on refinery-specific analysis
of investment requirements. Supply is estimated for four scenarios of investment
behavior, and a range of demand is projected for comparison with the supply
curves. In addition, two other sets of supply sensitivities are provided,
assuming higher capital costs and higher required return on investment.
Supply scenarios that assume more cautious investment indicate inadequate
supply compared with the demand levels projected in the Annual Energy Outlook
2001. Only more aggressive investment scenarios or lower demand cenarios
show adequate supply to meet estimated demand. The two sets of supply sensitivities
show even lower production estimates than the initial set. This indicates
the possibility of a tight market supply situation when the ULSD Rule takes
effect in 2006. While considerable uncertainty exists in both the supply
and demand estimates, this analysis indicates that even though the market
could see supply meet demand at a cost increase for production between
5.4 and 7.6 cents per gallon, there are a number of scenarios in which
inadequate supply of ULSD could result.
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