|
|
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|
|
CCAR Export SalesHistorically,
Air Products total international sales for refrigeration
services have approximated domestic sales levels. Commensurately,
Air Products anticipates that international CCAR sales
will approach domestic sales levels, but subject to some
delay. Given the absence of formal market studies for
overseas demand and of significant international marketing
activity to date, it was assumed that first export sales
would be delayed until 2004. Subsequent, overseas sales
were estimated to be one CCAR unit in 2004, three units
in 2005, and four units in 2006. Quantitative Benefits
to the U.S. Economy
|
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Table
8. Base Case Cash Flows from Improved
Quality, Yield, and Production Rates
and from Reduced Refrigeration Costs |
|||||
Year |
CCAR
replacement of mechamical systems |
CCAR
replacement of cryogenic systems |
Combined
cash flow |
||
Cash
flow from quality improvement |
Cash
flow from yeild improvement |
Cash
flow from higher production |
Cash
flow form cost reduction |
||
(Millions
2001 dollars) |
|||||
| 1996 | INVESTMENT
YEARS |
0.8610 |
|||
| 1997 | 0.9150 |
||||
| 1998 | 0.6020 |
||||
| 1999 | 0 |
||||
| 2000 | 0 |
||||
| 2001 e | 0 |
||||
| 2002 e | 0 |
0 |
0 |
0.832 |
0.8320 |
| 2003 e | 10.4 |
3.952 |
0.2184 |
2.496 |
17.0664 |
| 2004 e | 31.2 |
11.856 |
0.6552 |
4.160 |
47.8712 |
| 2005 e | 52.0 |
19.760 |
1.0920 |
5.824 |
78.6760 |
| 2006 e | 72.8 |
27.664 |
1.5288 |
8.320 |
110.3128 |
| 2007 e | 72.8 |
27.664 |
1.5288 |
8.320 |
1110.3128 |
| 2008 e | 72.8 |
27.664 |
1.5288 |
8.320 |
110.3128 |
| 2009 e | 72.8 |
27.664 |
1.5288 |
8.320 |
110.3128 |
| 2010 e | 72.8 |
27.664 |
1.5288 |
8.320 |
110.3128 |
| 2011 e | 72.8 |
27.664 |
1.5288 |
8.320 |
110.3128 |
| 2012 e | 72.8 |
27.664 |
1.5288 |
8.320 |
110.3128 |
| 2013 e | 72.8 |
27.664 |
1.5288 |
7.488 |
109.4808 |
| 2014 e | 62.4 |
23.712 |
1.3104 |
5.824 |
93.2464 |
| 2015 e | 41.6 |
15.808 |
0.8736 |
4.160 |
62.4416 |
| 2016 e | 20.8 |
7.904 |
0.4368 |
2.496 |
31.6368 |
Estimated
cash flows for the Base Case Scenario and Optimal Scenario
were used to compute several projected measures of the
public return from ATPs investment in CCAR technology
development: net present value, internal rate of return,
and benefit-to-cost ratio. They are summarized in Tables
9 and 10. (See Appendices B and C for
details.) The net present values of separate benefit
components were computed along with the total net present
value. The component measures for the Base Case Scenario
are included in Table 9 and for
the Optimal Scenario in Table 10.
Table
9. Base Case Net Present Value, Internal
Rate of Return, and Benefit-to-Cost Ratio |
|||||
Replacing
mechanical systems |
Replacing
cryogenic systems |
Combined
economic impact |
|||
Economic
ipact of improved quality |
Economic
impact of improved yield |
Economic
impact of faster production |
Economic
impact of reduced cost |
||
| Net present value (million) | $301 |
$113 |
$4 |
$33 |
$459 |
| Internal rate of return | 83% |
||||
| Benefit-to-cost ratio | 220:1 |
||||
Table
10. Optimal Scenario Net Present Value,
Internal Rate of Return and Benefit-to-Cost
Ratio |
|||||
Replacing
mechanical systems |
Replacing
cryogenic systems |
Combined
economic impact |
|||
Economic
ipact of improved quality |
Economic
impact of improved yield |
Economic
impact of faster production |
Economic
impact of reduced cost |
||
| Net present value (million) | $387 |
$146 |
$6 |
$41 |
$585 |
| Internal rate of return | 90% |
||||
| Benefit-to-cost ratio | 280:1 |
||||
Among the
component measures, CCAR-induced quality improvements
had the greatest economic impact, representing 66 percent
of the total $459 million net present value benefit in
the Base Case Scenario. Yield improvements contributed
25 percent while faster production rates contributed
only 1 percent to the total net present value. Cost savings
from displacing liquid nitrogen and carbon dioxide with
CCAR contributed 7 percent to net present value.
As with the Base Case Scenario, the Optimal Scenario showed the bulk of economic benefits coming from replacing mechanical refrigeration systems, through quality and yield improvements, and through faster production.
A comparison
of the Base Case Scenario and Optimal Scenario indicates
that economic impact according to the net present value
measure was roughly proportional to the number of installed
CCAR units. The Optimal Scenario had a 23 percent higher
number of installed CCAR units than the Base Case Scenario
and generated a 22 percent higher net present value and
27 percent higher benefit-to-cost ratio. Internal rates
of return do not behave in a linear manner and changed
by only 8 percent for the Optimal Scenario.
The ATP-funded
CCAR technology development is expected to generate significant
incremental U.S. exports over the 20042016 time
period. Average Base Case annual export revenues for
CCAR are estimated at $4.8 million dollars. Average Optimal
Scenario annual export revenues are estimated at $6 million
dollars.
Air Products
has intellectual property rights to CCAR technology under
existing patents and can thereby control the sale and
installation of CCAR units for the next 14 years. Future
benefits to Air Products in the form of incremental revenues
and profits provide their key motivation for marketing
the CCAR technology and reaching beyond the food processing
industry. The resulting CCAR sales are the vehicle by
which Air Products customers and consumers will
realize economic benefits from improved quality, yield,
production rates, and reduced operating costs in food
processing and other industries.
To assess
Air Products motivation to move the CCAR technology
forward, we estimated incremental revenue streams corresponding
to the Base Case Scenario, as shown in Table
11.
Table
11. Air Products Revenue Streams from
Base Case |
||
Cumulative
CCAR units U.S. and overseas |
Estimated
revenues sale of refrigeration ($ million) |
|
| 2002 e | 1 |
0.6 |
| 2003 e | 5 |
3.0 |
| 2004 e | 12 |
7.2 |
| 2005 e | 22 |
13.2 |
| 2006 e | 35 |
21.0 |
| 2007 e | 35 |
21.0 |
| 2008 e | 35 |
21.0 |
| 2009 e | 35 |
21.0 |
| 2010 e | 35 |
21.0 |
| 2011 e | 35 |
21.0 |
| 2012 e | 35 |
21.0 |
| 2013 e | 35 |
21.0 |
| 2014 e | 30 |
18.0 |
| 2015 e | 23 |
13.8 |
| 2016 e | 13 |
7.8 |
Discounting
revenue streams in Table 11 at 9 percent (a likely proxy
for the cost of funds of a major U.S. corporation), the
present value of projected revenues from CCAR installations
in the food processing, volatile organic compound recovery
and liquid natural gas markets was projected to be $64.8
million. For the Optimal Scenario, the present value
of revenue streams was projected to be $66.9 million.
In the absence of proprietary information about Air Products internal
cost structure, it was not possible to estimate CCARs
actual profit contributions.
Food safety
concerns have resulted in increased demand for fully
cooked product. However, food items, even if fully cooked
can grow bacteria in the 40°F to 141°F temperature
range, the so called danger zone. CCAR is
an innovative refrigeration technology that can accelerate
the rate of cooling of hot, cooked, further-processed
foods and facilitate passing through the danger
zone quickly, thereby minimizing food safety concerns.
Cryogenic
refrigeration (liquid nitrogen and carbon dioxide) can
also be used to accelerate falling through the
danger zone. However, liquid nitrogen and carbon
dioxide systems achieve this benefit at four times the
cost of conventional mechanical refrigeration and at
twice the cost of CCAR technology. As such, the CCAR
technology promises to be a cost-effective enabling technology
for promoting food safety in the manufacturing process
of precooked, further-processed foods.
The food
service industry is subject to Hazard
Analysis and Critical Control Points (HACCP) food
safety regulations, requiring labor-intensive monitoring
of food items during the time interval between cooking
and getting temperatures down to safe levels. When food
service establishments replace previously uncooked food
with precooked, further-processed foods, the need to
bring food temperatures to cooking levels is eliminated,
reducing labor requirements for HACCP compliance. Cost
savings from reduced labor requirements can improve the
operating economics of the food service industry and
contribute to its continued economic vitality and growth.
At the
time of the 1995 proposal to ATP, it was anticipated
that CCAR technology would displace mechanical refrigeration
systems that use CFC and other ozone depleting refrigerants.
This expectation is unlikely to be realized. Many industrial
refrigeration systems have already been converted from
CFC and other ozone-depleting refrigerants to ammonia-based
systems (Andersen, International Institute of Ammonia
Refrigeration; Shepherd, Toromont; Stellar Group (Interview)).
In addition, the economics of CCAR technology are attractive
only in the 70°F to 150°F operating
range, not in the warmer operating range of mechanical
refrigeration applications.
While impact
in the form of CFC reduction is unlikely to materialize,
a different pathway for reducing harmful emission can
now be identified where CCAR provides distributed refrigeration
through refrigeration units located at the site of use.
By replacing liquid nitrogen and carbon dioxide cryogens
with CCAR, diesel emissions from hauling cryogens to
the site of use can be entirely avoided. The beneficial
emissions impact of eliminating cryogen transportation
can be substantial over the 10-year operating life of
each CCAR unit. With 42 million pounds of annual production,
each food processor would utilize over 8 million gallons
of cryogen. Diesel powered trucks, each holding 7,000
gallons, would make 1,200 round-trips to meet cryogen
demand from one food processing plant. Across 1012
plants deploying CCAR units, 12,00014,000 annual
round trips can be avoided.
According
to recent research (Corbet and Fischbeck, 2000), air
emissions from cargo ships and ocean-going ferries powered
by diesel engines are among the most polluting combustion
sources per ton of fuel consumed. These findings are
prompting vigorous regulatory activity. The International
Maritime Organization is expected to implement new nitrogen
oxide reduction regulations. The European Union is expected
to set tougher limits on marine fuel sulfur levels. Under
the 1990 Clean Air Act, the U.S. Environmental Protection
Agency is developing regulations to reduce emissions
from diesel-powered marine engines.
Replacing diesel fuel with natural gas (in the form of liquid natural gas) for selected marine applications is expected to provide considerable environmental benefits. A March 2000 study conducted by Commonwealth Scientific Research Organization (Cope and Katzfey, 1998) referenced emission levels for heavy duty transport vehicles running on diesel fuel and natural gas. Natural gas-fired engines had significantly lower carbon monoxide, nitrogen oxide, and particulate (PM10) emissions than diesel engines. Hydrocarbon emissions from gas-fired engines were higher than diesel engines. However, this could be remedied by utilizing catalysts. Findings are summarized in Table 12.
Table
12. Emission Characteristics of Natural
GasFueled Transportation Vehicles
Versus Diesel-Fueled Vehicles |
||||
Emission
rates (grams/km) |
||||
CO |
NOx |
HC |
PM10 |
|
Existing
fleet |
33.00 |
22.00 |
3.70 |
1.00 |
Low
sulfur diesel |
1.20 |
14.00 |
0.87 |
0.11 |
Natural
gas |
0.66 |
9.90 |
3.61 |
0.05 |
Natural
gas* |
0.71 |
7.20 |
9.82 |
0.01 |
Note:
CO, carbon monoxide; NOx, nitrogen oxide; HC, hydrocarbons.
Source: Cope and Katzfey, 1998; *Motta
et al., 1996.
Assuming
heavy duty road transport emission statistics provide
an appropriate surrogate for large marine diesel engines,
a comparison of emission rates of natural gas with other
fuel sources suggests that conversion to liquid natural
gas could result in a 98 percent reduction of carbon
monoxide emissions , 55 percent reduction in nitrogen
oxide emissions, and 95 percent reduction of particulates.
Volatile
organic compound (VOC) emissions are regulated at the
federal and state levels. These regulations drive the
U.S. VOC recovery and abatement market. The VOC abatement
market is projected to reach revenue levels of $4.3 billion
(Power Engineering, 2000). If CCAR were to provide
a novel and economically viable VOC refrigeration technology,
it could then contribute to increased competition within
the VOC abatement industry. Increased competition could
lead to higher efficiency levels and lower VOC emissions
over time. Estimating VOC-related benefits would require
a formal market study and is beyond the scope of this
work.
After
Air Products received the CCAR patent in 1996, new
technical knowledge was developed during the subsequent
ATP-funded project, making it possible to reach step-out
performance levels with
The substantial
performance improvements associated with the design and
fabrication of these system components were recognized
by Chemical Engineering Magazine when CCAR was
chosen as a finalist for the 1999 Kirkpatrick Award.
Additional dissemination of information about CCARs
step-out performance characteristics is likely to lead
to expanded utilization of low leakage seals, high pressure
heat exchangers, and honeycombed investment casting technologies
in other industries. These innovations and associated
opportunities for cross-industry knowledge diffusion
and use beyond the CCAR technology are described in Appendix
B.
As a result
of the CCAR development experience, both Air Products
and Toromont reported enhanced organizational capabilities.
Return to Table of Contents or go to next section.
Date created: December
2001
Last updated:
August 2, 2005
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