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Prior to the 1970s, automobile air conditioning was a largely American phenomenon. By 1980, 80% of American new cars had factory-installed air conditioning and a large portion of the output of the Japanese auto industry was air conditioned as well. Over the 20 years between 1980 and now, penetration of air conditioning in car and light truck sales has approached 100% in both the U.S. and Japan and is becoming increasingly popular in Europe. Not only is vehicle air conditioning a preferred comfort feature, but in many car models total engine power (and fuel consumption) at highway speed is less with the windows up and the air conditioning running than it is with the windows down and the air conditioning off. Worldwide, approximately 45 million air-conditioned cars are produced annually.
Pre-Montreal Protocol, automobile air conditioning systems used CFC-12 refrigerant- based vapor compression cycles. CFC-12 was universally replaced with HFC-134a in the 1993-1996 time period. A significant investment, estimated by the Mobile Air Conditioning Society at U.S. $5 billion [Vogelsburg, 1996] ($3.5 billion by OEMs and $1.5 billion by the service industry) by the automobile and fluorochemical industries in the development and evaluation of compatible lubricants, construction materials, and fine tuning of compressor design and heat exchanger capacities was required to make this change so that traditional performance, reliability, durability and safety levels were maintained. This change was made with full knowledge that the global warming potential of the replacement (HFC-134a) was significantly lower than the original fluid being used (CFC-12) and that the replacement did not deplete stratospheric ozone. However, despite the lower GWP of HFC-134a, the use of either of two so-called natural refrigerants has been advocated by some to avoid the global warming impact of HFC-134a emissions. The two alternatives in question are: a vapor compression cycle using flammable refrigerants (propane or HFC-152a) or a transcritical vapor compression cycle using carbon dioxide. These alternatives are evaluated below.
In addition to the usual objectives of minimum weight and cost that drive the design of all automotive components, automobile air conditioning systems are designed, for a given vehicle, to meet cooling performance criteria that each vehicle manufacturer has established to represent competitive performance, meeting the expectations of their customers. In addition, systems are designed for suitability for assembly line installation into the vehicle, and for life (approximately 4,000 operating hours) and reliability consistent with the operating life of a passenger automobile.
A common automobile air conditioning system configuration has evolved to meet these requirements. Shown in Figure 5-1, the main features are:

Three alternative technologies to the HFC-134a vapor compression cycle will be evaluated here:

In comparing the HFC-134a based vapor compression cycle with the alternatives, it is important to remember that the HFC-134a system is characterized on the basis of the fully developed, mass produced system that is installed in approximately 45 million automobiles annually, and meets the diverse range of competitive cost, performance, reliability, durability, and safety requirements outlined previously. The current HFC-134a based system is an evolutionary adaptation of its CFC-12 based predecessor, whose design evolved over a period of 50 years. Despite the evolutionary nature of the adaptation from CFC-12 to HFC-134a, an enormous resource expenditure was required to resolve material compatibility and performance issues and to ensure that traditional consumer expectations for cooling performance and reliability would be met. The two alternatives, CO2 and hydrocarbon/secondary loop, have been prototyped and some performance test results are available to provide a basis for energy and LCCP analysis, but these designs would require substantial additional development to fully address the cost, performance, reliability, and safety requirements of the automobile customer. Therefore, the impact on the cost of an automobile to a consumer cannot be accurately assessed for either of these alternatives,
beyond general expectations. First, to bring CO2 based systems to production would require an enormous investment in new manufacturing equipment and facilities, simultaneously making obsolete the existing manufacturing base built up over the past decade, let alone the cost to the service industry. Second, it is reasonable to anticipate that the significantly higher operating pressures typical of CO2 transcritical AC systems will increase hardware cost, as well. HC based systems will require additional hardware to address safety concerns, also increasing the cost. An HFC-152a/secondary loop system provides a low GWP refrigerant alternative that can utilize the existing HFC-134a production base. A transition to either CO2 or flammable refrigerants would require substantial transition costs for service infrastructure and training.
A detailed comparison of energy use of HFC-134a and the two alternative systems is cited below from the TEWI-3 study and the recently published GMR/ORNL studies. Prior to this, a simple, theoretical comparison of vapor compression cycle COPs is presented to help provide some perspective on the detailed results. Assuming the following, typical operating conditions:
Tables 5-1 and 5-2 summarize the cycle COP calculations for mild and severe ambient conditions, respectively. Thermodynamic property data was taken from ASHRAE thermodynamic property tables.
|
Parameter (Enthalpy in Btu/lb) |
Values for |
|||||
| HFC-134 | Propane | HFC-152a | Transcritical CO2 | |||
| Refrigeration Effect: | ||||||
| Enthalpy of saturated vapor leaving the evaporator | 107 | 199 | 152 | 137 | ||
| Enthalpy of refrigerant entering and leaving the expansion device | 43 | 80 | 46 | 59* | ||
| Net refrigeration effect | 64 | 119 | 106 | 78 | ||
| Compressor Power: | ||||||
| Enthalpy of vapor entering compressor | 112 | 210 | 158 | 153* | ||
| Enthalpy of vapor leaving compressor (70% isentropic efficiency) | 129 | 249 | 192 | 186 | ||
| Compressor work | 17 | 39 | 34 | 37 | ||
| COP = Refrigeration effect/compressor work | 3.76 | 3.05 | 3.11 | 2.11 | ||
|
Parameter (Enthalpy in Btu/lb) |
Values for |
|||||
| HFC-134 | Propane | HFC-152a | Transcritical CO2 | |||
| Refrigeration Effect: | ||||||
| Enthalpy of saturated vapor leaving the evaporator | 107 | 199 | 152 | 137 | ||
| Enthalpy of refrigerant entering and leaving the expansion device | 51 | 94 | 55 | 61* | ||
| Net refrigeration effect | 56 | 105 | 97 | 76 | ||
| Compressor Power: | ||||||
| Enthalpy of vapor entering compressor | 112 | 210 | 158 | 158* | ||
| Enthalpy of vapor leaving compressor (70% isentropic efficiency) | 133.5 | 257 | 201 | 204 | ||
| Compressor work | 21.5 | 47 | 43 | 50 | ||
| COP = Refrigeration effect/compressor work | 2.60 | 2.23 | 2.26 | 1.52 | ||
A higher COP corresponds to higher-energy efficiency, as it indicates that more cooling capacity is provided for the mechanical power input expended. At both mild and severe ambient conditions, the HFC-134a vapor compression system has the highest theoretical COP, exceeding that of propane or HFC-152a (with secondary coolant loop) by 15 to 20% and of transcritical CO2 by more than 70%. The COP decrement of the propane cycle compared to HFC-134a is primarily caused by the lower evaporator temperature needed to accommodate the secondary coolant loop. The large difference in thermodynamic cycle COP between the transcritical CO2 cycle and the R134a cycle is inherent in a transcritical cycle operating with heat rejection above the two-phase dome and with the evaporator operating within, but near the top of the dome, where the latent heat is small in comparison to the compression work. Note that an interchanger would improve the COP of an HFC-134a or HFC-152a or a hydrocarbon vapor cycle and that an interchanger adds to the manufacturing cost. In a real system, of course, other factors affect the energy consumption. A major factor is the transport properties of the refrigerant, which have a strong influence on the evaporating and condensing (or super-critical cooling) heat transfer coefficients. In a mobile air conditioning application, engine fuel consumption is attributable to both the compressor power consumption and to the portion of the traction power to move the weight of the air conditioning system, whether it is operating or not. A detailed analysis is beyond the scope of this study, but results of other studies are discussed briefly below.
The TEWI-3 study took the following into account:
Recent work on flammable refrigerant (propane or HFC-152a)/secondary loop systems [Ghodbane, 1999], [Ghodbane,2000] indicates that the energy penalty for the secondary loop are considerably less than those estimated by the TEWI-3 study. In the TEWI-3 results, flammable/secondary energy use was 45% higher than the baseline HFC-134a system. Ghodbane's results, which are based on a combination of experimental results and validated simulations, show that the average penalty for air conditioning system energy over a range of driving conditions is 15%, plus a 10-15% penalty for transporting the added weight of the secondary loop. The TEWI-3 results have been adjusted accordingly, assuming an air conditioning system energy penalty of 15% and an added weight penalty of 12% (compared to the baseline HFC-134a system).
The estimated energy consumption from TEWI-3, with hydrocarbon/secondary loop adjusted as discussed in the preceding paragraph, is summarized in Table 5-3, based on backing it out from the indirect TEWI contribution.
| Region | Refrigerant | |||
| Baseline HFC-134a |
Secondary Loop Hydrocarbon* |
CO2 | ||
| A | B | |||
| Europe A/C Energy Weight Total Energy |
541 106 647 |
622 119 741 |
667 143 810 |
883 143 1026 |
| Japan A/C Energy Weight Total Energy |
419 66 485 |
482 74 556 |
494 89 583 |
730 89 819 |
| North America A/C Energy Weight Total Energy |
1245 156 1401 |
1432 175 1607 |
1620 212 1832 |
2113 212 2325 |
Both the TEWI and LCCP are intended to account for the warming impact of a product or a process over the complete lifetime of the product --- from production of the raw materials and manufacturing through usage through end of life disposal. Early TEWI analyses typically included the direct global warming impact of fluorochemical emissions, but neglected the warming impact of the embodied energy and fugitive emissions associated with manufacturing the fluorochemicals. Embodied energy and fugitive emissions are included in the LCCP calculations. In principle, the embodied energy in the materials and processes used to produce the automobile air conditioning system components should be included in the LCCP calculations. It has been neglected in this analysis, because the magnitude is quite small and almost all materials used to construct the air conditioning system (primarily aluminum alloys) are recycled when a vehicle is scrapped.
The direct GWP of refrigerant emission is a significant part of the LCCP of HFC-134a emissions, so the assumed emissions over the vehicle lifetime is important. Table 5-4 summarizes three emissions scenarios that were used in the TEWI-3 study. The assumed 1 kg refrigerant charge corresponds to current practice for larger passenger cars. Actual charges range from about 0.5 kg for small cars to more than 1 kg for large vans and SUVs
| Refrigerant Requirement | "As Manufactured" | 1 Service Additions | 2 Service Additions |
| Original Equipment Charge | 1000 g | 1000 g | 1000 g |
| Service Additions | 0 g | 400 g | 800 g |
| Total Refrigerant Usage | 1000 g | 1400 g | 1800 g |
| End-of-Life Charge | 650 g | 600 g | 800 g |
| End-of-Life Refrigerant Recovery | 585 g | 540 g | 720 g |
| New Lifetime Refrigerant Usage: Emissions (Total Usage - Recovery) | 415 g | 860 g | 1080 g |
In June, 1998, the world's major automobile manufacturers held a workshop in Phoenix, Arizona [Baker, 1998]. They developed a consensus estimate of lifetime HFC-134a emissions. For current vehicles, estimated lifetime usage is 1.26 system charges; for future vehicles, estimated lifetime usage is 0.71 charges. The former figure is somewhat higher than range of scenarios used in the TEWI-3 study; the latter falls within the range of scenarios.
The results of the first experimental study of HFC-134a leakage from mobile air conditioning systems were reported recently [Siegel, 2002]. Leakage rates were experimentally measured from a sample of 28 cars and light trucks. Vehicles from 5 manufacturers were tested, vehicle mileage ranged from 0 to 151,000 miles. Leakage rates were measured in a Sealed Housing for Evaporative Determination (SHED) apparatus, with the vehicles not operating. With an adjustment to account for vehicle and air conditioner operating time, the average leakage rate was found to be 0.08 gram/day, or 29 gram/year. The study cites the work cited in the preceding paragraph [Baker, 1998], which found that losses of HFC-134a due to servicing and end of life disposal average 0.12 grams/day when recovery and recycling are practiced or 0.53 gram/day when the refrigerant is (illegally in the U.S.) vented. When the no-vent regulations are followed, the total lifeitme loss of HFC-134a averages 0.08 + 0.12 = 0.20 gram/day, or 730 grams over a 10 year vehicle life, within the ranges addressed in the TEWI-3 study.
Table 5-5 is based on Table 17 from the TEWI-3 study, where the Climate Change 95 GWP value for R134a was used. The LCCP values were derived by updating the TEWI values to include embedded energy and the pro-rata GWP of fugitive emissions from the production of HFC-134a (effective GWP of HFC-134a is increased from 1300 to 1313). The numbers for the direct effect of HFC-134a in Table 5-5 represent the range from as manufactured up to two service additions, as contained in Table 5-4, bottom row. The energy related contributions to the LCCP of the hydrocarbon/secondary loop system have been adjusted to reflect more recent data, as discussed in 5.2.2.
| Region | Refrigerant | |||
| Baseline HFC-134a |
Secondary Loop Hydrocarbon* |
CO2 | ||
| A | B | |||
| Europe A/C Energy Weight Direct Effect LCCP |
1255 245 545 to 1418** 2045 to 2918 |
1443 275 4 1722 |
1547 331 1 1878 |
2048 331 1 2380 |
| Japan A/C Energy Weight Direct Effect LCCP |
972 154 512 to 993** 1638 to 2119 |
1118 173 3 1294 |
1147 208 0.7 1356 |
1694 208 0.7 1903 |
| North America A/C Energy Weight Direct Effect LCCP |
2889 363 545 to 1418** 3797 to 4670 |
3322 407 4 3733 |
3759 491 1 4240 |
4902 491 1 5393 |
In general, the lower energy use of HFC-134a based systems more than offsets the direct effect of projected HFC-134a emissions. Overall, the LCCP results do not provide a compelling basis to favor one working fluid over the others, based on the conditions and assumptions made. However, when other considerations, such as cost and safety are taken into account, HFC-134a systems demonstrate clear advantages. In addition, HFC-134a systems also have potential for further improvement from an LCCP viewpoint.
General Motors Research and the Oak Ridge National Lab collaborated on an in-depth update of the TEWI-3 study analysis for mobile air conditioning. The results were presented at an SAE meeting on June 28th, 1999. As was the case in the TEWI-3 study, the impact of climate and driving cycles was taken into account. To include the effect of climate and regional differences in driving patterns, six cities were selected --- Phoenix, Miami, Boston, Tokyo, Frankfurt, and Sydney. For each of these cities, hourly weather data was used to generate an annual distribution of temperatures and relative humidity levels. Local driving patterns were taken into account through the use of local fuel economy test cycles, e.g. the Federal Urban Driving Schedule in the U.S. Wind tunnel test data were used to relate condenser performance and CO2 gas cooler performance to the driving cycle. The study attempts to more realistically model real world air conditioners, including the effect of recirculating hot air from the engine compartment through the condenser at idling conditions, based on wind tunnel data.
The primary focus of the GMR/ORNL study is comparing conventional HFC-134a based systems with transcritical CO2 systeMs. The warming impact of HFC-134a emissions are a significant contributor to the TEWI. A range of HFC-134a emission scenarios (E1, E2, E3, and E4) were defined, corresponding to lifetime service additions of approximately 150, 300, 450, and 600 grams, respectively. TEWI values were calculated for CO2 and HFC-134a systems, for small and mid-sized cars, in each of the six aforementioned cities. The impact on the TEWI of different emission rates and different levels of cooling air reentrainment at idling conditions was calculated, along with the impact of transporting the weight of the air conditioning system. Figure 5-3, which was reproduced from the paper, summarizes these results for a mid-size car ( the results for the small car are similar).
The TEWI/LCCP results in Figure 5-3 are generally consistent with the TEWI-3 results, and show that for North America, where relatively more miles are driven annually in a warmer climate, the energy savings of an HFC-134a based system compared to CO2 and the associated reduced indirect warming more than offset the direct warming of refrigerant emissions, making HFC-134a the best LCCP alternative. In Northern Europe, where the climate is milder and fewer kilometers are driven annually, the LCCP for CO2 is less than the LCCP for HFC-134a, although this relationship would likely reverse in a warmer climate.

Subsequent to the publication of the ORNL/GMR study, additional analysis was undertaken by GMr. Three sets of TEWI charts were produced for 3 cases:
The latter option is technically feasible and may be a more cost-effective, lighter-weight way to achieve low LCCP in a mild climate.



Unlike other common uses of fluorocarbons, automobile air conditioning systems are mounted on a platform that is repeatedly exposed to the risk of road collision damage.
Of the four refrigerants being addressed for mobile air conditioning --- HFC-134a, hydrocarbon HC-290, HFC-152a, and carbon dioxide --- none have high toxicity concerns. However, HC-290 (propane) is highly flammable, HFC-152a is flammable, and carbon dioxide operates at significantly higher pressures (CO2 high-side pressures are approximately 5 times higher than HFC-134a and CO2 low-side pressures are 10 times higher than HFC-134a). The question of safely containing CO2 pressures during operation, repair/maintenance, collision, and disposal at the end of life requires accurate definition of specific criteria. CO2 is acutely toxic only in high concentrations, a potential concern if the evaporator were to rupture suddenly. The acute effects of CO2 must be considered not only for healthy adults, but for children, elderly individuals, and individuals whose health is impaired. It is known that a rupture in the engine compartment can cause sheet metal to crumple.
In view of the greater risk for collisions of motor vehicles (than for stationary equipment) that could result in damage to the areas of the vehicle where air conditioning system components and tubing are installed, the question of fire safety when using a hydrocarbon refrigerant requires careful examination.
In the cradle-to-grave lifecycle of an automobile having a hydrocarbon refrigerant in the air conditioning system, there are several distinct events where fire safety issues must be considered:
As illustrated in Figure 5-1, in a typical automobile air conditioning system, interior cooling is provided by a direct expansion evaporator located in the climate control ductwork, within the passenger compartment. An alternative arrangement for a hydrocarbon refrigerant, illustrated in Figure 5-2, locates the chiller evaporator in the engine compartment. The evaporator cools a secondary coolant which is circulated to an air cooling heat exchanger located in the climate control ductwork where the evaporator normally would be located. This arrangement keeps the flammable refrigerant outside the passenger compartment. The arrangement of the compressor, condenser, and interconnecting refrigerant hoses and lines is similar for both configurations.
A large scale program to evaluate the fire safety of a conventional configuration air conditioning system with hydrocarbon refrigerant, or to redesign mobile a/c systems to use a hydrocarbon refrigerant with an acceptable level of fire safety has never been carried out, either within the automobile industry or under public sector sponsorship. Such a program would include fault-tree risk analysis, component testing, and collision testing and redesign and development effort as well, if the objective were to design a fire-safe flammable refrigerant based system. Some preliminary studies and tests have been undertaken.
In 1991, Dieckmann and Bentley did a preliminary fire risk analysis, using a flammable refrigerant in a conventional a/c system configuration. The study was focussed on the fire risk associated with collision, not the other phases of the product life cycle. The preliminary conclusion of the study was that fire risks could prove to be acceptably low. The specific points relative to fire risk in the report conclusions noted the major uncertainties involved, as did the detailed treatment in the report:
Considerably more work would be needed to develop reasonably definitive estimates of passenger compartment and engine compartment fire risks and injury risks. This work would involve a combination of field data collection, characterization of potential ignition sources (both in the passenger compartment and in the engine compartment), and collision testing. Again, the report did not address refrigerant retrofit directly; in view of the level of front end collision damage related refrigerant system rupture in the engine compartment that was observed in the limited field survey work that was undertaken in the study, and the absence of hard data on ignition sources and ignition probabilities, the study did not provide a firm basis to conclude that the resulting occurrence of engine compartment fires would be acceptably low.
Interestingly, the preliminary results indicated that the primary fire issue with a hydrocarbon refrigerant may be collision-related fires originating in the engine compartment, rather than the passenger compartment. In the limited field sample (10 cars, a sample far to small to be the basis of a firm conclusion) of cars that had suffered severe (intrusion in excess of 12 inches) "A" pillar area passenger side impacts, the evaporators and refrigerant lines had not been punctured at all. In several instances, the evaporator had been displaced from its original position by close to 12 inches.
On the other hand, front-end collisions beyond minor "fender-benders", resulted in a high percentage of refrigerant line ruptures. In the collision damaged cars examined in the limited field study, the hood latch often was driven into the upper rows of the condenser tubing, puncturing one or more tubes. Some relatively simple design charges could potentially reduce the susceptibility of AC system components to front-end collision damage, but no development program to this end has been pursued to date. It must be emphasized that confining flammable refrigerant releases and potential ignitions to the engine compartment does not, by itself, satisfy the fire safety issue (the inherent assumption behind configuring an HC system with a secondary coolant loop to the passenger compartment). Beyond the obvious increase in property loss, a hydrocarbon refrigerant fire in the engine compartment can spread rapidly, igniting plastic materials, the fuel, and in fairly short order can place at grave risk a passenger who is trapped by collision damage or unable to move due to injury.
Engine compartment ignition probabilities can be reduced by a battery/alternator disconnect switch which is activated by the air bag sensor. This switch is currently under development and may be widely implemented in the foreseeable future. The effect of immediately disconnecting the battery in a front end collision is to greatly reduce, if not eliminate, the electrical system as a potential ignition source.
For a variety of reasons (in the U.S., product liability risk is one significant reason), the automobile industry has not invested the extensive effort and resources that would need to be invested to address the technical and societal issues outlined above.
The potential safety issues associated with high pressure CO2 systems have not been studied in depth. Two issues have been identified:
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