CFC Chlorofluorocarbons
Overview
Chlorofluorocarbons (CFCs) are fully halogenated hydrocarbons containing only carbon, chlorine, and fluorine atoms. These synthetic compounds revolutionized refrigeration and air conditioning from the 1930s through the 1980s due to their excellent thermodynamic properties, chemical stability, and non-toxic nature. However, their atmospheric persistence and severe ozone depletion potential led to their global phaseout under the Montreal Protocol.
CFCs represent the first generation of synthetic refrigerants that replaced hazardous substances like ammonia, sulfur dioxide, and methyl chloride in mainstream applications. Their development by Thomas Midgley Jr. at General Motors in 1928 marked a paradigm shift in refrigeration safety and reliability.
Molecular Structure and Nomenclature
Chemical Composition
CFCs are saturated aliphatic compounds where all hydrogen atoms have been replaced by chlorine or fluorine atoms. The general chemical formula is:
CClₓFᵧ (for single-carbon compounds) C₂ClₓFᵧ (for two-carbon compounds)
Where x + y equals the total number of bonds available on the carbon skeleton.
Refrigerant Numbering System
The ASHRAE refrigerant numbering system for CFCs follows this format:
R-ABC
Where:
- A = Number of carbon atoms minus 1 (omitted if zero)
- B = Number of hydrogen atoms plus 1
- C = Number of fluorine atoms
The number of chlorine atoms is determined by difference after accounting for carbon valence.
Example: R-12 (CCl₂F₂)
- A = 0 (one carbon, 0 is omitted)
- B = 1 (zero hydrogens + 1 = 1)
- C = 2 (two fluorine atoms)
- Chlorine atoms = 4 - 2 = 2
Common CFC Refrigerants
R-11 (CCl₃F) - Trichlorofluoromethane
Molecular Properties:
| Property | Value | Units |
|---|---|---|
| Molecular weight | 137.37 | g/mol |
| Boiling point (1 atm) | 23.8 | °C |
| Critical temperature | 198.0 | °C |
| Critical pressure | 4.408 | MPa |
| Ozone depletion potential | 1.0 | reference |
| Global warming potential (100-yr) | 4,660 | CO₂ equiv |
| Atmospheric lifetime | 45 | years |
Thermodynamic Characteristics:
- Low pressure refrigerant (operates below atmospheric at typical evaporator conditions)
- Excellent for large centrifugal chillers
- High molecular weight provides good compressor efficiency
- Low latent heat requires large mass flow rates
Historical Applications:
- Large centrifugal water chillers (100-10,000 tons)
- Low-temperature industrial refrigeration
- Foam blowing agent
- Aerosol propellant
Operating Considerations:
- Evaporator operates in vacuum at standard air conditioning temperatures
- Air and moisture ingress major concern
- Requires purge systems for non-condensables
- Oil return challenges due to low refrigerant velocities
R-12 (CCl₂F₂) - Dichlorodifluoromethane
Molecular Properties:
| Property | Value | Units |
|---|---|---|
| Molecular weight | 120.91 | g/mol |
| Boiling point (1 atm) | -29.8 | °C |
| Critical temperature | 112.0 | °C |
| Critical pressure | 4.136 | MPa |
| Ozone depletion potential | 1.0 | reference |
| Global warming potential (100-yr) | 10,200 | CO₂ equiv |
| Atmospheric lifetime | 100 | years |
Thermodynamic Characteristics:
- Medium pressure refrigerant
- Excellent volumetric efficiency
- Good coefficient of performance
- Favorable pressure-temperature relationship
- Compatible with mineral oils
Historical Applications:
- Domestic refrigerators and freezers
- Automotive air conditioning
- Medium-sized commercial refrigeration
- Reciprocating and scroll compressors
- Transport refrigeration
- Industrial process cooling
Saturation Properties (Selected Points):
| Temperature (°C) | Pressure (kPa) | Liquid Density (kg/m³) | Vapor Density (kg/m³) | Latent Heat (kJ/kg) |
|---|---|---|---|---|
| -40 | 64.7 | 1,546 | 3.98 | 165.1 |
| -20 | 151.1 | 1,488 | 8.86 | 160.3 |
| 0 | 309.1 | 1,426 | 17.42 | 154.6 |
| 20 | 567.5 | 1,357 | 31.49 | 147.5 |
| 40 | 961.8 | 1,279 | 54.18 | 138.2 |
R-12 was the most widely used CFC refrigerant, considered the industry standard for decades. Its balanced properties made it suitable for a vast range of applications.
R-113 (CCl₂FCClF₂) - 1,1,2-Trichloro-1,2,2-trifluoroethane
Molecular Properties:
| Property | Value | Units |
|---|---|---|
| Molecular weight | 187.38 | g/mol |
| Boiling point (1 atm) | 47.6 | °C |
| Critical temperature | 214.1 | °C |
| Critical pressure | 3.392 | MPa |
| Ozone depletion potential | 0.8 | reference |
| Global warming potential (100-yr) | 6,130 | CO₂ equiv |
| Atmospheric lifetime | 85 | years |
Historical Applications:
- Very large centrifugal chillers
- Industrial solvent
- Electronics cleaning
- Precision cleaning applications
- Aerospace applications
Operating Characteristics:
- Very low pressure operation (below atmospheric)
- Highest molecular weight of common CFCs
- Excellent for very large capacity systems
- Superior chemical stability
- Non-flammable solvent properties
R-114 (CClF₂CClF₂) - 1,2-Dichloro-1,1,2,2-tetrafluoroethane
Molecular Properties:
| Property | Value | Units |
|---|---|---|
| Molecular weight | 170.92 | g/mol |
| Boiling point (1 atm) | 3.6 | °C |
| Critical temperature | 145.7 | °C |
| Critical pressure | 3.257 | MPa |
| Ozone depletion potential | 1.0 | reference |
| Global warming potential (100-yr) | 9,800 | CO₂ equiv |
| Atmospheric lifetime | 300 | years |
Historical Applications:
- Military and naval refrigeration systems
- Heat pumps
- Medium-temperature applications
- Centrifugal chillers
- Specialized industrial processes
Unique Characteristics:
- Long atmospheric lifetime (300 years)
- Exceptionally stable molecule
- Low toxicity
- Good thermal stability at high temperatures
- Used in binary refrigerant blends
R-115 (CClF₂CF₃) - Chloropentafluoroethane
Molecular Properties:
| Property | Value | Units |
|---|---|---|
| Molecular weight | 154.47 | g/mol |
| Boiling point (1 atm) | -38.7 | °C |
| Critical temperature | 80.0 | °C |
| Critical pressure | 3.129 | MPa |
| Ozone depletion potential | 0.6 | reference |
| Global warming potential (100-yr) | 7,370 | CO₂ equiv |
| Atmospheric lifetime | 1,020 | years |
Historical Applications:
- Low-temperature refrigeration
- Cascade systems (low stage)
- Cryogenic applications
- Component in azeotropic blends (R-502)
- Ultra-low temperature freezers
Operating Characteristics:
- Suitable for temperatures below -40°C
- High pressure operation
- Component of R-502 (48.8% R-115 / 51.2% R-22)
- Extremely long atmospheric persistence
- Limited standalone use
Thermodynamic Performance Analysis
Vapor Compression Cycle with R-12
For a standard vapor compression cycle operating between evaporator and condenser temperatures:
Given Conditions:
- Evaporator temperature: 0°C (273.15 K)
- Condenser temperature: 40°C (313.15 K)
- Subcooling: 5 K
- Superheat: 10 K
State Points:
| State | Description | Pressure (kPa) | Temperature (°C) | Enthalpy (kJ/kg) | Entropy (kJ/kg·K) |
|---|---|---|---|---|---|
| 1 | Compressor inlet | 309.1 | 10 | 188.6 | 0.7085 |
| 2 | Compressor discharge | 961.8 | 65 | 218.4 | 0.7085 |
| 3 | Condenser exit | 961.8 | 35 | 64.6 | 0.2451 |
| 4 | Evaporator inlet | 309.1 | -29.8 | 64.6 | 0.2517 |
Performance Metrics:
- Refrigeration effect: qₑ = h₁ - h₄ = 188.6 - 64.6 = 124.0 kJ/kg
- Compressor work: wc = h₂ - h₁ = 218.4 - 188.6 = 29.8 kJ/kg
- COP = qₑ / wc = 124.0 / 29.8 = 4.16
- Carnot COP = Tₑ / (Tc - Tₑ) = 273.15 / 40 = 6.83
- Efficiency ratio = 4.16 / 6.83 = 60.9%
Comparative Performance
CFC Refrigerants Performance Comparison (Standard Rating Conditions):
| Refrigerant | Evaporator Pressure (kPa) | Compression Ratio | Discharge Temp (°C) | COP | Volumetric Capacity (kJ/m³) |
|---|---|---|---|---|---|
| R-11 | 36.2 | 7.9 | 85 | 5.2 | 1,850 |
| R-12 | 183.0 | 3.8 | 52 | 4.4 | 2,150 |
| R-113 | 18.4 | 10.2 | 92 | 5.4 | 1,420 |
| R-114 | 81.5 | 4.5 | 58 | 4.6 | 1,680 |
| R-115 | 528.0 | 2.9 | 45 | 3.8 | 1,920 |
Note: Rating conditions - Evaporator: -15°C, Condenser: 30°C, 5K subcooling, 10K superheat
Ozone Depletion Mechanism
Stratospheric Chemistry
CFCs are chemically inert in the troposphere due to the absence of hydrogen atoms and strong C-F and C-Cl bonds. This stability allows them to migrate to the stratosphere (15-50 km altitude) where ultraviolet radiation breaks the C-Cl bonds:
Step 1: Photodissociation
CCl₂F₂ + hν (UV) → CClF₂• + Cl•
The photolysis occurs at wavelengths below 220 nm, abundant in the stratosphere but filtered by ozone in the troposphere.
Step 2: Catalytic Ozone Destruction
Cl• + O₃ → ClO• + O₂ ClO• + O → Cl• + O₂ Net: O₃ + O → 2O₂
A single chlorine atom can destroy 100,000 ozone molecules through this catalytic cycle before being deactivated.
Step 3: Chlorine Reservoir Formation
Cl• + CH₄ → HCl + CH₃• ClO• + NO₂ → ClONO₂
These reservoir species temporarily sequester chlorine but can be reactivated.
Ozone Depletion Potential (ODP)
ODP quantifies the relative ability of a substance to destroy stratospheric ozone compared to R-11 (defined as 1.0).
Factors Affecting ODP:
- Number of chlorine atoms per molecule
- Atmospheric lifetime
- Molecular weight (affects transport to stratosphere)
- Photodissociation rate in stratosphere
CFC ODP Values:
| Refrigerant | Chemical Formula | Cl Atoms | ODP |
|---|---|---|---|
| R-11 | CCl₃F | 3 | 1.0 |
| R-12 | CCl₂F₂ | 2 | 1.0 |
| R-113 | CCl₂FCClF₂ | 3 | 0.8 |
| R-114 | CClF₂CClF₂ | 2 | 1.0 |
| R-115 | CClF₂CF₃ | 1 | 0.6 |
The lower ODP of R-113 and R-115 results from reduced stratospheric chlorine yield, not fewer chlorine atoms.
Antarctic Ozone Hole
The most severe ozone depletion occurs over Antarctica during austral spring (September-November) due to unique atmospheric conditions:
- Polar Stratospheric Clouds (PSCs): Form at temperatures below -78°C, providing surfaces for heterogeneous reactions that convert reservoir species to reactive chlorine
- Polar Vortex: Isolates Antarctic air mass, preventing mixing with mid-latitude air
- Sunlight Return: Spring sunlight photolyzes chlorine compounds, triggering rapid ozone destruction
- Surface Chemistry: PSC particles enable: ClONO₂ + HCl → Cl₂ + HNO₃
CFC-derived chlorine levels in the stratosphere peaked around 2000 at approximately 3.6 ppbv (parts per billion by volume).
Montreal Protocol and Phaseout
International Framework
The Montreal Protocol on Substances that Deplete the Ozone Layer, signed in 1987, represents the most successful international environmental agreement. It mandated the phased elimination of CFC production and consumption.
Timeline for Developed Countries (Article 5.1 Non-Parties):
| Date | Regulation | Impact |
|---|---|---|
| July 1, 1989 | Freeze consumption at 1986 levels | Baseline established |
| July 1, 1993 | Reduce 75% from baseline | Major production cuts |
| January 1, 1994 | Reduce 100% from baseline | Production ban for most CFCs |
| January 1, 1996 | Complete phaseout | All CFC production prohibited |
Timeline for Developing Countries (Article 5 Parties):
| Date | Regulation | Impact |
|---|---|---|
| July 1, 1999 | Freeze consumption at 1995-1997 average | 10-year grace period |
| January 1, 2005 | Reduce 50% from baseline | Gradual reduction |
| January 1, 2007 | Reduce 85% from baseline | Accelerated under amendments |
| January 1, 2010 | Complete phaseout | Production ended |
Essential Use Exemptions
Limited CFC production continued post-phaseout for essential uses where no technically or economically feasible alternatives existed:
Approved Essential Uses:
- Metered dose inhalers (MDIs) for asthma medication
- Laboratory and analytical applications
- Critical defense applications
- Space vehicle applications
Medical MDI use of CFCs (primarily R-12 and R-114) continued until HFA (hydrofluoroalkane) propellants became available in the early 2000s.
Regulatory Framework in United States
Clean Air Act Section 608:
- Prohibits venting CFCs during service, maintenance, or disposal
- Mandates technician certification (Type I, II, III, Universal)
- Requires use of certified recovery/recycling equipment
- Establishes maximum penalties for violations ($37,500 per day per violation as of 2020)
EPA Regulations:
- 40 CFR Part 82 Subpart F: Recycling and emissions reduction
- 40 CFR Part 82 Subpart G: Significant New Alternatives Policy (SNAP)
- Recordkeeping requirements for refrigerant purchases and usage
Replacement Refrigerants and Conversion Strategies
Direct Replacement Options
R-11 Replacements:
| Alternative | Type | ODP | GWP | Status |
|---|---|---|---|---|
| R-123 | HCFC | 0.02 | 77 | Phasing out under Kigali Amendment |
| R-245fa | HFC | 0 | 950 | Being phased down |
| R-1233zd(E) | HFO | 0 | 1 | Preferred long-term solution |
R-12 Replacements:
| Alternative | Type | ODP | GWP | Status |
|---|---|---|---|---|
| R-134a | HFC | 0 | 1,430 | Phasing down under Kigali |
| R-401A, R-409A | HCFC blend | 0.03-0.04 | 1,200 | Interim solutions, phased out |
| R-1234yf | HFO | 0 | 4 | Automotive standard |
| R-513A | HFO blend | 0 | 631 | Commercial applications |
Retrofit Considerations
System Compatibility Assessment:
Lubricant Compatibility:
- CFCs used mineral oil or alkylbenzene
- HFC replacements require polyolester (POE) or polyalkylene glycol (PAG)
- Oil change typically necessary (minimum 95% conversion)
- Residual mineral oil affects miscibility and return
Material Compatibility:
- Elastomers: Different swelling characteristics
- Desiccants: XH-7 or XH-9 required for HFCs (replace XH-5)
- Expansion devices: May require resizing due to different pressure-temperature relationships
System Modifications:
| Component | R-12 to R-134a Conversion | Reason |
|---|---|---|
| Compressor oil | Replace with POE | Miscibility with HFC |
| Filter-drier | Replace with XH-7/XH-9 type | HFC compatibility |
| O-rings/gaskets | Inspect/replace | Different swelling |
| TXV | Recalibrate or replace | 10-15% higher capacity needed |
| Service ports | Replace with new fittings | Prevent cross-contamination |
| Labels | Update refrigerant identification | Code requirement |
Performance Expectations:
- R-134a in R-12 systems: 5-10% capacity reduction typical
- Energy efficiency: Generally comparable or slightly lower
- Discharge temperatures: 5-10°C higher with R-134a
- Operating pressures: R-134a operates at slightly higher pressures
Legacy Equipment Management
Servicing Existing CFC Systems
Refrigerant Supply Challenges:
- New CFC production prohibited since 1996 (developed countries)
- Reclaimed and recycled CFCs only legal source
- Prices increased 1000-2000% since phaseout
- Counterfeit refrigerants concern in some markets
Reclaimed Refrigerant Standards:
Per AHRI Standard 700-2016, reclaimed refrigerants must meet virgin product specifications:
| Parameter | R-11 | R-12 | Test Method |
|---|---|---|---|
| Purity (min %) | 99.9 | 99.9 | Gas chromatography |
| Moisture (max ppm) | 20 | 10 | Karl Fischer |
| Acidity (max ppm) | 1 | 1 | Acid titration |
| High boiling residue (max %) | 0.01 | 0.01 | Gravimetric |
| Particulates/solids | Visually clean | Visually clean | Visual inspection |
| Non-condensables (max vol %) | 1.5 | 1.5 | Pressure method |
Economic Analysis
Cost-Benefit of Retrofit vs. Continued Service:
Factors Favoring Retrofit/Replacement:
- CFC refrigerant costs exceeding $50-150/kg
- Frequent refrigerant additions (leak rate >10% annually)
- Equipment age >20 years
- High energy consumption (EER <8)
- Availability of utility incentives
- Upcoming major maintenance requirements
Factors Favoring Continued Service:
- Tight system with minimal leakage
- Recent major component replacements
- Adequate refrigerant inventory
- Specialized application with limited replacement options
- Short remaining service life (≤5 years)
Payback Calculation Example:
Retrofit 100-ton R-11 centrifugal chiller to R-123:
- Retrofit cost: $80,000
- Annual CFC cost avoided: $12,000
- Energy savings: $3,000/year
- Simple payback: 80,000 / 15,000 = 5.3 years
Decommissioning Procedures
EPA Requirements for Equipment Disposal:
Refrigerant Recovery:
- Recover to EPA-mandated levels before disposal
- High-pressure equipment: 0 psig (vacuum)
- Low-pressure equipment (R-11): 25 mmHg absolute
- Very high-pressure equipment: 0 psig
Documentation:
- Maintain records of refrigerant recovery
- Report to refrigerant tracking systems if required
- Document final disposition of equipment
Recovery Equipment Requirements:
- Must be certified to AHRI Standard 740
- Regular calibration and maintenance
- Separate equipment for different refrigerant classes
Environmental Impact and Atmospheric Recovery
Global Atmospheric Trends
Chlorine Loading:
- Peak stratospheric chlorine: ~3.6 ppbv (2000)
- Current levels: ~3.1 ppbv (2023)
- Pre-industrial baseline: ~0.6 ppbv
- Projected return to baseline: 2060-2070
CFC Concentrations in Atmosphere:
| Refrigerant | Peak Concentration (ppt) | Current Trend | Half-Life in Atmosphere |
|---|---|---|---|
| R-11 | 268 (1994) | Declining 1-2%/year | 45 years |
| R-12 | 535 (2002) | Declining 0.5-1%/year | 100 years |
| R-113 | 84 (2004) | Declining 1%/year | 85 years |
| R-114 | 17 (current) | Stable/declining | 300 years |
| R-115 | 8.5 (current) | Slowly increasing | 1,020 years |
Note: ppt = parts per trillion by volume
Ozone Layer Recovery
Montreal Protocol Success Indicators:
- Antarctic ozone hole stabilized in size (not growing)
- Mid-latitude ozone showing recovery (0.5-3% per decade)
- Stratospheric chlorine declining
- UV-B radiation increases halted
Projected Recovery Timeline:
- Arctic ozone: Return to 1980 baseline by 2030-2040
- Mid-latitudes: Return to 1980 baseline by 2040-2050
- Antarctic ozone hole: Return to 1980 baseline by 2060-2070
Without the Montreal Protocol, atmospheric models project:
- Stratospheric chlorine would have reached 17 ppbv by 2050
- Global ozone depletion of 50% by 2050
- Arctic ozone hole comparable to Antarctic hole
- UV radiation increases causing millions of additional skin cancer cases
Technical Specifications Summary
Physical Properties Comparison
| Property | R-11 | R-12 | R-113 | R-114 | R-115 | Units |
|---|---|---|---|---|---|---|
| Molecular weight | 137.37 | 120.91 | 187.38 | 170.92 | 154.47 | g/mol |
| Boiling point | 23.8 | -29.8 | 47.6 | 3.6 | -38.7 | °C |
| Freezing point | -111 | -158 | -35 | -94 | -106 | °C |
| Critical temperature | 198.0 | 112.0 | 214.1 | 145.7 | 80.0 | °C |
| Critical pressure | 4.408 | 4.136 | 3.392 | 3.257 | 3.129 | MPa |
| Liquid density (25°C) | 1,467 | 1,311 | 1,565 | 1,456 | 1,291 | kg/m³ |
| Vapor thermal conductivity (25°C) | 8.3 | 9.8 | 7.5 | 11.2 | 12.4 | mW/(m·K) |
| Liquid viscosity (25°C) | 0.420 | 0.250 | 0.680 | 0.390 | 0.220 | mPa·s |
| Surface tension (25°C) | 16.8 | 8.5 | 15.2 | 11.8 | 6.3 | mN/m |
Safety Classification
Per ASHRAE Standard 34, all CFCs are classified as A1:
- A: Lower toxicity (permissible exposure limit ≥400 ppm)
- 1: No flame propagation at 60°C, 101.3 kPa
Occupational Exposure Limits:
| Refrigerant | OSHA PEL | ACGIH TLV | AIHA WEEL | Units |
|---|---|---|---|---|
| R-11 | 1,000 | 1,000 | 1,000 | ppm (8-hr TWA) |
| R-12 | 1,000 | 1,000 | 1,000 | ppm (8-hr TWA) |
| R-113 | 1,000 | 1,000 | 1,000 | ppm (8-hr TWA) |
| R-114 | 1,000 | 1,000 | 1,000 | ppm (8-hr TWA) |
| R-115 | Not established | Not established | 1,000 | ppm (8-hr TWA) |
Cardiac Sensitization: CFCs can sensitize the heart to epinephrine, potentially causing cardiac arrhythmia at high concentrations (>10,000 ppm). This effect limits occupational exposures during maintenance activities in confined spaces.
Historical Significance
Industry Impact
CFCs enabled the widespread adoption of refrigeration and air conditioning technology from the 1930s through 1980s:
Key Milestones:
- 1928: Thomas Midgley Jr. synthesizes dichlorodifluoromethane (R-12)
- 1930: DuPont commercializes CFCs under trade name “Freon”
- 1935: R-11 introduced for centrifugal chillers
- 1940s-1950s: CFCs replace ammonia and SO₂ in most applications
- 1960s: Explosive growth in residential and automotive air conditioning
- 1974: Molina-Rowland hypothesis on ozone depletion published
- 1987: Montreal Protocol signed
- 1996: CFC production banned in developed countries
Market Dominance: At peak usage (early 1980s):
- R-12: ~500,000 metric tons/year global production
- R-11: ~300,000 metric tons/year global production
- Combined CFC production: ~1.1 million metric tons/year
Lessons Learned
The CFC experience provides critical lessons for refrigerant selection:
- Long-term environmental assessment: Atmospheric lifetime and environmental impact must be evaluated before widespread adoption
- Chemical stability trade-off: Compounds that are chemically stable in systems may persist in the environment
- Global cooperation: International agreements can successfully address global environmental threats
- Transition planning: Adequate transition periods and alternatives are essential for successful phaseout
- Continuous improvement: Each generation of refrigerants addresses previous issues while introducing new considerations
Current Status and Future Outlook
Remaining Applications
Legitimate CFC use in 2024 is limited to:
- Servicing existing equipment (using reclaimed refrigerants only)
- Essential use exemptions (laboratory, analytical standards)
- Feedstock use (chemical synthesis where CFCs are destroyed)
Global Reclaimed Refrigerant Market:
- Annual reclaimed CFC supply: ~5,000-10,000 metric tons
- Primary sources: Equipment decommissioning, recovered refrigerants
- Quality concerns necessitate AHRI 700 certification
- Prices: $30-150/kg depending on refrigerant type and purity
Enforcement and Illegal Trade
Enforcement Challenges:
- Continued illegal CFC production detected in East Asia (2018-2019)
- Counterfeit refrigerant cylinders
- Cross-border smuggling to avoid phaseout compliance
- Mislabeled refrigerants
Detection Methods:
- Atmospheric monitoring networks
- Cylinder sampling and analysis
- Isotopic fingerprinting
- Import/export tracking systems
Environmental Legacy
While CFC emissions have largely ceased, their environmental impact continues:
- R-115 concentrations still slowly increasing due to 1,020-year lifetime
- Stratospheric chlorine will remain elevated for decades
- Antarctic ozone hole will persist until at least 2060
- Climate impact continues (high GWP values)
Total Climate Impact: CFCs contribute approximately 12% of historical radiative forcing from long-lived greenhouse gases, despite representing a small fraction of emissions by mass.
References and Standards
Key Standards:
- ASHRAE Standard 34: Designation and Safety Classification of Refrigerants
- AHRI Standard 700: Specifications for Refrigerants
- ASHRAE Standard 15: Safety Standard for Refrigeration Systems
- ISO 817: Refrigerants - Designation and Safety Classification
Regulatory Documents:
- Montreal Protocol on Substances that Deplete the Ozone Layer
- Clean Air Act Section 608 (40 CFR Part 82)
- EPA Significant New Alternatives Policy (SNAP) Program
- UNEP Ozone Secretariat Technical Reports
Scientific Assessment:
- WMO/UNEP Scientific Assessment of Ozone Depletion (published every 4 years)
- IPCC Climate Change Reports
- ASHRAE Handbook - Fundamentals (Chapter on Refrigerants)