8.2 Type II Recovery and Evacuation Procedures
Key Takeaways
- High-pressure systems: evacuate to 0 psig (10" Hg vacuum) before opening
- Recovery sequence: liquid recovery first (fast), then vapor recovery (remaining charge)
- Push-pull method: liquid displacement for fast recovery on large commercial systems
- Oil changes require pressure reduction to 5 psig or below
- Zeotropic blends must be liquid-charged; use a flow restrictor when charging through suction side
8.2 Type II Recovery and Evacuation Procedures
Type II recovery and evacuation requirements are more detailed than Type I because high-pressure systems range from small residential units to large commercial installations with hundreds of pounds of refrigerant.
Evacuation Requirements for High-Pressure Systems
| System Type | Charge Size | Required Evacuation (Post-11/15/1993 Equipment) |
|---|---|---|
| Very high-pressure | Any | 0 psig |
| High-pressure | Less than 200 lbs | 0 psig (10 inches Hg vacuum) |
| High-pressure | 200 lbs or more | 0 psig (10 inches Hg vacuum) |
Before Opening for Service
Before opening a high-pressure or very high-pressure system for service (not just connecting gauges):
- Recover refrigerant to the required evacuation level
- For high/very high-pressure appliances: evacuate to 0 psig or below
- Never open a system while it is under positive pressure (above 0 psig) — this would vent refrigerant
Recovery Procedure for Type II Systems
Step-by-step recovery procedure:
- Identify the refrigerant — verify type from equipment nameplate or use a refrigerant identifier
- Select appropriate recovery equipment — ensure it is rated for the refrigerant type and pressure
- Connect recovery equipment — attach hoses to service ports (suction and/or liquid service valves)
- Prepare the recovery cylinder — ensure it has capacity, is rated for the refrigerant, and is not over 80% full
- Begin recovery — start the recovery machine; typically recover liquid first for speed, then switch to vapor recovery
- Monitor progress — watch system pressure gauges and recovery cylinder weight
- Complete to required level — continue until the required vacuum level is achieved
- Isolate and verify — close valves and monitor for pressure rise (which indicates remaining refrigerant or a leak)
Liquid Recovery vs. Vapor Recovery
| Method | How It Works | Speed | When to Use |
|---|---|---|---|
| Liquid recovery | Pump liquid directly from system's liquid line | Fast | First — removes most of the charge quickly |
| Vapor recovery | Compress vapor from system's suction side | Slower | After liquid recovery — removes remaining charge |
| Push-pull | Uses recovered liquid to push remaining liquid from system | Fastest | Large commercial systems with extensive piping |
Push-Pull Recovery Method
For large systems (supermarkets, industrial installations), the push-pull method significantly speeds up recovery:
- Connect the recovery machine to the system's vapor port
- Connect a line from the recovery cylinder's liquid port back to the system's liquid line
- The recovery machine creates a pressure differential
- Liquid from the recovery cylinder is pushed through the system, displacing the remaining system liquid into the recovery cylinder
- This method leverages liquid displacement for faster recovery
Oil Changes During Recovery
When changing compressor oil during service:
- Refrigerant must be recovered to reduce pressure to 5 psig or below before changing oil
- Changing oil at pressures above 5 psig is a violation (releases excessive refrigerant dissolved in oil)
- After oil change, evacuate the system before recharging
Charging Procedures
Liquid charging is required or recommended for:
- Zeotropic blends (R-407C, R-404A) — MUST be charged as liquid
- R-410A — should be charged as liquid per manufacturer guidelines
- Any time the system nameplate or manufacturer specifies liquid charging
Vapor charging is acceptable for:
- Single-component refrigerants (R-22, R-134a) when topped off
- Azeotropic blends
Important: When liquid charging through the suction (low) side, use a metering device or flow restrictor to prevent liquid slugging the compressor.
For the Exam: Know the push-pull method for large systems. Oil changes require reducing pressure to 5 psig or below. Zeotropic blends MUST be liquid charged. Always liquid-charge R-410A through the high side, or through the low side with a metering device to prevent liquid slugging.
At what pressure must a high-pressure system be before changing compressor oil?
What is the "push-pull" recovery method used for?
When liquid-charging a system through the suction (low-pressure) side, what precaution is necessary?