CORECore25%
Ten topics, and the base for everything else. They fall into three groups. The science: how chlorine from CFC and HCFC refrigerants destroys stratospheric ozone, and which common refrigerants are CFCs, HCFCs and HFCs. The law: the Clean Air Act and the Montreal Protocol, the phaseouts, the bans on venting, the Section 608 rules on equipment, sales and reclaimed refrigerant. And the practice: the refrigeration cycle, gauges, leak detection, recovery, dehydration, cylinder safety and shipping labels.
- CORE.1Environmental impacts: how chlorine from CFC and HCFC refrigerants destroys stratospheric ozone, which common refrigerants are CFCs, HCFCs or HFCs, their relative ozone-depletion potential and atmospheric effects, and the evidence for and health and environmental effects of ozone depletion.
- CORE.2Clean Air Act and Montreal Protocol: CFC and R-22 phaseout dates, the bans on venting during service and at disposal and on venting substitute refrigerants, the maximum Clean Air Act penalty, and the Montreal Protocol's role.
- CORE.3Section 608 regulations: high- versus low-pressure refrigerants, system-dependent versus self-contained recovery equipment, which equipment the rule covers, third-party certification of recovery and recycling equipment, the purity standard for reclaimed refrigerant, the sales restriction and the venting prohibition.
- CORE.4Substitute refrigerants and oils: why there are no drop-in replacements, which lubricants are compatible with which refrigerants, and how blends fractionate when they leak.
- CORE.5Refrigeration: refrigerant state and pressure at each point of the cycle and where cooling takes place, gauge color codes, ranges and correct use, and leak detection.
- CORE.6Three R definitions: tell recovering, recycling and reclaiming refrigerant apart.
- CORE.7Recovery techniques: why refrigerants must not be mixed, and what affects recovery speed, such as ambient temperature, equipment size and hose length and diameter.
- CORE.8Dehydration evacuation: why a system is evacuated at the end of service to remove air and moisture.
- CORE.9Safety: hazards of refrigerant exposure, protective equipment, reusable recovery cylinders versus disposable cylinders, the danger of filling a cylinder beyond 80 percent, and leak testing with nitrogen through a regulator and relief valve rather than oxygen or compressed air.
- CORE.10Shipping: the refrigerant identification and DOT classification labels required on refrigerant cylinders.
Where people lose points: The three Rs, which have fixed meanings. To recover is to remove refrigerant from an appliance and store it in an external container, without necessarily testing or processing it. To recycle is to clean it for reuse, usually by separating oil and passing it through filter-driers, without meeting the reclamation standard. To reclaim is to reprocess it to the purity specifications the regulation sets, which are based on AHRI Standard 700, and verify that by analysis. Questions describe one and offer the other two as options. The cylinder rules are the other set to know exactly: a recovery cylinder is refillable and a disposable cylinder is not, a cylinder is not filled beyond 80 percent, and a system is pressurized for leak testing with nitrogen through a regulator and relief valve, never with oxygen or compressed air.
T1Type I (Small Appliances)25%
Three topics: recovery requirements, recovery techniques and safety. Know what counts as a small appliance. Know the evacuation level required in each of four cases, set by whether the recovery equipment was made before or after November 15, 1993 and whether the appliance's compressor works. Know passive, or system-dependent, recovery with an operating compressor and with one that does not run.
- T1.1Recovery requirements: what counts as a small appliance, and the evacuation levels required with a working or non-working compressor for recovery equipment made before versus after November 15, 1993.
- T1.2Recovery techniques: using pressure and temperature to identify a refrigerant and detect noncondensables, passive (system-dependent) recovery with operating and inoperative compressors, fitting high- and low-side access valves, removing solderless fittings after service, and R-134a as the likely substitute for R-12.
- T1.3Safety: the decomposition products formed when refrigerants are exposed to high temperatures.
Where people lose points: Taking the short topic list for a light section. Type I has three headings and the same 25 questions as every other section, so expect its few topics to be asked from several directions. The four-case recovery table is the place to be careful: it is easy to learn one figure and apply it to every case. The smaller points are easy marks if you have seen them: that both high-side and low-side access valves are needed when the compressor does not run, that solderless fittings come off after service, and what refrigerants break down into at high temperatures.
T2Type II (High- and Very High-Pressure)25%
Six topics, and the most rule-heavy section. Leak detection and the leak repair requirements: allowable leak rates for commercial refrigeration, industrial process refrigeration and other appliances holding more than 50 pounds, with the recordkeeping and deadline extensions that go with them. Recovery techniques and the evacuation levels required in each situation. The refrigeration topic: identifying the refrigerant, pressure-temperature relationships, and what state the refrigerant is in at each component. And safety, including equipment room requirements.
- T2.1Leak detection: signs of leakage in high-pressure systems, leak testing before charging or recharging, and the order of preference for leak-test gases.
- T2.2Leak repair requirements: allowable leak rates for commercial and industrial process refrigeration and for other appliances holding more than 50 pounds, leak repair recordkeeping, and extensions to repair deadlines.
- T2.3Recovery techniques: speeding recovery by removing liquid first, chilling the recovery vessel or heating the appliance, avoiding cross-contamination when a machine changes refrigerants, and waiting after reaching the required vacuum to see whether pressure rises.
- T2.4Recovery requirements: evacuation levels for high-pressure appliances by situation (disposal, major versus non-major repair, leaky versus non-leaky, under versus over 200 pounds, equipment built before versus after November 15, 1993), what a major repair is, and the ban on system-dependent equipment above 15 pounds of refrigerant.
- T2.5Refrigeration: identifying the refrigerant in an appliance, pressure-temperature relationships of common high-pressure refrigerants including gauge-to-absolute conversion, components of high-pressure appliances and the refrigerant state in each, and the rule that hydrocarbons are not approved for retrofits.
- T2.6Safety: never energizing a hermetic compressor under vacuum, and ASHRAE Standard 15 equipment room requirements, including oxygen deprivation sensors.
Where people lose points: The evacuation-level table has five variables: disposal or repair, major or non-major repair, leaky or not, under or over 200 pounds of refrigerant, and recovery equipment built before or after November 15, 1993. Write the table out yourself until you can do it from memory. Keep the leak-rate thresholds attached to the right category of appliance, because the options will offer the right number for the wrong category. Three single facts from the topics are worth having cold: system-dependent recovery equipment is not allowed on appliances holding more than 15 pounds, a hermetic compressor must never be energized under vacuum, and gauge pressure becomes absolute pressure by adding atmospheric pressure.
T3Type III (Low-Pressure)25%
Seven topics built on one physical fact: parts of a low-pressure system run below atmospheric pressure, so a leak draws air and moisture in instead of letting refrigerant out. That is why these systems have purge units, why excessive purging is a sign of a leak, and why leak testing means raising the system's pressure, with hot water or built-in heating first and nitrogen after. The rest follows: leak repair requirements, recovery and recharging techniques that keep water in the tubes from freezing, evacuation levels, and equipment room safety including a refrigerant sensor for R-123.
- T3.1Leak detection: preferred ways to pressurize a low-pressure system for leak testing (hot water or built-in heating, then nitrogen), signs of air leaking in such as excessive purging, the maximum leak-test pressure for centrifugal chillers, leak inspections for appliances over the leak rate, and reporting of chronically leaking appliances.
- T3.2Leak repair requirements: allowable annual leak rates for commercial and industrial process refrigeration and for other appliances holding more than 50 pounds.
- T3.3Recovery techniques: recovering liquid first and then vapor, heating oil to 130 degrees F before draining it, circulating or removing chiller water to prevent freezing during evacuation, and the high-pressure cut-out setting of recovery units used on low-pressure appliances.
- T3.4Recharging techniques: introducing vapor before liquid so water in the tubes does not freeze, and charging centrifugal chillers through the evaporator charging valve.
- T3.5Recovery requirements: evacuation levels for low-pressure appliances by situation (disposal, major versus non-major repair, leaky versus non-leaky, under versus over 200 pounds, equipment built before versus after November 15, 1993), what major and non-major repairs are, permitted ways to pressurize for a non-major repair, and waiting after reaching vacuum to check for a pressure rise.
- T3.6Refrigeration: what a purge unit does in a low-pressure system, and pressure-temperature relationships of low-pressure refrigerants.
- T3.7Safety: ASHRAE Standard 15 equipment room requirements, including oxygen deprivation sensors and a refrigerant sensor for R-123.
Where people lose points: Carrying Type II habits into Type III. The orders are the thing to learn. Recovering: liquid first, then vapor. Recharging: vapor first, then liquid, so that water in the tubes does not freeze. During evacuation, circulate or remove the chiller water for the same reason. Oil is heated to 130 degrees F before it is drained. The EPA lists the same situations for low-pressure evacuation levels as for Type II, but the required values are different, and a Universal candidate who has learned both in the same week can easily swap them.