## SECTION 110.2 – MANDATORY REQUIREMENTS FOR SPACE-CONDITIONING EQUIPMENT

Certification by Manufacturers. Any space-conditioning equipment 'listed in this section may be installed only if the manufacturer has certified to the Commission that the equipment complies with all the applicable requirements of this section.

### (a) Efficiency.

Equipment shall meet the applicable efficiency requirements in TABLE 110.2-A through TABLE 110.2-K subject to the following:

1. If more than one efficiency standard is 'listed for any equipment in TABLE 110.2-A through TABLE 110.2-K, the equipment shall meet all the applicable standards that are 'listed; and

2. If more than one test method is 'listed in TABLE 110.2-A through TABLE 110.2-K, the equipment shall comply with the applicable efficiency standard when tested with each listed’ test method; and

3. Where equipment serves more than one function, it shall comply with the efficiency standards applicable to each function; and

4. Where a requirement is for equipment rated at its "maximum rated capacity" or "minimum rated capacity," the capacity shall be as provided for and allowed by the controls, during steady-state operation.

EXCEPTION 1 to Section 110.2(a): Water-cooled centrifugal water-chilling packages that are not designed for operation at ANSI/AHRI Standard 550/590 test conditions of 44°F leaving chilled water temperature and 85°F entering condenser water temperature with 3 gallons per minute per ton condenser water flow shall have a maximum full load kW/ton and NPLV ratings adjusted using the following equation:

Adjusted maximum full-load kW/ton rating = (full-load kW/ton from TABLE 110.2-D) / Kadj

Adjusted maximum NPLV rating = (IPLV from TABLE 110.2-D) / Kadj

Where:

Kadj = (A) x (B)

A = 0.00000014592 x (LIFT)4 – 0.0000346496 x (LIFT)3+0.00314196 x (LIFT)2 – 0.147199 x (LIFT) + 3.9302

LIFT = LvgCond – LvgEvap (°F)

LvgCond = Full-load leaving condenser fluid temperature (°F)

LvgEvap = Full-load leaving evaporator fluid temperature (°F)

B = (0.0015 x LvgEvap) + 0.934

The adjusted full-load and NPLV values are only applicable for centrifugal chillers meeting all of the following full-load design ranges:

• Minimum Leaving Evaporator Fluid Temperature: 36°F

• Maximum Leaving Condenser Fluid Temperature: 115°F

• LIFT ≥ 20°F and ≤ 80°F

Centrifugal chillers designed to operate outside of these ranges are not covered by this exception.

EXCEPTION 2 to Section 110.2(a): Positive displacement (air-cooled and water-cooled) chillers with a leaving evaporator fluid temperature higher than 32°F shall show compliance with TABLE 110.2-D when tested or certified with water at standard rating conditions, per the referenced test procedure.

EXCEPTION 3 to Section 110.2(a): Equipment primarily serving refrigerated warehouses or commercial refrigeration.

### (b) Controls for Heat Pumps with Supplementary Electric Resistance Heaters.

Heat pumps with supplementary electric resistance heaters shall have controls:

1. That prevent supplementary heater operation when the heating load can be met by the heat pump alone; and

2. In which the cut-on temperature for compression heating is higher than the cut-on temperature for supplementary heating, and the cut-off temperature for compression heating is higher than the cut-off temperature for supplementary heating.

EXCEPTION 1 to Section 110.2(b): The controls may allow supplementary heater operation during:

A. Defrost; and

B. Transient periods such as start-ups and following room thermostat setpoint advance, if the controls provide preferential rate control, intelligent recovery, staging, ramping or another control mechanism designed to preclude the unnecessary operation of supplementary heating.

EXCEPTION 2 to Section 110.2(b): Room air-conditioner heat pumps.

### (c) Thermostats.

All heating or cooling systems not controlled by a central energy management control system (EMCS) shall have a setback thermostat.

1. Setback Capabilities. All thermostats shall have a clock mechanism that allows the building occupant to program the temperature setpoints for at least four periods within 24 hours. Thermostats for heat pumps shall meet the requirements of Section 110.2(b).

EXCEPTION to Section 110.2(c): Gravity gas wall heaters, gravity floor heaters, gravity room heaters, non-central electric heaters, fireplaces or decorative gas appliances, wood stoves, room air conditioners, and room air-conditioner heat pumps.

### (d) Gas-Fired and Oil-Fired Furnace Standby Loss Controls.

Gas-fired and oil-fired forced air furnaces with input ratings ≥225,000 Btu/hr shall also have an intermittent ignition or interrupted device (IID), and have either power venting or a flue damper. A vent damper is an acceptable alternative to a flue damper for furnaces where combustion air is drawn from the conditioned space. All furnaces with input ratings ≥225,000 Btu/h, including electric furnaces, that are not located within the conditioned space shall have jacket losses not exceeding 0.75 percent of the input rating.

### (e) Open and Closed Circuit Cooling Towers.

All open and closed circuit cooling tower installations shall comply with the following:

1. Be equipped with Conductivity or Flow-based Controls that maximize cycles of concentration based on local water quality conditions. Controls shall automate system bleed and chemical feed based on conductivity, or in proportion to metered makeup volume, metered bleed volume, recirculating pump run time, or bleed time. Conductivity controllers shall be installed in accordance with manufacturer’s specifications in order to maximize accuracy.

2. Documentation of Maximum Achievable Cycles of Concentration. Building owners shall document the maximum cycles of concentration based on local water supply as reported annually by the local water supplier, and using the calculator approved by the Energy Commission. The calculator is intended to determine maximum cycles based on a Langelier Saturation Index (LSI) of 2.5 or less. Building owner shall document maximum cycles of concentration on the mechanical compliance form which shall be reviewed and signed by the Professional Engineer (P.E.) of Record.

3. Be equipped with a Flow Meter with an analog output for flow either hardwired or available through a gateway on the makeup water line.

4. Be equipped with an Overflow Alarm to prevent overflow of the sump in case of makeup water valve failure. Overflow alarm shall send an audible signal or provide an alert via the Energy Management Control System to the tower operator in case of sump overflow.

5. Be equipped with Efficient Drift Eliminators that achieve drift reduction to 0.002 percent of the circulated water volume for counter-flow towers and 0.005 percent for cross-flow towers.

EXCEPTION to Section 110.2(e): Towers with rated capacity < 150 tons.

### (f) Low Leakage Air-Handling Units.

To qualify as a low leakage air-handling unit for use for meeting the requirements for applicable low leakage air-handling unit compliance credit(s) available in the performance standards set forth in Sections 150.1(b) and 140.1, the manufacturer shall certify to the Energy Commission that the air-handling unit meets the specifications in Reference Joint Appendix JA9.

#### TABLE 110.2-A AIR CONDITIONERS AND CONDENSING UNITS –
MINIMUM EFFICIENCY REQUIREMENTS

‘Equipment Type | Size Category | Efficiency a,b | Test Procedure c
Air conditioners, air cooled both split system and single package | ≥ 65,000 Btu/h and < 135,000 Btu/h | 11.2 EER 12.9 IEER | ANSI/AHRI 340/360
≥ 135,000 Btu/h and < 240,000 Btu/h | 11.0 EER 12.4 IEER | ANSI/AHRI 340/360
≥ 240,000 Btu/h and < 760,000 Btu/h | 10.0 EER 11.6 IEER
≥ 760,000 Btu/h | 9.7 EER 11.2 IEER
Air conditioners, water cooled | ≥ 65,000 Btu/h and < 135,000 Btu/h | 12.1 EER 13.9 IEER | ANSI/AHRI 340/360
≥135,000 Btu/h and < 240,000 Btu/h | 12.5 EER 13.9 IEER | ANSI/AHRI 340/360
≥240,000 Btu/h and < 760,000 Btu/h | 12.4 EER 13.6 IEER | ANSI/AHRI 340/360
≥ 760,000 Btu/h | 12.2EER 13.5 IEER | ANSI/AHRI 340/360
Air conditioners, evaporatively cooled | ≥65,000 Btu/h and < 135,000 Btu/h | 12.1 EERb 12.3 IEERb | ANSI/AHRI 340/360
≥ 135,000 Btu/h and < 240,000 Btu/h | 12.0 EERb 12.2 IEERb | ANSI/AHRI 340/360
≥240,000 Btu/h and < 760,000 Btu/h | 11.9 EERb 12.1 IEERb | ANSI/AHRI 340/360
≥ 760,000 Btu/h | 11.7 EERb 11.9 IEERb | ANSI/AHRI 340/360
Condensing units, air cooled | ≥ 135,000 Btu/h | 10.5 EER 11.8 IEER | ANSI/AHRI 365
Condensing units, water cooled | ≥ 135,000 Btu/h | 13.5 EER 14.0 IEER
Condensing units, evaporatively cooled | ≥ 135,000 Btu/h | 13.5 EER 14.0 IEER
a IEERs are only applicable to equipment with capacity control as specified by ANSI/AHRI 340/360 test procedures b Deduct 0.2 from the required EERs and IEERs for units with a heating section other than electric resistance heat. c Applicable test procedure and reference year are provided under the definitions.

#### TABLE 110.2-B HEAT PUMPS,
MINIMUM EFFICIENCY REQUIREMENTS

‘Equipment Type | Size Category | Efficiency a, b | Test Procedurec
Air Cooled (Cooling Mode) both split system and single package | ≥ 65,000 Btu/h and < 135,000 Btu/h |  | 11.0 EER 12.2 IEER | ANSI/AHRI 340/360
≥ 135,000 Btu/h and < 240,000 Btu/h |  | 10.6 EER 11.6 IEER
≥ 240,000 Btu/h |  | 9.5 EER 10.6 IEER
Water source (cooling mode) | ≥ 65,000 Btu/h and < 135,000 Btu/h | 86ºF entering water | 13.0 EER | ISO-13256-1
Groundwater source (cooling mode) | < 135,000 Btu/h | 59ºF entering water | 18.0 EER | ISO-13256-1
Ground source (cooling mode) | < 135,000 Btu/h | 77ºF entering water | 14.1 EER | ISO-13256-1
Water source water-to-water (cooling mode) | < 135,000 Btu/h | 86ºF entering water | 10.6 EER | ISO-13256-2
Groundwater source water-to-water (cooling mode) | < 135,000 Btu/h | 59ºF entering water | 16.3 EER | ISO-13256-1
Ground source brine-to-water (cooling mode) | < 135,000 Btu/h | 77ºF entering water | 12.1 EER | ISO-13256-2
Air Cooled (Heating Mode) Split system and single package | ≥ 65,000 Btu/h and < 135,000 Btu/h (cooling capacity) | 47° F db/43° F wb outdoor air | 3.3 COP | ANSI/AHRI 340/360
≥ 135,000 Btu/h and < 240,000 Btu/h | 17° F db/15° F wb outdoor air | 2.25 COP |
Groundwater source (heating mode) | ≥ 135,000 Btu/h (cooling capacity) | 47° F db/43° F wb outdoor air | 3.2 COP | ISO-13256-1
Ground source (heating mode) | < 135,000 Btu/h (cooling capacity) | 17° F db/15° F wb outdoor air | 2.05 COP | ISO-13256-1
|  |  |  |  |  |

#### CONTINUED: TABLE 110.2-B HEAT PUMPS, MINIMUM EFFICIENCY REQUIREMENTS

‘Equipment Type | Size Category | Subcategory or Rating Condition | Efficiency a | Test Procedurec
Water source (heating mode) | < 135,000 Btu/h (cooling capacity) | 68ºF entering water | 4.3 COP | ISO-13256-1
≥ 135,000 Btu/h and < 240,000 Btu/h | 68ºF entering water | 2.90 COP
Groundwater source (heating mode) | < 135,000 Btu/h (cooling capacity) | 50ºF entering water | 3.7 COP | ISO-13256-1
Ground source (heating mode) | < 135,000 Btu/h (cooling capacity) | 32ºF entering water | 3.2 COP | ISO-13256-1
Water source water-to-water (heating mode) | < 135,000 Btu/h (cooling capacity) | 68ºF entering water | 3.7 COP | ISO-13256-2
Groundwater source water-to-water (heating mode) | < 135,000 Btu/h (cooling capacity) | 50ºF entering water | 3.1 COP | ISO-13256-2
Ground source brine-to-water (heating mode) | < 135,000 Btu/h (cooling capacity) | 32ºF entering water | 2.5 COP | ISO-13256-2
a IEERs are only applicable to equipment with capacity control as as specified by ANSI/AHRI 340/360 test procedures. b Deduct 0.2 from the required EERs and IEERs for units with a heating section other than electric resistance heat. c Applicable test procedure and reference year are provided under the definitions.

#### TABLE 110.2-C AIR-COOLED GAS-ENGINE HEAT PUMPS

‘Equipment Type | Size Category | Subcategory or Rating Condition | Efficiency | Test Procedurea
Air-Cooled Gas-Engine 'Heat Pump (Cooling Mode) | All Capacities | 95° F db Outdoor Air | 0.60 COP | ANSI Z21.40.4A
Air-Cooled Gas-Engine 'Heat Pump (Heating Mode) | All Capacities | 47° F db/43° F wb Outdoor Air | 0.72 COP | ANSI Z21.40.4A
a Applicable test procedure and reference year are provided under the definitions.

#### TABLE 110.2-D WATER CHILLING PACKAGES
MINIMUM EFFICIENCY REQUIREMENTS a,b

‘Equipment Type | Size Category | Path A Efficiency a,b | Path B Efficiency a,b | Test Procedure c
Air Cooled, With Condenser Electrically Operated | < 150 Tons | ≥ 10.100 EER ≥ 13.700 IPLV | ≥ 9.700 EER ≥15.800 IPLV | AHRI 550/590
≥ 150 Tons | ≥ 10.100 EER ≥ 14.000 IPLV | ≥ 9.700 EER ≥16.100 IPLV
Air Cooled, Without Condenser Electrically Operated | All Capacities | Air-cooled chillers without condensers must be rated with matching condensers and comply with the air-cooled chiller efficiency requirements..
Water Cooled, Electrically Operated, Reciprocating | All Capacities | Reciprocating units must comply with the water-cooled positive displacement efficiency requirements | AHRI 550/590
Water Cooled, Electrically Operated Positive Displacement | < 75 Tons | ≤0.750 kW/ton ≤ 0.600 IPLV | ≤ 0.780 kW/ton ≤ 0.500 IPLV | AHRI 550/590
≥ 75 tons and < 150 tons | ≤ 0.720 kW/ton ≤ 0.560 IPLV | ≤ 0.750 kW/ton ≤ 0.490 IPLV
≥ 150 tons and < 300 tons | ≤ 0.660 kW/ton ≤ 0.540 IPLV | ≤ 0.680 kW/ton ≤ 0.440 IPLV
≥ 300 tons and < 600 tons | ≤ 0.610 kW/ton ≤ 0.520 IPLV | ≤ 0.625 kW/ton ≤ 0.410 IPLV
> 600 tons | ≤ 0.560 kW/ton ≤ 0.500 IPLV | ≤ 0.585 kW/ton ≤ 0.380 IPLV
Water Cooled, Electrically Operated, Centrifugal | < 150 Tons | ≤ 0.610 kW/ton ≤ 0.550 IPLV | ≤ 0.695 kW/ton ≤ 0.440 IPLV
≥ 150 tons and < 300 tons | ≤ 0.610 kW/ton ≤ 0.550 IPLV | ≤ 0.635 kW/ton ≤ 0.400 IPLV
≥ 300 tons and < 400 tons | ≤ 0.560 kW/ton ≤ 0.520 IPLV | ≤ 0.595 kW/ton ≤ 0.390 IPLV
≥ 400 tons and < 600 tons | ≤ 0. 560 kW/ton ≤ 0. 500 IPLV | ≤ 0. 585 kW/ton ≤ 0. 380 IPLV
≥ 600 tons | ≤ 0.560 kW/ton ≤ 0.500 IPLV | ≤ 0.585 kW/ton ≤ 0.380 IPLV
Air Cooled Absorption, Single Effect | All Capacities | ≥0.600 COP | N.A. d | ANSI/AHRI 560
Water Cooled Absorption, Single Effect | All Capacities | ≥ 0.700 COP | N.A. d
Absorption Double Effect, Indirect-Fired | All Capacities | ≥ 1.000 COP ≥ 1.050 IPLV | N.A. d
Absorption Double Effect, Direct-Fired | All Capacities | ≥ 1.000 COP ≥1.000 IPLV | N.A. d
Water Cooled Gas Engine Driven Chiller | All Capacities | ≥ 1.2 COP ≥ 2.0 IPLV | N.A. d | ANSI Z21.40.4A
a No requirements for: • Centrifugal chillers with design leaving evaporator temperature < 36°F; or • Positive displacement chillers with design leaving fluid temperature ≤ 32°F; • or Absorption chillers with design leaving fluid temperature < 40°F b Must meet the minimum requirements of Path A or Path B. However, both the full load (COP) and IPLV must be met to fulfill the requirements of the applicable Path. c See Section 100.1 for definitions d NA means not applicable

#### TABLE 110.2-E PACKAGED TERMINAL AIR CONDITIONERS AND PACKAGED
TERMINAL HEAT PUMPS – MINIMUM EFFICIENCY REQUIREMENTS

‘Equipment Type | Size Category (Input) | Subcategory or Rating Condition | Efficiency | Test Procedure c
PTAC (Cooling mode) Newly constructed or newly conditioned buildings or additions | All Capacities | 95°F db Outdoor Air | 14.0 - (0.300 x Cap/1000) a EER | ANSI/ AHRI/ CSA 310/380
PTAC (Cooling mode) Replacements b | All Capacities | 95°F db Outdoor Air | 10.9 - (0.213 x Cap/1000) a EER
PTHP (Cooling mode) Newly constructed or newly conditioned buildings or additions | All Capacities | 95°F db Outdoor Air | 14.0 - (0.300 x Cap/1000) a EER
PTHP (Cooling mode) Replacements b | All Capacities | 95°F db Outdoor Air | 10.8 - (0.213 x Cap/1000) a EER
PTHP (Heating Mode) Newly constructed or newly conditioned buildings or additions | All Capacities | - | 3.7 - (0.052 x Cap/1000) a COP
PTHP (Heating mode)Replacements b | All Capacities | - | 2.9 - (0.026 x Cap/1000) a COP
SPVAC (Cooling Mode) | <65,000 Btu/h | 95°F db / 75°F wb Outdoor Air | 11.0 EER | ANSI/AHRI 390
≥65,000 Btu/h and <135,000 Btu/h | 95°F db / 75°F wb Outdoor Air | 10.0 EER
≥135,000 Btu/h and <240,000 Btu/h | 95°F db / 75°F wb Outdoor Air | 10.0 EER
SPVAC (Cooling Mode) nonweatherized space constrained | ≤ 30,000 Btu/h | "95 ⁰ F db / 75 ⁰ F wb outdoor air" | 9.20 EER
> 30,000 Btu/h and ≤ 36,000 Btu/h | "95 ⁰ F db / 75 ⁰ F wb outdoor air" | 9.00 EER
SPVHP (Cooling Mode) | <65,000 Btu/h | 95°F db / 75°F wb Outdoor Air | 10.0 EER
≥65,000 Btu/h and <135,000 Btu/h | 95°F db / 75°F wb Outdoor Air | 10.0 EER
≥135,000 Btu/h and <240,000 Btu/h | 95°F db / 75°F wb Outdoor Air | 10.0 EER
SPVHP (Cooling Mode) nonweatherized space constrained | ≤ 30,000 Btu/h | 95°F db / 75°F wb Outdoor Air | 9.20 EER
> 30,000 Btu/h and ≤ 36,000 Btu/h | 95°F db / 75°F wb Outdoor Air | 9.00 EER
SPVHP (Heating Mode) | <65,000 Btu/h | 47°F db / 43°F wb Outdoor Air | 3.3 COP
≥65,000 Btu/h and <135,000 Btu/h | 47°F db / 43°F wb Outdoor Air | 3.0 COP
≥135,000 Btu/h and <240,000 Btu/h | 47°F db / 43°F wb Outdoor Air | 3.0 COP
SPVHP (Heating Mode) nonweatherized space constrained | ≤ 30,000 Btu/h | 47°F db / 43°F wb Outdoor Air | 3.00 COP
> 30,000 Btu/h and ≤ 36,000 Btu/h | 47°F db / 43°F wb Outdoor Air | 3.00 COP
a Cap means the rated cooling capacity of the product in Btu/h. If the unit’s capacity is less than 7000 Btu/h, use 7000 Btu/h in the calculation. If the unit’s capacity is greater than 15,000 Btu/h, use 15,000 Btu/h in the calculation b Replacement units must be factory labeled as follows: "MANUFACTURED FOR REPLACEMENT APPLICATIONS ONLY; NOT TO BE INSTALLED IN NEWLY CONSTRUCTED BUILDINGS." Replacement efficiencies apply only to units with existing sleeves less than 16 inches high or less than 42 inch wide and having a cross-sectional area less than 670 square inches. c Applicable test procedure and reference year are provided under the definitions.

#### TABLE 110.2-F HEAT TRANSFER EQUIPMENT

‘Equipment Type | Subcategory | Minimum Efficiencya | Test Procedure b
Liquid-to-liquid heat exchangers | Plate type | NR | ANSI/AHRI 400
a NR - means no requirement b Applicable test procedure and reference year are provided under the definitions

#### TABLE 110.2-G PERFORMANCE REQUIREMENTS FOR HEAT REJECTION EQUIPMENT

‘Equipment Type | Total System Heat Rejection Capacity at Rated Conditions | Subcategory or Rating Condition | Performance Required ,a ,b, c, d | Test Procedure e
Propeller or axial fan Open-circuit cooling towers | All | 95°F entering water 85°F leaving water 75 °F entering air wb | >42.1 gpm/hp | CTI ATC-105 and CTI STD-201 RS
Centrifugal fan Open-circuit cooling towers | All | 95°F entering water 85°F leaving water 75 °F entering air wb | > 20.0 gpm/hp
Propeller or axial fan closed-circuit cooling towers | All | 102°F entering water 90°F leaving water 75 °F entering air wb | > 16.1 gpm/hp
Centrifugal fan closed-circuit cooling towers | All | 102°F entering water 90°F leaving water 75 °F entering air wb | > 7.0 gpm/hp
Propeller or axial fan evaporative condensers | All | R-507A test fluid 165 ⁰ F entering gas temp 105 ⁰ F condensing temp 75 ⁰ F entering air wb" | ≥ 157,000 Btu/h • hp | CTI ATC-106
All | Ammonia test fluid 140 ⁰ F entering gas temp 96.3 ⁰ F condensing temp 75 ⁰ F entering air wb" | ≥ 134,000 Btu/h • hp
Centrifugal fan evaporative condensers | All | R-507A test fluid 165 ⁰ F entering gas temp 105 ⁰ F condensing temp 75 ⁰ F entering air wb" | ≥ 135,000 Btu/h • hp
All | Ammonia test fluid 140 ⁰ F entering gas temp 96.3 ⁰ F condensing temp 75 ⁰ F entering air wb" | ≥ 110,000 Btu/h • hp
Air cooled condensers | All | 125°F condensing temperature R22 test fluid 190°F entering gas temperature 15°F subcooling 95°F entering drybulb | >176,000 Btu/h • hp | ANSI/AHRI 460
a For purposes of this table, open-circuit cooling tower performance is defined as the water flow rating of the tower at the given rated conditions divided by the fan motor nameplate power. b For purposes of this table, closed-circuit cooling tower performance is defined as the process water flow rating of the tower at the given rated conditions divided by the sum of the fan motor nameplate rated power and the integral spray pump motor nameplate power . c For purposes of this table air-cooled condenser performance is defined as the heat rejected from the refrigerant divided by the fan motor nameplate power. d Open cooling towers shall be tested using the test procedures in CTI ATC-105. Performance of factory assembled open cooling towers shall be either certified as base models as specified in CTI STD-201 or verified by testing in the field by a CTI approved testing agency. Open factory assembled cooling towers with custom options added to a CTI certified base model for the purpose of safe maintenance or to reduce environmental or noise impact shall be rated at 90 percent of the CTI certified performance of the associated base model or at the manufacturer’s stated performance, whichever is less. Base models of open factory assembled cooling towers are open cooling towers configured in exact accordance with the Data of Record submitted to CTI as specified by CTI STD-201. There are no certification requirements for field erected cooling towers. e Applicable test procedure and reference year are provided under the definitions. For refrigerated warehouses or commercial refrigeration applications, condensers shall comply with requirements specified by Section 120.6(a)|topic=(a) Mandatory Requirements for Refrigerated Warehouses or Section 120.6(b)|topic=(b) Mandatory Requirements for Commercial Refrigeration or 120.6(b)

#### TABLE 110.2-H Electrically Operated Variable Refrigerant Flow (VRF) Air Conditioners
Minimum Efficiency Requirements

‘Equipment Type | Size Category | Heating Section Type | Sub-Category or Rating Condition | Minimum Efficiency | Test Procedurea
VRF Air Conditioners, Air Cooled | <65,000 Btu/h | All | VRF Multi-split System | 13.0 SEER | ANSI/AHRI 1230
≥65,000 Btu/h and <135,000 Btu/h | Electric Resistance (or none) | VRF Multi-split System | 11.2 EER 15.5 IEER b
≥135,000 Btu/h and <240,000 Btu/h | Electric Resistance (or none) | VRF Multi-split System | 11.0 EER 14.9 IEER b
≥240,000 Btu/h | Electric Resistance (or none) | VRF Multi-split System | 10.0 EER 13.9 IEER b
a Applicable test procedure and reference year are provided under the definitions. b IEERs are only applicable to equipment with capacity control as specified by ANSI/AHRI 1230 test procedures.

#### TABLE 110.2-I Electrically Operated Variable Refrigerant Flow Air-to-Air and Applied Heat Pumps -
Minimum Efficiency Requirements

‘Equipment Type | Size Category | Heating Section Type | Sub-Category or Rating Condition | Minimum Efficiency | Test Procedure b
VRF Air Cooled, (cooling mode) | <65,000 Btu/h | All | VRF Multi-split System | 13.0 SEER | AHRI 1230
≥65,000 Btu/h and <135,000 Btu/h | Electric Resistance (or none) | VRF Multi-split System a | 11.0 EER 14.6 IEER c
≥135,000 Btu/h and <240,000 Btu/h | Electric Resistance (or none) | VRF Multi-split System a | 10.6 EER 13.9 IEER c
≥240,000 Btu/h | Electric Resistance (or none) | VRF Multi-split System a | 9.5 EER 12.7 IEER c
VRF Water source (cooling mode) | <65,000 Btu/h | All | VRF Multi-split systemsa 86ºF entering water | 12.0 EER 15.8 IEER | AHRI 1230
≥65,000 Btu/h and <135,000 Btu/h | All | VRF Multi-split Systema 86ºF entering water | 12.0 EER 15.8 IEER
≥135,000 Btu/h and < 240,000 | All | VRF Multi-split Systema 86ºF entering water | 10.0 EER 13.8 IEER
≥ 240,000 Btu/h | All | VRF Multi-split Systema 86oF entering water | 10.0 EER 12.0 IEER
VRF Groundwater source (cooling mode) | <135,000 Btu/h | All | VRF Multi-split Systema 59ºF entering water | 16.2 EER | AHRI 1230
≥135,000 Btu/h | All | VRF Multi-split Systema 59ºF entering water | 13.8 EER
VRF Ground source (cooling mode) | <135,000 Btu/h | All | VRF Multi-split Systema 77ºF entering water | 13.4 EER | AHRI 1230
≥135,000 Btu/h | All | VRF Multi-split Systema 77ºF entering water | 11.0 EER
VRF Air Cooled (heating mode) | <65,000 Btu/h (cooling capacity) | - - - | VRF Multi-split System | 7.7 HSPF | AHRI 1230
≥65,000 Btu/h and <135,000 Btu/h (cooling capacity) | - - - | VRF Multi-split system47ºF db/ 43ºF wb outdoor air | 3.3 COP
VRF Multi-split system17ºF db/15ºF wb outdoor air | 2.25 COP
≥135,000 Btu/h (cooling capacity) | - - - | VRF Multi-split system 47ºF db/ 43ºF wb outdoor air | 3.2 COP
VRF Multi-split system 17ºF db/15ºF wb outdoor air | 2.05 COP
VRF Water source (heating mode) | <135,000 Btu/h (cooling capacity) | --- | VRF Multi-split System 68ºF entering water | 4.2 COP | AHRI 1230
≥135,000 Btu/h (cooling capacity) | --- | VRF Multi-split System 68ºF entering water | 3.9 COP
VRF Groundwater source (heating mode) | <135,000 Btu/h (cooling capacity) | --- | VRF Multi-split System 50ºF entering water | 3.6 COP | AHRI 1230
≥135,000 Btu/h (cooling capacity) | --- | VRF Multi-split System 50ºF entering water | 3.3 COP
VRF Ground source (heating mode) | <135,000 Btu/h (cooling capacity) | --- | VRF Multi-split System 32ºF entering water | 3.1 COP | AHRI 1230
≥135,000 Btu/h (cooling capacity) | --- | VRF Multi-split System 32ºF entering water | 2.8 COP
a Deduct 0.2 from the required EERs and IEERs for Variable Refrigerant Flow (VRF) Multi-split system units with a heating recovery section. b Applicable test procedure and reference year are provided under the definitions. c IEERs are only applicable to equipment with capacity control as specified by ANSI/AHRI 1230 test procedures.

#### TABLE 110.2-J Warm-Air Furnaces and Combination Warm-Air Furnaces/Air-Conditioning Units,
Warm-Air Duct Furnaces, and Unit Heaters

‘Equipment Type | Size Category (Input) | Subcategory or Rating Conditionb | Minimum Efficiencyd,e | Test Procedurea
Warm-Air Furnace, Gas-Fired | ≥ 225,000 Btu/h | Maximum Capacityb | 80% Et | Section 2.39, Thermal Efficiency, ANSI Z21.47
Warm-Air Furnace, oil-Fired | ≥ 225,000 Btu/h | Maximum Capacityb | 81% Et | Section 42, Combustion, UL 727
Warm-Air Duct Furnaces, Gas-Fired | All Capacities | Maximum Capacityb | 80% Ec | Section 2.10, Efficiency, ANSI Z83.8
Warm-Air Unit Heaters, Gas-Fired | All Capacities | Maximum Capacityb | 80% Ec | Section 2.10, Efficiency, ANSI Z83.8
Warm-Air Unit Heaters, Oil-Fired | All Capacities | Maximum Capacityb | 81% Ec | Section 40, Combustion, UL 731
a Applicable test procedure and reference year are provided under the definitions. b Compliance of multiple firing rate units shall be at maximum firing rate. c Combustion units not covered by the U.S. Department of Energy Code of Federal Regulations 10 CFR 430 (3-phase power or cooling capacity greater than or equal to 19 kW) may comply with either rating. d Et= thermal efficiency. Units must also include an interrupted or intermittent ignition device (IID), have jacket losses not exceeding 0.75% of the input rating, and have either power venting or a flue damper. A vent damper is an acceptable alternative to a flue damper for those furnaces where combustion air is drawn from the conditioned space. e Ec= combustion efficiency (100% less flue losses). See test procedure for detailed discussion. f As of August 8, 2008, according to the Energy Policy Act of 2005, units must also include interrupted or intermittent ignition device (IID) and have either power venting or an automatic flue damper.

#### TABLE 110.2-K Gas- and Oil-Fired Boilers,
Minimum Efficiency requirements

‘Equipment Type | Sub Category | Size Category (Input) | Minimum Efficiency b,c | Test Procedure a
|  |  | Before 3/2/2020 | After 3/2/2020 |
Boiler, hot water | Gas-Fired | < 300,000 Btu/h | 82% AFUE | 82% AFUE | DOE 10 CFR Part 430
≥ 300,000 Btu/h and ≤ 2,500,000 Btu/h d | 80% Et | 80% Et | DOE 10 CFR Part 431
> 2,500,000 Btu/h e | 82% Ec | 82% Ec
Oil-Fired | < 300,000 Btu/h | 84% AFUE | 84% AFUE | DOE 10 CFR Part 430
≥ 300,000 Btu/h and ≤ 2,500,000 Btu/h d | 82% Et | 82% Et | DOE 10 CFR Part 431
> 2,500,000 Btu/h e | 84% Ec | 84% Ec
Boiler, steam | Gas-Fired | < 300,000 Btu/h | 80% AFUE | 80% AFUE | DOE 10 CFR Part 430
Gas-Fired all, except natural draft | ≥ 300,000 Btu/h and ≤ 2,500,000 Btu/h d | 79% Et | 79% Et | DOE 10 CFR Part 431
> 2,500,000 Btu/h e | 79% Et | 79% Et | DOE 10 CFR Part 431
Gas-Fired, natural draft | ≥ 300,000 Btu/h and ≤ 2,500,000 Btu/h d | 77% Et | 79% Et | DOE 10 CFR Part 431
> 2,500,000 Btu/h e | 77% Et | 79% Et | DOE 10 CFR Part 431
Oil-Fired | < 300,000 Btu/h | 82% AFUE | 82% AFUE | DOE 10 CFR Part 430
≥ 300,000 Btu/h and ≤ 2,500,000 Btu/h d | 81% Et | 81% Et | DOE 10 CFR Part 431
> 2,500,000 Btu/h e | 81% Et | 81% Et | DOE 10 CFR Part 431
a Applicable test procedure and reference year are provided under the definitions. b Ec = combustion efficiency (100% less flue losses). See reference document for detailed information c Et= thermal efficiency. See test procedure for detailed information. d Maximum capacity - minimum and maximum ratings as provided for and allowed by the unit’s controls. e Included oil-fired (residual).

NOTE: Authority: Sections 25213, 25218, 25218.5, 25402 and 25402.1, Public Resources Code. Reference: Sections 25007, 25008, 25218.5, 25310, 25402, 25402.1, 25402.4, 25402.8, and 25943, Public Resources Code