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 can serve more than one function, such as both heating and cooling, or both space heating and water heating, it shall comply with all 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 = (fullload 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- 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.

(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 unitary heating or cooling systems, including heat pumps, 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, noncentral electric heaters, fireplaces or decorative gas appliances, wood stoves, room air conditioners, and room air-conditioner heat pumps.

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

Gas-fired and oil-fired forced air furnaces with input ratings ≥225,000 Btu/h 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  ELECTRICALLY OPERATED UNITARY AIR CONDITIONERS AND CONDENSING UNITS – MINIMUM EFFICIENCY REQUIREMENTS

Equipment Type

Size Category

Efficiency a

Test Procedurec

Before 1/1/2015

After 1/1/2015

Air conditioners,

air cooled

both split system

and single package

≥ 65,000 Btu/h and

< 135,000 Btu/h

11.2 EERb

11.4 IEERb

Applicable minimum efficiency values as determined by Title 20

California Code of Regulations Section 1605.1

 

ANSI/AHRI 340/360

 

≥ 135,000 Btu/h and

< 240,000 Btu/h

11.0 EERb

11.2 IEERb

ANSI/AHRI 340/360

≥ 240,000 Btu/h and

< 760,000 Btu/h

10.0 EERb

10.1 IEERb

≥ 760,000 Btu/h

9.7 EERb

9.8 IEERb

Air conditioners,

water 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

12.5 EERb

12.5 IEERb

ANSI/AHRI 340/360

≥240,000 Btu/h and

< 760,000 Btu/h

12.4 EERb

12.6 IEERb

ANSI/AHRI 340/360

≥ 760,000 Btu/h

12.2 EERb

12.4 IEERb

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 per 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 UNITARY AND APPLIED HEAT PUMPS, MINIMUM EFFICIENCY REQUIREMENTS

Equipment Type

Size Category

Subcategory or Rating Condition

Efficiency a

Test Procedurec

Air Cooled

(Cooling Mode)

≥ 65,000 Btu/h and  
< 135,000 Btu/h

Split system and

single package

11.0 EERb

11.2 IEERb

ANSI/AHRI 340/360

 

≥ 135,000 Btu/h and

< 240,000 Btu/h

10.6 EERb

10.7 IEERb

 

≥  240,000 Btu/h

9.5 EERb

9.6 IEERb

Water source (cooling mode)

≥ 65,000 Btu/h and  
< 135,000 Btu/h

86ºF entering water

12.0 EER

ISO-13256-1

Groundwater source (cooling mode)

 

< 135,000 Btu/h

59ºF entering water

16.2 EER

ISO-13256-1

Ground source (cooling mode)

 

< 135,000 Btu/h

77ºF entering water

13.4 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

17° F db/15° F wb  
outdoor air

2.25 COP

 

≥ 135,000 Btu/h

(cooling capacity)

47° F db/43° F wb  
outdoor air

3.2 COP

 

17° F db/15° F wb  
outdoor air

2.05 COP

 

CONTINUED: TABLE 110.2-B UNITARY AND APPLIED 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

4.2 COP

ISO-13256-1

Groundwater source (heating mode)

 

< 135,000 Btu/h

(cooling capacity)

50ºF entering water

3.6 COP

ISO-13256-1

Ground source (heating mode)

 

< 135,000 Btu/h

(cooling capacity)

32ºF entering water

3.1 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 per 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 Procedure

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

≥ 9.562 EER

≥ 12.500 IPLV

N.A. d

AHRI 550/590

 

 

≥ 150 Tons

≥  9.562 EER
≥ 12.750 IPLV

N.A. d

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

(Reciprocating)

Water Cooled,
Electrically Operated Positive Displacement

< 75 Tons

≤0.780 kW/ton

≤ 0.630 IPLV

≤ 0.800 kW/ton

≤ 0.600 IPLV

AHRI 550/590

≥ 75 tons and < 150 tons

≤ 0.775 kW/ton

0.615 IPLV

≤ 0.790 kW/ton

≤ 0.586 IPLV

≥ 150 tons and < 300 tons

≤ 0.680 kW/ton

≤ 0.580 IPLV

≤ 0.718 kW/ton

≤ 0.540 IPLV

≥ 300 Tons

≤ 0.620 kW/ton

≤ 0.540 IPLV

≤ 0.639 kW/ton

≤ 0.490 IPLV

Water Cooled, Electrically Operated, Centrifugal

< 150 Tons

≤ 0.634 kW/ton

≤ 0.596 IPLV

≤ 0.639 kW/ton

≤ 0.450 IPLV

≥ 150 tons and < 300 tons

0.634 kW/ton

≤ 0.596 IPLV

≤ 0.639 kW/ton

≤ 0.450 IPLV

≥ 300 tons and < 600 tons

0.576 kW/ton

0.549 IPLV

≤ 0.600 kW/ton

≤ 0.400 IPLV

≥ 600 Tons

≤ 0.570 kW/ton

≤ 0.539 IPLV

≤ 0.590 kW/ton

≤ 0.400 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

 

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

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.

See Section 100.1 for definitions

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

Before 10/08/2012

After 10/08/2012

PTAC (Cooling mode)

Newly constructed or newly conditioned buildings or additions

All Capacities

95°F db Outdoor Air

12.5 - (0.213 x Cap/1000)a EER

13.8 - (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

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

12.3 - (0.213 x Cap/1000) a EER

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

10.8 - (0.213 x Cap/1000) a EER

PTHP  (Heating Mode)

Newly constructed or newly conditioned buildings or additions

All Capacities

-

3.2 - (0.026 x Cap/1000) a COP

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

2.9 - (0.026 x Cap/1000) a COP

SPVAC (Cooling Mode)

<65,000 Btu/h

95°F db / 75°F wb
Outdoor Air

9.0 EER

9.0 EER

ANSI/AHRI 390

 

≥65,000 Btu/h and
<135,000 Btu/h

95°F db / 75°F wb
Outdoor Air

8.9 EER

8.9 EER

≥135,000 Btu/h and
<240,000 Btu/h

95°F db / 75°F wb
Outdoor Air

8.6 EER

8.6 EER

SPVHP (Cooling Mode)

<65,000 Btu/h

95°F db / 75°F wb
Outdoor Air

9.0 EER

9.0 EER

 

≥65,000 Btu/h and
<135,000 Btu/h

95°F db / 75°F wb
Outdoor Air

8.9 EER

8.9 EER

≥135,000 Btu/h and
<240,000 Btu/h

95°F db / 75°F wb
Outdoor Air

8.6 EER

8.6 EER

SPVHP (Heating Mode)

<65,000 Btu/h

47°F db / 43°F wb
Outdoor Air

3.0 COP

3.0 COP

 

≥65,000 Btu/h and
<135,000 Btu/h

47°F db / 43°F wb
Outdoor Air

3.0 COP

3.0 COP

≥135,000 Btu/h and
<240,000 Btu/h

47°F db / 43°F wb
Outdoor Air

2.9 COP

2.9 COP

 Cap means the rated cooling capacity of the product in Btu/h. If the unit’s capacity is less than 7000 Btu/h, use 7,000 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 = 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

 

Centrifugal fan

Open-circuit cooling towers

All

95°F entering water

85°F leaving water

75 °F entering air wb

  20.0 gpm/hp

CTI ATC-105

and

CTI STD-201

Propeller or axial fan

closed-circuit  cooling towers

All

102°F entering water

90°F leaving water

75 °F entering air wb

  14.0 gpm/hp

CTI ATC-105S

and

CTI STD-201

Centrifugal fan

closed-circuit cooling towers

All

102°F entering water

90°F leaving water

75 °F entering air wb

  7.0 gpm/hp

CTI ATC-105S

and

CTI STD-201

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.

                                                                                                                

 

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 Procedure a

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

13.1 IEER b

≥135,000 Btu/h and <240,000 Btu/h

Electric Resistance (or none)

VRF Multi-split System

11.0 EER

12.9 IEER b

≥240,000 Btu/h

Electric Resistance (or none)

VRF Multi-split System

10.0 EER

11.6 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 per 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

12.9 IEER c

≥135,000 Btu/h and <240,000 Btu/h

Electric Resistance (or none)

VRF Multi-split System a

10.6 EER

12.3 IEER c

≥240,000 Btu/h

Electric Resistance (or none)

VRF Multi-split System a

9.5 EER

11.0 IEER c

VRF Water source

(cooling mode)

<65,000 Btu/h

All

VRF Multi-split systems a

86ºF entering water

12.0 EER

AHRI 1230

≥65,000 Btu/h and

<135,000 Btu/h

All

VRF Multi-split System a

86ºF entering water

12.0 EER

 

≥135,000 Btu/h

All

VRF Multi-split System a

86ºF entering water

10.0 EER

 

VRF Groundwater source (cooling mode)

 

<135,000 Btu/h

All

VRF Multi-split System

59ºF entering water

16.2 EER

AHRI 1230

≥135,000 Btu/h

All

VRF Multi-split System a

59ºF entering water

13.8 EER

VRF Ground source (cooling mode)

 

<135,000 Btu/h

All

VRF Multi-split System a

77ºF entering water

13.4 EER

AHRI 1230

 

≥135,000 Btu/h

All

VRF Multi-split System a

77ºF entering water

11.0 EER

 

 

CONTINUED:   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

(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 system

47ºF db/ 43ºF wb outdoor air

3.3 COP

VRF Multi-split system

17ºF 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 per 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 Condition b

Minimum Efficiency d,e

Test Procedure a

Warm-Air Furnace, Gas-Fired


< 225,000 Btu/h

Maximum Capacityb

78% AFUE or 80% Et

DOE 10 CFR Part 430 or Section 2.39, Thermal Efficiency, ANSI Z21.47


≥ 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

78% AFUE or 80% Et

DOE 10 CFR Part 430 or Section 42, Combustion, UL 727


≥ 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

80% 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 NAECA (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

Boiler, hot water

Gas-Fired

< 300,000 Btu/h

82% AFUE

DOE 10 CFR Part 430

≥ 300,000 Btu/h and

≤ 2,500,000 Btu/h d

80% Et

DOE 10 CFR Part 431

>  2,500,000 Btu/h e

82% Ec

Oil-Fired

< 300,000 Btu/h

84% AFUE

DOE 10 CFR Part 430

≥ 300,000 Btu/h and

≤ 2,500,000 Btu/h d

82% Et

DOE 10 CFR Part 431

>  2,500,000 Btu/h e

84% Ec

Boiler, steam

Gas-Fired

< 300,000 Btu/h

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

DOE 10 CFR Part 431

> 2,500,000 Btu/h e

79% Et

DOE 10 CFR Part 431

Gas-Fired, natural draft

≥ 300,000 Btu/h and

≤ 2,500,000 Btu/h d

77% Et

DOE 10 CFR Part 431

>  2,500,000 Btu/h e

77% Et

DOE 10 CFR Part 431

Oil-Fired

< 300,000 Btu/h

82% AFUE

DOE 10 CFR Part 430

≥ 300,000 Btu/h and

≤ 2,500,000 Btu/h d

81% Et

DOE 10 CFR Part 431

> 2,500,000 Btu/h e

81% Et

DOE 10 CFR Part 431

a  Applicable test procedure and reference year are provided under the definitions.

Ec = combustion efficiency (100% less flue losses) .See reference document for detailed information.

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).