Copyright

Preface

Effective Use of the International Residential Code

Legislation

Chapter 1 Scope and Administration

Chapter 2 Definitions

Chapter 3 Building Planning

Chapter 4 Foundations

Chapter 5 Floors

Chapter 6 Wall Construction

Chapter 7 Wall Covering

Chapter 8 Roof-Ceiling Construction

Chapter 9 Roof Assemblies

Chapter 10 Chimneys and Fireplaces

Chapter 11 [Re] Energy Efficiency

Chapter 12 Mechanical Administration

Chapter 13 General Mechanical System Requirements

Chapter 14 Heating and Cooling Equipment and Appliances

Chapter 15 Exhaust Systems

Chapter 16 Duct Systems

Chapter 17 Combustion Air

Chapter 18 Chimneys and Vents

Chapter 19 Special Appliances, Equipment and Systems

Chapter 20 Boilers and Water Heaters

Chapter 21 Hydronic Piping

Chapter 22 Special Piping and Storage Systems

Chapter 23 Solar Thermal Energy Systems

Chapter 24 Fuel Gas

Chapter 25 Plumbing Administration

Chapter 26 General Plumbing Requirements

Chapter 27 Plumbing Fixtures

Chapter 28 Water Heaters

Chapter 29 Water Supply and Distribution

Chapter 30 Sanitary Drainage

Chapter 31 Vents

Chapter 32 Traps

Chapter 33 Storm Drainage

Chapter 34 General Requirements

Chapter 35 Electrical Definitions

Chapter 36 Services

Chapter 37 Branch Circuit and Feeder Requirements

Chapter 38 Wiring Methods

Chapter 39 Power and Lighting Distribution

Chapter 40 Devices and Luminaires

Chapter 41 Appliance Installation

Chapter 42 Swimming Pools

Chapter 43 Class 2 Remote-Control, Signaling and Power-Limited Circuits

Chapter 44 Referenced Standards

Appendix A Sizing and Capacities of Gas Piping

Appendix B Sizing of Venting Systems Serving Appliances Equipped With Draft Hoods, Category I Appliances, and Appliances Listed for Use With Type B Vents

Appendix C Exit Terminals of Mechanical Draft and Direct-Vent Venting Systems

Appendix D Recommended Procedure for Safety Inspection of an Existing Appliance Installation

Appendix E Manufactured Housing Used as Dwellings

Appendix F Passive Radon Gas Controls

Appendix G Piping Standards for Various Applications

Appendix H Patio Covers

Appendix I Private Sewage Disposal

Appendix J Existing Buildings and Structures

Appendix K Sound Transmission

Appendix L Permit Fees

Appendix M HOME DAY CARE—R-3 OCCUPANCY

Appendix N Venting Methods

Appendix O Automatic Vehicular Gates

Appendix P Sizing of Water Piping System

Appendix Q Reserved

Appendix R Light Straw-Clay Construction

Appendix S Strawbale Construction

Appendix T Recommended Procedure for Worst-Case Testing of Atmospheric Venting Systems Under N1102.4 or N1105 Conditions

Appendix U SOLAR-READY PROVISIONS—DETACHED ONE- AND TWO-FAMILY DWELLINGS, MULTIPLE SINGLE- FAMILY DWELLINGS (TOWNHOUSES)

(The provisions contained in this appendix are not mandatory unless specifically referenced in the adopting ordinance.)
This appendix outlines two procedures for sizing a water piping system (see Sections AP103.3 and AP201.1). The design procedures are based on the minimum static pressure available from the supply source, the head changes in the system caused by friction and elevation, and the rates of flow necessary for operation of various fixtures.
Because of the variable conditions encountered in hydraulic design, it is impractical to specify definite and detailed rules for sizing of the water piping system. Accordingly, other sizing or design methods conforming to good engineering practice standards are acceptable alternatives to those presented herein.
Obtain the necessary information regarding the minimum daily static service pressure in the area where the building is to be located. If the building supply is to be metered, obtain information regarding friction loss relative to the rate of flow for meters in the range of sizes likely to be used. Friction loss data can be obtained from most manufacturers of water meters.
Estimate the supply demand of the building main and the principal branches and risers of the system by totaling the corresponding demand from the applicable part of Table AP103.3(3).
Estimate continuous supply demands, in gallons per minute (gpm) (L/m), for lawn sprinklers, air conditioners, etc., and add the sum to the total demand for fixtures. The result is the estimated supply demand for the building supply.
Decide from Table P2903.1 what is the desirable minimum residual pressure that should be maintained at the highest fixture in the supply system. If the highest group of fixtures contains flushometer valves, the pressure for the group should be not less than 15 pounds per square inch (psi) (103.4 kPa) flowing. For flush tank supplies, the available pressure should be not less than 8 psi (55.2 kPa) flowing, except blowout action fixtures must not be less than 25 psi (172.4 kPa) flowing.
Pipe sizes can be selected using the following procedure or by use of other design methods conforming to acceptable engineering practice that are approved by the building official. The sizes selected must not be less than the minimum required by this code.
Water pipe sizing procedures are based on a system of pressure requirements and losses, the sum of which must not exceed the minimum pressure available at the supply source. These pressures are as follows:

1. Pressure required at fixture to produce required flow. See Sections P2903.1 of this code and Section 604.3 of the International Plumbing Code.

2. Static pressure loss or gain (due to head) is computed at 0.433 psi per foot (9.8 kPa/m) of elevation change.

Example: Assume that the highest fixture supply outlet is 20 feet (6096 mm) above or below the supply source. This produces a static pressure differential of 8.66 psi (59.8 kPa) loss [20 feet by 0.433 psi per foot (2096 mm by 9.8 kPa/m)].

3. Loss through water meter. The friction or pressure loss can be obtained from meter manufacturers.

4. Loss through taps in water main.

5. Loss through special devices, such as filters, softeners, backflow prevention devices and pressure regulators. These values must be obtained from the manufacturer.

6. Loss through valves and fittings. Losses for these items are calculated by converting to the equivalent length of piping and adding to the total pipe length.

7. Loss caused by pipe friction can be calculated where the pipe size, pipe length and flow through the pipe are known. With these three items, the friction loss can be determined. For piping flow charts not included, use manufacturers’ tables and velocity recommendations.

Note: For all examples, the following metric conversions are applicable.

1 cubic foot per minute = 0.4719 L/s.

1 square foot = 0.0929 m2.

1 degree = 0.0175 rad.

1 pound per square inch = 6.895 kPa.

1 inch = 25.4 mm.

1 foot = 304.8 mm.

1 gallon per minute = 3.785 L/m.
The size of water service mains, branch mains and risers by the segmented loss method, must be determined by knowing the water supply demand [gpm (L/m)], available water pressure [psi (kPa)] and friction loss caused by the water meter and developed length of pipe [feet (m)], including the equivalent length of fittings. This design procedure is based on the following parameters:

1. The calculated friction loss through each length of pipe.

2. A system of pressure losses, the sum of which must not exceed the minimum pressure available at the street main or other source of supply.

3. Pipe sizing based on estimated peak demand, total pressure losses caused by difference in elevation, equipment, developed length and pressure required at the most remote fixture; loss through taps in water main; losses through fittings, filters, backflow prevention devices, valves and pipe friction.

Because of the variable conditions encountered in hydraulic design, it is impractical to specify definite and detailed rules for the sizing of the water piping system. Current sizing methods do not address the differences in the probability of use and flow characteristics of fixtures between types of occupancies. Creating an exact model of predicting the demand for a building is impossible and final studies assessing the impact of water conservation on demand are not yet complete. The following steps are necessary for the segmented loss method.

1. Preliminary. Obtain the necessary information regarding the minimum daily static service pressure in the area where the building is to be located. If the building supply is to be metered, obtain information regarding friction loss relative to the rate of flow for meters in the range of sizes to be used. Friction loss data can be obtained from manufacturers of water meters. Enough pressure must be available to overcome all system losses caused by friction and elevation so that plumbing fixtures operate properly. Section 604.6 of the International Plumbing Code requires that the water distribution system be designed for the minimum pressure available taking into consideration pressure fluctuations. The lowest pressure must be selected to guarantee a continuous, adequate supply of water. The lowest pressure in the public main usually occurs in the summer because of lawn sprinkling and supplying water for air-conditioning cooling towers. Future demands placed on the public main as a result of large growth or expansion should be considered. The available pressure will decrease as additional loads are placed on the public system.

2. Demand load. Estimate the supply demand of the building main and the principal branches and risers of the system by totaling the corresponding demand from the applicable part of Table AP103.3(3). When estimating peak demand, sizing methods typically use water supply fixture units (w.s.f.u.) [see Table AP103.3(2)]. This numerical factor measures the load-producing effect of a single plumbing fixture of a given kind. The use of fixture units can be applied to a single basic probability curve (or table), found in the various sizing methods [see Table AP103.3(3)]. The fixture units are then converted into a gpm (L/m) flow rate for estimating demand.

2.1. Estimate continuous supply demand in gpm (L/m) for lawn sprinklers, air conditioners, etc., and add the sum to the total demand for fixtures. The result is the estimated supply demand for the building supply. Fixture units cannot be applied to constant-use fixtures, such as hose bibbs, lawn sprinklers and air conditioners. These types of fixtures must be assigned the gpm (L/m) value.

3. Selection of pipe size. This water pipe sizing procedure is based on a system of pressure requirements and losses, the sum of which must not exceed the minimum pressure available at the supply source. These pressures are as follows:

3.1. Pressure required at the fixture to produce required flow. See Section P2903.1 of this code and Section 604.3 of the International Plumbing Code.

3.2. Static pressure loss or gain (because of head) is computed at 0.433 psi per foot (9.8 kPa/m) of elevation change.

3.3. Loss through a water meter. The friction or pressure loss can be obtained from the manufacturer.

3.4. Loss through taps in water main [see Table AP103.3(4)].

3.5. Loss through special devices, such as filters, softeners, backflow prevention devices and pressure regulators. These values must be obtained from the manufacturers.

3.6. Loss through valves and fittings [see Tables AP103.3(5) and AP103.3(6)]. Losses for these items are calculated by converting to the equivalent length of piping and adding to the total pipe length.

3.7. Loss caused by pipe friction can be calculated where the pipe size, pipe length and flow through the pipe are known. With these three items, the friction loss can be determined using Figures AP103.3(2) through AP103.3(7). Where using charts, use pipe inside diameters. For piping flow charts not included, use manufacturers’ tables and velocity recommendations. Before attempting to size any water supply system, it is necessary to gather preliminary information including available pressure, piping material, select design velocity, elevation differences and developed length to the most remote fixture. The water supply system is divided into sections at major changes in elevation or where branches lead to fixture groups. The peak demand must be determined in each part of the hot and cold water supply system. The expected flow through each section is determined in w.s.f.u. and converted to gpm (L/m) flow rate. Sizing methods require determination of the "most hydraulically remote" fixture to compute the pressure loss caused by pipe and fittings. The hydraulically remote fixture represents the most downstream fixture along the circuit of piping requiring the most available pressure to operate properly. Consideration must be given to all pressure demands and losses, such as friction caused by pipe, fittings and equipment; elevation; and the residual pressure required by Table P2903.1. The two most common and frequent complaints about water supply system operation are lack of adequate pressure and noise.

Problem: What size Type L copper water pipe, service and distribution will be required to serve a two-story factory building having on each floor, back-to-back, two toilet rooms each equipped with hot and cold water? The highest fixture is 21 feet above the street main, which is tapped with a 2-inch corporation cock at which point the minimum pressure is 55 psi. In the building basement, a 2-inch meter with a maximum pressure drop of 11 psi and 3-inch reduced pressure principle backflow preventer with a maximum pressure drop of 9 psi are to be installed. The system is shown in Figure AP103.3(1). To be determined are the pipe sizes for the service main, and the cold and hot water distribution pipes.

Solution: A tabular arrangement such as shown in Table AP103.3(1) should first be constructed. The steps to be followed are indicated by the tabular arrangement itself as they are in sequence, Columns 1 through 10 and Lines A through L.

Step 1

Columns 1 and 2: Divide the system into sections breaking at major changes in elevation or where branches lead to fixture groups. After Point B [see Figure AP103.3(1)], separate consideration will be given to the hot and cold water piping. Enter the sections to be considered in the service and cold water piping in Column 1 of the tabular arrangement. Column 1 of Table AP103.3(1) provides a line-by-line, recommended tabular arrangement for use in solving pipe sizing.

The objective in designing the water supply system is to ensure an adequate water supply and pressure to all fixtures and equipment. Column 2 provides the psi (kPa) to be considered separately from the minimum pressure available at the main. Losses to take into consideration are the following: the differences in elevations between the water supply source and the highest water supply outlet; meter pressure losses; the tap in main loss; special fixture devices, such as water softeners and backflow prevention devices; and the pressure required at the most remote fixture outlet.

The difference in elevation can result in an increase or decrease in available pressure at the main. Where the water supply outlet is located above the source, this results in a loss in the available pressure and is subtracted from the pressure at the water source. Where the highest water supply outlet is located below the water supply source, there will be an increase in pressure that is added to the available pressure of the water source.

Column 3: Using Table AP103.3(3), determine the gpm (L/m) of flow to be expected in each section of the system. These flows range from 28.6 to 108 gpm. Load values for fixtures must be determined as w.s.f.u. and then converted to a gpm rating to determine peak demand. Where calculating peak demands, the w.s.f.u. are added and then converted to the gpm rating. For continuous flow fixtures, such as hose bibbs and lawn sprinkler systems, add the gpm demand to the intermittent demand of fixtures. For example, a total of 120 w.s.f.u. is converted to a demand of 48 gpm. Two hose bibbs × 5 gpm demand = 10 gpm. Total gpm rating = 48.0 gpm + 10 gpm = 58.0 gpm demand.

Step 2

Line A: Enter the minimum pressure available at the main source of supply in Column 2. This is 55 psi (379.2 kPa). The local water authorities generally keep records of pressures at different times of the day and year. The available pressure can also be checked from nearby buildings or from fire department hydrant checks.

Line B: Determine from Table P2903.1 the highest pressure required for the fixtures on the system, which is 15 psi (103.4 kPa), to operate a flushometer valve. The most remote fixture outlet is necessary to compute the pressure loss caused by pipe and fittings, and represents the most downstream fixture along the circuit of piping requiring the available pressure to operate properly as indicated by Table P2903.1.

Line C: Determine the pressure loss for the meter size given or assumed. The total water flow from the main through the service as determined in Step 1 will serve to aid in the meter selected. There are three common types of water meters; the pressure losses are determined by the American Water Works Association Standards for displacement type, compound type and turbine type. The maximum pressure loss of such devices takes into consideration the meter size, safe operating capacity [gpm (L/m)] and maximum rates for continuous operations [gpm (L/m)]. Typically, equipment imparts greater pressure losses than piping.

Line D: Select from Table AP103.3(4) and enter the pressure loss for the tap size given or assumed. The loss of pressure through taps and tees in psi (kPa) is based on the total gpm (L/m) flow rate and size of the tap.

Line E: Determine the difference in elevation between the main and source of supply and the highest fixture on the system. Multiply this figure, expressed in feet (mm), by 0.43 psi. Enter the resulting psi (kPa) loss on Line E. The difference in elevation between the water supply source and the highest water supply outlet has a significant impact on the sizing of the water supply system. The difference in elevation usually results in a loss in the available pressure because the water supply outlet is generally located above the water supply source. The loss is caused by the pressure required to lift the water to the outlet. The pressure loss is subtracted from the pressure at the water source. Where the highest water supply outlet is located below the water source, there will be an increase in pressure that is added to the available pressure of the water source.

Lines F, G and H: The pressure losses through filters, backflow prevention devices or other special fixtures must be obtained from the manufacturer or estimated and entered on these lines. Equipment, such as backflow prevention devices, check valves, water softeners, instantaneous, or tankless water heaters, filters and strainers, can impart a much greater pressure loss than the piping. The pressure losses can range from 8 to 30 psi.

Step 3

Line I: The sum of the pressure requirements and losses that affect the overall system (Lines B through H) is entered on this line. Summarizing the steps, all of the system losses are subtracted from the minimum water pressure. The remainder is the pressure available for friction, defined as the energy available to push the water through the pipes to each fixture. This force can be used as an average pressure loss, as long as the pressure available for friction is not exceeded. Saving a certain amount for available water supply pressures as an area incurs growth, or because of the aging of the pipe or equipment added to the system is recommended.

Step 4

Line J: Subtract Line I from Line A. This gives the pressure that remains available from overcoming friction losses in the system. This figure is a guide to the pipe size that is chosen for each section, incorporating the total friction losses to the most remote outlet (measured length is called developed length).

Exception: Where the main is above the highest fixture, the resulting psi (kPa) must be considered a pressure gain (static head gain) and omitted from the sums of Lines B through H and added to Line J.

The maximum friction head loss that can be tolerated in the system during peak demand is the difference between the static pressure at the highest and most remote outlet at no-flow conditions and the minimum flow pressure required at that outlet. If the losses are within the required limits, every run of pipe will be within the required friction head loss. Static pressure loss is at the most remote outlet in feet × 0.433 = loss in psi caused by elevation differences.

Step 5

Column 4: Enter the length of each section from the main to the most remote outlet (at Point E). Divide the water supply system into sections breaking at major changes in elevation or where branches lead to fixture groups.

Step 6

Column 5: Where selecting a trial pipe size, the length from the water service or meter to the most remote fixture outlet must be measured to determine the developed length. However, in systems having a flushometer valve or temperature-controlled shower at the topmost floors, the developed length would be from the water meter to the most remote flushometer valve on the system. A rule of thumb is that size will become progressively smaller as the system extends farther from the main source of supply. A trial pipe size can be arrived at by the following formula:

Line J: (Pressure available to overcome pipe friction) × 100/equivalent length of run total developed length to most remote fixture × percentage factor of 1.5 (Note: a percentage factor is used only as an estimate for friction losses imposed for fittings for initial trial pipe size) = psi (average pressure drop per 100 feet of pipe).

For trial pipe size, see Figure AP103.3(3) (Type L copper) based on 2.77 psi and 108 gpm = 21/2 inches. To determine the equivalent length of run to the most remote outlet, the developed length is determined and added to the friction losses for fittings and valves. The developed lengths of the designated pipe sections are as follows:

A-B 54 feet
B-C 8 feet
C-D 13 feet
D-E 150 feet
Total developed length = 225 feet


The equivalent length of the friction loss in fittings and valves must be added to the developed length (most remote outlet). Where the size of fittings and valves is not known, the added friction loss should be approximated. A general rule that has been used is to add 50 percent of the developed length to allow for fittings and valves. For example, the equivalent length of run equals the developed length of run (225 feet × 1.5 = 338 feet). The total equivalent length of run for determining a trial pipe size is 338 feet.

Example: 9.36 (pressure available to overcome pipe friction) × 100/338 (equivalent length of run = 225 × 1.5) = 2.77 psi (average pressure drop per 100 feet of pipe).

Step 7

Column 6: Select from Table AP103.3(6) the equivalent lengths for the trial pipe size of fittings and valves on each pipe section. Enter the sum for each section in Column 6. (The number of fittings to be used in this example must be an estimate). The equivalent length of piping is the developed length plus the equivalent lengths of pipe corresponding to the friction head losses for fittings and valves. Where the size of fittings and valves is not known, the added friction head losses must be approximated. An estimate for this example is found in Table AP.1.

Step 8

Column 7: Add the figures from Columns 4 and 6, and enter in Column 7. Express the sum in hundreds of feet.

Step 9

Column 8: Select from Figure AP103.3(3) the friction loss per 100 feet of pipe for the gpm flow in a section (Column 3) and trial pipe size (Column 5). Maximum friction head loss per 100 feet is determined on the basis of the total pressure available for friction head loss and the longest equivalent length of run. The selection is based on the gpm demand, uniform friction head loss and maximum design velocity. Where the size indicated by the hydraulic table indicates a velocity in excess of the selected velocity, a size must be selected that produces the required velocity.

Step 10

Column 9: Multiply the figures in Columns 7 and 8 for each section and enter in Column 9.

Total friction loss is determined by multiplying the friction loss per 100 feet for each pipe section in the total developed length by the pressure loss in fittings expressed as equivalent length in feet (mm). Note: Section C-F should be considered in the total pipe friction losses only if greater loss occurs in Section C-F than in pipe Section D-E. Section C-F is not considered in the total developed length. Total friction loss in equivalent length is determined in Table AP.2.

Step 11

Line K: Enter the sum of the values in Column 9. The value is the total friction loss in equivalent length for each designated pipe section.

Step 12

Line L: Subtract Line J from Line K and enter in Column 10.

The result should always be a positive or plus figure. If it is not, repeat the operation using Columns 5, 6, 8 and 9 until a balance or near balance is obtained. If the difference between Lines J and K is a high positive number, it is an indication that the pipe sizes are too large and should be reduced, thus saving materials. In such a case, the operations using Columns 5, 6, 8 and 9 should be repeated.

The total friction losses are determined and subtracted from the pressure available to overcome pipe friction for the trial pipe size. This number is critical because it provides a guide to whether the pipe size selected is too large and the process should be repeated to obtain an economically designed system.

Answer: The final figures entered in Column 5 become the design pipe size for the respective sections. Repeating this operation a second time using the same sketch but considering the demand for hot water, it is possible to size the hot water distribution piping. This has been worked up as a part of the overall problem in the tabular arrangement used for sizing the service and water distribution piping. Note that consideration must be given to the pressure losses from the street main to the water heater (Section A-B) in determining the hot water pipe sizes.


For SI: 1 foot = 304.8 mm, 1 gallon per minute = 3.785 L/m.


FIGURE AP103.3(1) EXAMPLE‒SIZING


Note: Fluid velocities in excess of 5 to 8 feet per second are not usually recommended.
For SI: 1 inch = 25.4 mm, 1 foot = 304.8 mm, 1 gallon per minute = 3.785 L/m, 1 pound per square inch = 6.895 kPa, 1 foot per second = 0.305 m/s.
a. This figure applies to smooth new copper tubing with recessed (streamline) soldered joints and to the actual sizes of types indicated on the diagram.


FIGURE AP103.3(2) FRICTION LOSS IN SMOOTH PIPEa (TYPE K, ASTM B 88 COPPER TUBING)


Note: Fluid velocities in excess of 5 to 8 feet per second are not usually recommended.
For SI: 1 inch = 25.4 mm, 1 foot = 304.8 mm, 1 gallon per minute = 3.785 L/m, 1 pound per square inch = 6.895 kPa, 1 foot per second = 0.305 m/s.
a. This figure applies to smooth new copper tubing with recessed (streamline) soldered joints and to the actual sizes of types indicated on the diagram.


FIGURE AP103.3(3) FRICTION LOSS IN SMOOTH PIPEa (TYPE L, ASTM B 88 COPPER TUBING)


Note: Fluid velocities in excess of 5 to 8 feet per second are not usually recommended.
For SI: 1 inch = 25.4 mm, 1 foot = 304.8 mm, 1 gallon per minute = 3.785 L/m, 1 pound per square inch = 6.895 kPa, 1 foot per second = 0.305 m/s.
a. This figure applies to smooth new copper tubing with recessed (streamline) soldered joints and to the actual sizes of types indicated on the diagram.


FIGURE AP103.3(4) FRICTION LOSS IN SMOOTH PIPEa (TYPE M, ASTM B 88 COPPER TUBING)


For SI: 1 inch = 25.4 mm, 1 foot = 304.8 mm, 1 gallon per minute = 3.785 L/m, 1 pound per square inch = 6.895 kPa, 1 foot per second = 0.305 m/s.
a. This figure applies to smooth new steel (fairly smooth) pipe and to actual diameters of standard-weight pipe.


FIGURE AP103.3(5) FRICTION LOSS IN FAIRLY SMOOTH PIPEa


For SI: 1 inch = 25.4 mm, 1 foot = 304.8 mm, 1 gallon per minute = 3.785 L/m, 1 pound per square inch = 6.895 kPa, 1 foot per second = 0.305 m/s.
a. This figure applies to fairly rough pipe and to actual diameters which, in general, will be less than the actual diameters of the new pipe of the same kind.


FIGURE AP103.3(6) FRICTION LOSS IN FAIRLY ROUGH PIPEa


For SI: 1 inch = 25.4 mm, 1 foot = 304.8 mm, 1 gallon per minute = 3.785 L/m, 1 pound per square inch = 6.895 kPa, 1 foot per second = 0.305 m/s.
a. This figure applies to very rough pipe and existing pipe, and to their actual diameters.


FIGURE AP103.3(7) FRICTION LOSS IN ROUGH PIPEa

TABLE AP103.3(1) RECOMMENDED TABULAR ARRANGEMENT FOR USE IN SOLVING PIPE SIZING PROBLEMS

COLUMN 1 2 3 4 5 6 7 8 9 10
Line Description Pounds
per
square
inch
Gallons
per min
through
section
Length of
section
(feet)
Trial
pipe
size
(inches)
Equivalent
length of
fittings and
valves (feet)
Total
equivalent
length
[(Col. 4 +
Col. 6)/100
feet)]
Friction
loss per
100 feet of
trial size
pipe (psi)
Friction
loss in
equivalent
length
Column 8 x
Column 7
(psi)
Excess
pressure
over
friction
losses (psi)
A Service and cold
water distribution
pipinga
Minimum pressure available at main 55.00
B Highest pressure required at a fixture
(see Table P2903.1)
15.00
C Meter loss 2″ meter 11.00
D Tap in main loss 2″ tap [see Table AP103.3(4)] 1.61
E Static head loss 21 ft × 0.43 psi/ft 9.03
F Special fixture loss backflow preventer 9.00
G Special fixture loss‒Filter 0.00
H Special fixture loss‒Other 0.00
I Total overall losses and requirements
(Sum of Lines B through H)
45.64
J Pressure available to overcome pipe friction
(Line A minus Line I)
9.36
Pipe section (from diagram)
cold water distribution piping
A-B 288 108.0 54 21/2 15.00 0.69 3.2 2.21
B-C 264 104.5 8 21/2 0.5 0.085 3.1 0.26
C-D 132 77.0 13 21/2 7.00 0.20 1.9 0.38
C-Fb 132 77.0 150 21/2 12.00 1.62 1.9 3.08
D-Eb 132 77.0 150 21/2 12.00 1.62 1.9 3.08
K Total pipe friction losses (cold) 5.93
L Difference (Line J minus Line K) 3.43
Pipe section (from diagram)
Hot water Distribution Piping
A′B′ 288 108.0 54 21/2 12.00 0.69 3.3 2.21
B′C′ 24 38.0 8 2 7.5 0.16 1.4 0.22
C′D′ 12 28.6 13 11/2 4.0 0.17 3.2 0.54
C′F′b 12 28.6 150 11/2 7.00 1.57 3.2 5.02
D′E′b 12 28.6 150 11/2 7.00 1.57 3.2 5.02
K Total pipe friction losses (hot) 7.99
L Difference (Line J minus Line K) 1.37

For SI: 1 inch = 25.4 mm, 1 foot = 304.8 mm, 1 pound per square inch = 6.895 kPa, 1 gallon per minute = 3.785 L/m.
a. To be considered as pressure gain for fixtures below main (to consider separately, omit from "I" and add to "J").
b. To consider separately, in Line K use Section C-F only if greater loss than the loss in Section D-E.


TABLE AP103.3(2) LOAD VALUES ASSIGNED TO FIXTURESa

FIXTURE OCCUPANCY TYPE OF SUPPLY
CONTROL
LOAD VALUES, IN WATER SUPPLY FIXTURE UNITS (w.s.f.u.)
Cold Hot Total
Bathroom group Private Flush tank 2.7 1.5 3.6
Bathroom group Private Flushometer valve 6.0 3.0 8.0
Bathtub Private Faucet 1.0 1.0 1.4
Bathtub Public Faucet 3.0 3.0 4.0
Bidet Private Faucet 1.5 1.5 2.0
Combination fixture Private Faucet 2.25 2.25 3.0
Dishwashing machine Private Automatic 1.4 1.4
Drinking fountain Offices, etc. 3/8″ valve 0.25 0.25
Kitchen sink Private Faucet 1.0 1.0 1.4
Kitchen sink Hotel, restaurant Faucet 3.0 3.0 4.0
Laundry trays (1 to 3) Private Faucet 1.0 1.0 1.4
Lavatory Private Faucet 0.5 0.5 0.7
Lavatory Public Faucet 1.5 1.5 2.0
Service sink Offices, etc. Faucet 2.25 2.25 3.0
Shower head Public Mixing valve 3.0 3.0 4.0
Shower head Private Mixing valve 1.0 1.0 1.4
Urinal Public 1″ flushometer valve 10.0 10.0
Urinal Public 3/4″ flushometer valve 5.0 5.0
Urinal Public Flush tank 3.0 3.0
Washing machine (8 lb) Private Automatic 1.0 1.0 1.4
Washing machine (8 lb) Public Automatic 2.25 2.25 3.0
Washing machine (15 lb) Public Automatic 3.0 3.0 4.0
Water closet Private Flushometer valve 6.0 6.0
Water closet Private Flush tank 2.2 2.2
Water closet Public Flushometer valve 10.0 10.0
Water closet Public Flush tank 5.0 5.0
Water closet Public or private Flushometer tank 2.0 2.0

For SI: 1 inch = 25.4 mm, 1 pound = 0.454 kg.
a. For fixtures not listed, loads should be assumed by comparing the fixture to one listed using water in similar quantities and at similar rates. The assigned loads for fixtures with both hot and cold water supplies are given for separate hot and cold water loads, and for total load. The separate hot and cold water loads are three-fourths of the total load for the fixture in each case.


TABLE AP103.3(3) TABLE FOR ESTIMATING DEMAND

SUPPLY SYSTEMS PREDOMINANTLY FOR FLUSH TANKS SUPPLY SYSTEMS PREDOMINANTLY FOR FLUSHOMETERS
Load Demand Load Demand
(w.s.f.u.) (gpm) (cfm) (w.s.f.u.) (gpm) (cfm)
1 3.0 0.04104
2 5.0 0.0684
3 6.5 0.86892
4 8.0 1.06944
5 9.4 1.256592 5 15.0 2.0052
6 10.7 1.430376 6 17.4 2.326032
7 11.8 1.577424 7 19.8 2.646364
8 12.8 1.711104 8 22.2 2.967696
9 13.7 1.831416 9 24.6 3.288528
10 14.6 1.951728 10 27.0 3.60936
11 15.4 2.058672 11 27.8 3.716304
12 16.0 2.13888 12 28.6 3.823248
13 16.5 2.20572 13 29.4 3.930192
14 17.0 2.27256 14 30.2 4.037136
15 17.5 2.3394 15 31.0 4.14408
16 18.0 2.90624 16 31.8 4.241024
17 18.4 2.459712 17 32.6 4.357968
18 18.8 2.513184 18 33.4 4.464912
19 19.2 2.566656 19 34.2 4.571856
20 19.6 2.620128 20 35.0 4.6788
25 21.5 2.87412 25 38.0 5.07984
30 23.3 3.114744 30 42.0 5.61356
35 24.9 3.328632 35 44.0 5.88192
40 26.3 3.515784 40 46.0 6.14928
45 27.7 3.702936 45 48.0 6.41664
50 29.1 3.890088 50 50.0 6.684
60 32.0 4.27776 60 54.0 7.21872
70 35.0 4.6788 70 58.0 7.75344
80 38.0 5.07984 80 61.2 8.181216
90 41.0 5.48088 90 64.3 8.595624
100 43.5 5.81508 100 67.5 9.0234
120 48.0 6.41664 120 73.0 9.75864
140 52.5 7.0182 140 77.0 10.29336
160 57.0 7.61976 160 81.0 10.82808
180 61.0 8.15448 180 85.5 11.42964
200 65.0 8.6892 200 90.0 12.0312
225 70.0 9.3576 225 95.5 12.76644


(continued)

TABLE AP103.3(3)‒continued TABLE FOR ESTIMATING DEMAND

SUPPLY SYSTEMS PREDOMINANTLY FOR FLUSH TANKS SUPPLY SYSTEMS PREDOMINANTLY FOR FLUSHOMETERS
Load Demand Load Demand
(w.s.f.u.) (gpm) (cfm) (w.s.f.u.) (gpm) (cfm)
250 75.0 10.026 250 101.0 13.50168
275 80.0 10.6944 275 104.5 13.96956
300 85.0 11.3628 300 108.0 14.43744
400 105.0 14.0364 400 127.0 16.97736
500 124.0 16.57632 500 143.0 19.11624
750 170.0 22.7256 750 177.0 23.66136
1,000 208.0 27.80544 1,000 208.0 27.80544
1,250 239.0 31.94952 1,250 239.0 31.94952
1,500 269.0 35.95992 1,500 269.0 35.95992
1,750 297.0 39.70296 1,750 297.0 39.70296
2,000 325.0 43.446 2,000 325.0 43.446
2,500 380.0 50.7984 2,500 380.0 50.7984
3,000 433.0 57.88344 3,000 433.0 57.88344
4,000 535.0 70.182 4,000 525.0 70.182
5,000 593.0 79.27224 5,000 593.0 79.27224

For SI: 1 gallon per minute = 3.785 L/m, 1 cubic foot per minute = 0.000471 m3/s.


TABLE AP103.3(4) LOSS OF PRESSURE THROUGH TAPS AND TEES IN POUNDS PER SQUARE INCH (psi)

GALLONS PER MINUTE SIZE OF TAP OR TEE (inches)
5/8 3/4 1 11/4 11/2 2 3
10 1.35 0.64 0.18 0.08
20 5.38 2.54 0.77 0.31 0.14
30 12.10 5.72 1.62 0.69 0.33 0.10
40 10.20 3.07 1.23 0.58 0.18
50 15.90 4.49 1.92 0.91 0.28
60 6.46 2.76 1.31 0.40
70 8.79 3.76 1.78 0.55 0.10
80 11.50 4.90 2.32 0.72 0.13
90 14.50 6.21 2.94 0.91 0.16
100 17.94 7.67 3.63 1.12 0.21
120 25.80 11.00 5.23 1.61 0.30
140 35.20 15.00 7.12 2.20 0.41
150 17.20 8.16 2.52 0.47
160 19.60 9.30 2.92 0.54
180 24.80 11.80 3.62 0.68
200 30.70 14.50 4.48 0.84
225 38.80 18.40 5.60 1.06
250 47.90 22.70 7.00 1.31
275 27.40 7.70 1.59
300 32.60 10.10 1.88

For SI: 1 inch = 25.4 mm, 1 pound per square inch = 6.895 kPa, 1 gallon per minute = 3.785 L/m.


TABLE AP103.3(5) ALLOWANCE IN EQUIVALENT LENGTHS OF PIPE FOR FRICTION LOSS IN VALVES AND THREADED FITTINGS (feet)

FITTING OR VALVE PIPE SIZE (inches)
1/2 3/4 1 11/4 11/2 2 21/2 3
45-degree elbow 1.2 1.5 1.8 2.4 3.0 4.0 5.0 6.0
90-degree elbow 2.0 2.5 3.0 4.0 5.0 7.0 8.0 10.0
Tee, run 0.6 0.8 0.9 1.2 1.5 2.0 2.5 3.0
Tee, branch 3.0 4.0 5.0 6.0 7.0 10.0 12.0 15.0
Gate valve 0.4 0.5 0.6 0.8 1.0 1.3 1.6 2.0
Balancing valve 0.8 1.1 1.5 1.9 2.2 3.0 3.7 4.5
Plug-type cock 0.8 1.1 1.5 1.9 2.2 3.0 3.7 4.5
Check valve, swing 5.6 8.4 11.2 14.0 16.8 22.4 28.0 33.6
Globe valve 15.0 20.0 25.0 35.0 45.0 55.0 65.0 80.0
Angle valve 8.0 12.0 15.0 18.0 22.0 28.0 34.0 40.0

For SI: 1 inch = 25.4 mm, 1 foot = 304.8 mm, 1 degree = 0.0175 rad.


TABLE AP103.3(6) PRESSURE LOSS IN FITTINGS AND VALVES EXPRESSED AS EQUIVALENT LENGTH OF TUBEa (feet)

NOMINAL OR
STANDARD
SIZE (inches)
FITTINGS Coupling VALVES
Standard EII 90-degree Tee Ball Gate Butterfly Check
90 Degree 45 Degree Side Branch Straight Run
3/8 0.5 1.5 1.5
1/2 1 0.5 2 2
5/8 1.5 0.5 2 2.5
3/4 2 0.5 3 3
1 2.5 1 4.5 0.5 4.5
11/4 3 1 5.5 0.5 0.5 0.5 5.5
11/2 4 1.5 7 0.5 0.5 0.5 6.5
2 5.5 2 9 0.5 0.5 0.5 0.5 7.5 9
21/2 7 2.5 12 0.5 0.5 1 10 11.5
3 9 3.5 15 1 1 1.5 15.5 14.5
31/2 9 3.5 14 1 1 2 12.5
4 12.5 5 21 1 1 2 16 18.5
5 16 6 27 1.5 1.5 3 11.5 23.5
6 19 7 34 2 2 3.5 13.5 26.5
8 29 11 50 3 3 5 12.5 39

For SI: 1 inch = 25.4 mm, 1 foot = 304.8 mm, 1 degree = 0.01745 rad.
a. Allowances are for streamlined soldered fittings and recessed threaded fittings. For threaded fittings, double the allowances shown in the table. The equivalent lengths presented in the table are based on a C factor of 150 in the Hazen-Williams friction loss formula. The lengths shown are rounded to the nearest half-foot.
The minimum size water service pipe shall be 3/4 inch (19.1 mm). The size of water service mains, branch mains and risers shall be determined according to water supply demand [gpm (L/m)], available water pressure [psi (kPa)] and friction loss caused by the water meter and developed length of pipe [feet (m)], including the equivalent length of fittings. The size of each water distribution system shall be determined according to the procedure outlined in this section or by other design methods conforming to acceptable engineering practice and approved by the building official:

1. Supply load in the building water distribution system shall be determined by the total load on the pipe being sized, in terms of w.s.f.u., as shown in Table AP103.3(2). For fixtures not listed, choose a w.s.f.u. value of a fixture with similar flow characteristics.

2. Obtain the minimum daily static service pressure [psi (kPa)] available (as determined by the local water authority) at the water meter or other source of supply at the installation location. Adjust this minimum daily static pressure [psi (kPa)] for the following conditions:

2.1. Determine the difference in elevation between the source of supply and the highest water supply outlet. Where the highest water supply outlet is located above the source of supply, deduct 0.5 psi (3.4 kPa) for each foot (0.3 m) of difference in elevation. Where the highest water supply outlet is located below the source of supply, add 0.5 psi (3.4 kPa) for each foot (0.3 m) of difference in elevation.

2.2. Where a water pressure-reducing valve is installed in the water distribution system, the minimum daily static water pressure available is 80 percent of the minimum daily static water pressure at the source of supply or the set pressure downstream of the water pressure-reducing valve, whichever is smaller.

2.3. Deduct all pressure losses caused by special equipment, such as a backflow preventer, water filter and water softener. Pressure loss data for each piece of equipment shall be obtained through the manufacturer of the device.

2.4. Deduct the pressure in excess of 8 psi (55 kPa) resulting from the installation of the special plumbing fixture, such as temperature-controlled shower and flushometer tank water closet. Using the resulting minimum available pressure, find the corresponding pressure range in Table AP201.1.

3. The maximum developed length for water piping is the actual length of pipe between the source of supply and the most remote fixture, including either hot (through the water heater) or cold water branches multiplied by a factor of 1.2 to compensate for pressure loss through fittings. Select the appropriate column in Table AP201.1 equal to or greater than the calculated maximum developed length.

4. To determine the size of the water service pipe, meter and main distribution pipe to the building using the appropriate table, follow down the selected "maximum developed length" column to a fixture unit equal to or greater than the total installation demand calculated by using the "combined" w.s.f.u. column of Table AP201.1. Read the water service pipe and meter sizes in the first left-hand column and the main distribution pipe to the building in the second left-hand column on the same row.

5. To determine the size of each water distribution pipe, start at the most remote outlet on each branch (either hot or cold branch) and, working back toward the main distribution pipe to the building, add up the w.s.f.u. demand passing through each segment of the distribution system using the related hot or cold column of Table AP201.1. Knowing demand, the size of each segment shall be read from the second left-hand column of the same table and the maximum developed length column selected in Steps 1 and 2, under the same or next smaller size meter row. In no case does the size of any branch or main need to be larger than the size of the main distribution pipe to the building established in Step 4.

TABLE AP201.1 MINIMUM SIZE OF WATER METERS, MAINS AND DISTRIBUTION PIPING BASED ON WATER SUPPLY FIXTURE UNIT VALUES (w.s.f.u.)

METER AND SERVICE PIPE
(inches)
DISTRIBUTION PIPE
(inches)
MAXIMUM DEVELOPMENT LENGTH (feet)
Pressure Range 30 to 39 psi 40 60 80 100 150 200 250 300 400 500
3/4 1/2a 2.5 2 1.5 1.5 1 1 0.5 0.5 0 0
3/4 3/4 9.5 7.5 6 5.5 4 3.5 3 2.5 2 1.5
3/4 1 32 25 20 16.5 11 9 7.8 6.5 5.5 4.5
1 1 32 32 27 21 13.5 10 8 7 5.5 5
3/4 11/4 32 32 32 32 30 24 20 17 13 10.5
1 11/4 80 80 70 61 45 34 27 22 16 12
11/2 11/4 80 80 80 75 54 40 31 25 17.5 13
1 11/2 87 87 87 87 84 73 64 56 45 36
11/2 11/2 151 151 151 151 117 92 79 69 54 43
2 11/2 151 151 151 151 128 99 83 72 56 45
1 2 87 87 87 87 87 87 87 87 87 86
11/2 2 275 275 275 275 258 223 196 174 144 122
2 2 365 365 365 365 318 266 229 201 160 134
2 21/2 533 533 533 533 533 495 448 409 353 311

METER AND SERVICE PIPE
(inches)
DISTRIBUTION PIPE
(inches)
MAXIMUM DEVELOPMENT LENGTH (feet)
Pressure Range 40 to 49 psi 40 60 80 100 150 200 250 300 400 500
3/4 1/2a 3 2.5 2 1.5 1.5 1 1 0.5 0.5 0.5
3/4 3/4 9.5 9.5 8.5 7 5.5 4.5 3.5 3 2.5 2
3/4 1 32 32 32 26 18 13.5 10.5 9 7.5 6
1 1 32 32 32 32 21 15 11.5 9.5 7.5 6.5
3/4 11/4 32 32 32 32 32 32 32 27 21 16.5
1 11/4 80 80 80 80 65 52 42 35 26 20
11/2 11/4 80 80 80 80 75 59 48 39 28 21
1 11/2 87 87 87 87 87 87 87 78 65 55
11/2 11/2 151 151 151 151 151 130 109 93 75 63
2 11/2 151 151 151 151 151 139 115 98 77 64
1 2 87 87 87 87 87 87 87 87 87 87
11/2 2 275 275 275 275 275 275 264 238 198 169
2 2 365 365 365 365 365 349 304 270 220 185
2 21/2 533 533 533 533 533 533 533 528 456 403


(continued)

TABLE AP201.1‒continued MINIMUM SIZE OF WATER METERS, MAINS AND DISTRIBUTION PIPING BASED ON WATER SUPPLY FIXTURE UNIT VALUES (w.s.f.u.)

METER AND SERVICE PIPE
(inches)
DISTRIBUTION PIPE
(inches)
MAXIMUM DEVELOPMENT LENGTH (feet)
Pressure Range 50 to 60 psi 40 60 80 100 150 200 250 300 400 500
3/4 1/2a 3 3 2.5 2 1.5 1 1 1 0.5 0.5
3/4 3/4 9.5 9.5 9.5 8.5 6.5 5 4.5 4 3 2.5
3/4 1 32 32 32 32 25 18.5 14.5 12 9.5 8
1 1 32 32 32 32 30 22 16.5 13 10 8
3/4 11/4 32 32 32 32 32 32 32 32 29 24
1 11/4 80 80 80 80 80 68 57 48 35 28
11/2 11/4 80 80 80 80 80 75 63 53 39 29
1 11/2 87 87 87 87 87 87 87 87 82 70
11/2 11/2 151 151 151 151 151 151 139 120 94 79
2 11/2 151 151 151 151 151 151 146 126 97 81
1 2 87 87 87 87 87 87 87 87 87 87
11/2 2 275 275 275 275 275 275 275 275 247 213
2 2 365 365 365 365 365 365 365 329 272 232
2 21/2 533 533 533 533 533 533 533 533 533 486

METER AND SERVICE PIPE
(inches)
DISTRIBUTION PIPE
(inches)
MAXIMUM DEVELOPMENT LENGTH (feet)
Pressure Range Over 60 40 60 80 100 150 200 250 300 400 500
3/4 1/2a 3 3 3 2.5 2 1.5 1.5 1 1 0.5
3/4 3/4 9.5 9.5 9.5 9.5 7.5 6 5 4.5 3.5 3
3/4 1 32 32 32 32 32 24 19.5 15.5 11.5 9.5
1 1 32 32 32 32 32 28 28 17 12 9.5
3/4 11/4 32 32 32 32 32 32 32 32 32 30
1 11/4 80 80 80 80 80 80 69 60 46 36
11/2 11/4 80 80 80 80 80 80 76 65 50 38
1 11/2 87 87 87 87 87 87 87 87 87 84
11/2 11/2 151 151 151 151 151 151 151 144 114 94
2 11/2 151 151 151 151 151 151 151 151 118 97
1 2 87 87 87 87 87 87 87 87 87 87
11/2 2 275 275 275 275 275 275 275 275 275 252
2 2 365 368 368 368 368 368 368 368 318 273
2 21/2 533 533 533 533 533 533 533 533 533 533

For SI: 1 inch = 25.4, 1 foot = 304.8 mm, 1 pound per square inch = 6.895 kPa.
a. Minimum size for building supply is a 3/4-inch pipe.


TABLE AP.1

COLD WATER PIPE
SECTION
FITTINGS/VALVES PRESSURE LOSS
EXPRESSED AS
EQUIVALENT LENGTH
OF TUBE (feet)
HOT WATER PIPE
SECTION
FITTINGS/VALVES PRESSURE LOSS
EXPRESSED AS
EQUIVALENT OF TUBE
(feet)
A-B 3 – 21/2″ Gate valves 3 A-B 3 – 21/2″ Gate valves 3
1 – 21/2″ Side branch tee 12 1 – 21/2″ Side branch tee 12
B-C 1 – 21/2″ Straight run tee 0.5 B-C 1 – 2″ Straight run tee 7
1 – 2″ 90-degree ell 0.5
C-F 1 – 21/2″ Side branch tee 12 C-F 1 – 11/2″ Side branch tee 7
C-D 1 – 21/2″ 90-degree ell 7 C-D 1 – 1/2″ 90-degree ell 4
D-E 1 – 21/2″ Side branch tee 12 D-E 1 – 11/2″ Side branch tee 7

For SI: 1 inch = 25.4 mm, 1 foot = 304.8 mm, 1 degree = 0.01745 rad.


TABLE AP.2

PIPE SECTIONS FRICTION LOSS EQUIVALENT LENGTH (feet)
Cold Water Hot Water
A-B 0.69 × 3.2 = 2.21 0.69 × 3.2 = 2.21
B-C 0.085 × 3.1 = 0.26 0.16 × 1.4 = 0.22
C-D 0.20 × 1.9 = 0.38 0.17 × 3.2 = 0.54
D-E 1.62 × 1.9 = 3.08 1.57 × 3.2 = 5.02
Total pipe friction losses (Line K) 5.93 7.99

For SI: 1 foot = 304.8 mm.
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