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2 - Engineering Design Considerations ©2003, 2004, 2005 - Plastics Pipe and Fittings Association

General Design Piping Practices

• Follow generally accepted engineering practices

when designing with thermoplastic piping. These

include: – Selecting the proper material for the application

– Controlling pressure surges and velocities

– Identifying standards for piping components

– Selecting and proper sizing of pipe, valves and fittings

– Proper pipe supports, anchors, and guides – Proper underground design considerations

– Selecting the most cost effective system for required service life

– Following all applicable codes and standards




Plastic Piping Design Practices

• Plastic piping has several unique engineering

properties compared to non-plastic materials. To

ensure an effective and long lasting piping

installation, the design engineer needs to be aware

of these properties: – Chemical Resistance

– Pipe and System Pressure Ratings

– Temperature Limits – Temperature/Pressure Relationship

– Expansion/Contraction

– Pipe Support

– Underground Pipe Flexibility




Chemical Resistance

• Plastics in general have excellent chemical

resistance; however, there are certain chemical

environments that affect the properties of plastics in

the following ways: – Chemical Attack: An environment that attacks certain active sites

on the polymer chain.

– Solvation: Absorption of a plastic by an organic solvent.

– Plasticization: Results when a liquid hydrocarbon is mixed with apolymer but unable to dissolve it.

– Environmental Stress-Cracking: A failure that occurs when tensile

stresses combined with prolonged exposure to certain fluids

generate localized surface cracks.




Chemical Resistance Tables

• Many manufacturers have tested hundreds of

reagents to determine their affect on plastics. These

lists are readily available and act as a guide for the

user and design engineer. Listed is a rather broad

chemical resistance table of chemical groups and

piping material. A recommended fluid is based on

performance and safety factors.




General Chemical Resistance Tables

Chemical - Inorganics CPVC PE PP PVC PVDF

Acids, dilute R R R R R

Acids, concentrated R L L R R

Acids, oxidizing R NR NR R R

Alkalis R R R R R

Acid gases R R R R R

Ammonia gases NR R R L R

Halogen gases L L L L R

Salts R R R R R

Oxidizing salts R R R R R

Chemical - Organics CPVC PE PP PVC PVDF

Acids R R R R R

Acid anhydrides NR L L R L

Alcohols-glycols L L R NR R

Esters / ketones / ethers NR L L NR L

Hydrocarbons – aliphatic R L L L R

Hydrocarbons – aromatic NR NR NR NR R

Hydrocarbons – halogenated L NR NR L R

Natural gas L R R L R

Synthetic gas NR L L NR R

Oils L L L L R

R = Recommended L = Limited Use NR = Not Recommended


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Chemical Resistance Detailed Partial Chart

Sample Chemical Resistance Chart

Chemical PVC CPVC PP PVDF PE

Temperature (° F) 70 140 70 140 185 70 150 180 70 150 250 70 140Sulfuric acid, 50% R R R R R R R NR R R R R —

Sulfuric acid, 60% R R R R R R R NR R R R R —

Sulfuric acid, 70% R R R R R R NR NR R R R R —

Sulfuric acid, 80% R R R R R R NR NR R R — R NR

Sulfuric acid, 90% R NR R R R R NR NR R R — R NR

Sulfuric acid, 93% R NR R R NR R NR NR R R — R NRSulfuric acid, 100% NR NR NR NR NR NR NR NR NR NR — NR NR

R = Recommended — = No information available NR = Not Recommended

Shown is a partial chemical resistance table adapted from a manufacturer’s detail listing of hundreds of

reagents. These and similar tables are compiled from years of testing and research, however, if involved with a critical application and conflicting chemical resistance information, self-testing is advised.



• Thermoplastic piping’s pressure-ratings aredetermined by ASTM and PPI standards and

requirements. Pipe pressure ratings are calculated

using the following ISO equation:

Operating Pressure Determination

where:

PR = Pressure rating, psi (MPa)t = Minimum wall thickness, in (mm)

Dm = Mean diameter, in (mm)

HDS* = Hydrostatic design stress = HDB** (hydrostatic design

basis) • DF*** (design factor)

PR = 2(HDS) •t

Dm

* Most values of HDS for water @ 73°F are specified by ASTM and other standards.

** Hydrostatic design basis (HDB) is determined by long-term hydrostatic strength testing as

defined by ASTM and PPI standards. Each thermoplastic pressure piping material has an

established HDB @ 73°F or 180°F for water and hot water applications, respectively.

*** Maximum HDS for water uses a pipe design factor of 0.5. For gas pipe, the DF is 0.32.

All thermoplastic piping manufacturers list product pressure ratings in their technical literature.


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Pressure Ratings of

Thermoplastic Piping



Schedule Pipe

• Schedule pipe is IPS (Iron Pipe Size) OD pipe with

wall thickness that matches the wall thickness of the

same size and schedule steel pipe. Most vinyl pipe

is available in Schedule 40, 80, and 120. (The higher

the Schedule number, the thicker the pipe wall for

each size.) Scheduled pipe pressure ratings vary

with each pipe diameter. Pipe pressure ratings

decrease as pipe diameter increases for allschedules.




Standard Dimension Ratio (SDR)

• SDR pipe is based on the IPS OD system. The SDR

(Standard Dimension Ratio) is the pipe OD divided

by the wall thickness. For a given SDR, the pressure

ratings are constant for all pipe sizes for each plastic

material. Non-standard DRs (dimension ratios) can

be computed for any pipe OD and wall thickness.




Metric / Bar Rating• Metric or Bar Rated pipe is similar to SDR piping

ratings in that all sizes of a single SDR and the same

material have the same pressure rating. In the Metric

system, one bar = one atmosphere = 14.7 psi. A bar

rating of 16 = (14.7 x 16) = 235.2 psi.




Comparisons of SDR PVC Pipe

Pressure Ratings @ 73°F

SDR Rating Pressure Rating (psi) Bar Rating (atm)

13.5 315 21.4

17.0 250 17.0

21.0 200 13.6

26.0 160 10.9

32.5 125 8.5

41.0 100 6.8




Fittings• Pressure ratings of molded fittings are similar to that

of pipe as shown in the listed tables. However, some

molded fitting manufacturers have lowered or are

considering lowering the pressure capability of their

products in comparison to pipe. For pressure

capabilities of molded and fabricated fittings, consult

the manufacturer’s recommendations.




Other • Other plastic piping systems have differing outside

diameter dimensions and pressure ratings such as

Copper Tube Size (CTS), Cast Iron (CI) and Sewer

& Drain. Plastic piping made to most of these piping

systems are used for non-industrial applications.




Temperature Ratings of Plastic Piping

• Thermoplastic piping materials decrease in tensile

strength as temperature increases, and increase intensile strength as temperature decreases. This

characteristic must be considered when designing

TIPS. The correction factor for each temperature

and material is calculated. To determine the

maximum suggested design pressure at a particular temperature, multiply the base pressure by the

correction factor.




Nominal

Pipe Size (in.)PVC / CPVC PE (SDR 11)* PP** PVDF

½ 850 160 410 580

¾ 690 160 330 470

1 630 160 310 430

1 ½ 470 160 230 320

2 400 160 200 270

3 370 160 190 250

4 320 160 160 220

6 280 160 140 190

8 250 160 N/A N/A

10 230 160 N/A N/A

12 230 160 N/A N/A

Comparison of Schedule 80 Pipe

Pressure Ratings (psi) @ 73°F

* PE is not Schedule 80.

** Pipe pressure ratings shown are piping manufacturer’s values. PPI, as of yet, does not publish PP HDB or

HDS ratings.




Operating Temp. (°F) CPVC PE PP PVC PVDF

70 1.00 1.00 1.00 1.00 1.00

80 1.00 .90 .97 .88 .95

90 .91 .84 .91 .75 .87

100 .82 .78 .85 .62 .80

110 .72 .74 .80 .50 .75

120 .65 .63 .75 .40 .68

130 .57 .57 .68 .30 .62

140 .50 .50 .65 .22 .58

150 .42 * .57 NR .52

160 .40 * .50 NR .49

170 .29 * .26 NR .45

180 .25 * * NR .42

200 .20 NR NR NR .36

210 .15 NR NR NR .33

220 NR NR NR NR .30

240 NR NR NR NR .25

Temperature Correction Factors for Piping

* Drainage only NR = Not recommended




Example• What is the maximum pressure rating of 3” PP Sch.

80 pipe @ 120°F?

• Maximum Pressure Rating:

0.75(190) = 142.5 psi

NominalPipe Size (in.) PVC / CPVC PE (SDR 11) PP PVDF

2 400 160 200 270

3 370 160 190 250

4 320 160 160 220

OperatingTemp. (°F)

CPVC PE PP PVC PVDF

110 .77 .74 .80 .50 .75

120 .70 .63 .75 .40 .68

130 .62 .57 .68 .30 .62




Operating Pressure of Valves, Unions, and Flanges

• One of the limiting pressure ratings of TIPS and

other piping systems is the 150-psi pressure ratingof most valves, unions and flanges (some

manufacturers list some valves and unions at higher

pressure ratings). As in pipe, as the temperature

goes up, the pressure rating goes down.




Operating Temp. (°F) CPVC PP PVC PVDF

73-100 150 150 150 150

110 140 140 135 150

120 130 130 110 150

130 120 118 75 150

140 110 105 50 150

150 100 93 NR 140

160 90 80 NR 133

170 80 70 NR 125

180 70 50 NR 115

190 60 NR NR 106

200 50 NR NR 97

220 NR NR NR 67

240 NR NR NR 52

* Valve and union pressure ratings may vary with each manufacturer. Consult manufacturer’s published information.

NR = Not recommended

Maximum Operating Pressure (psi) of

Valves* / Unions* / Flanges




Operating Pressure of Threaded Pipe• Direct threading of thermoplastic piping is

accomplished using only proper threading

equipment. However, do not thread pipe below the

thickness of a Schedule 80 pipe wall. Threading

vinyl pipe reduces operating pressures by 50%. With

most other Schedule 80 thermoplastic piping,

threading reduces operating pressure for all pipe

sizes to 20-psi or less. If threaded thermoplasticpiping systems must be used, increased working

pressure could be obtained using transition fittings

such as molded unions and adapters.




Vacuum Collapse Ratingand Underground Loading

• Most industrial thermoplastic piping systems can

handle a vacuum as low as 5 microns. Withatmospheric pressure at 14.7 psi and a perfect

vacuum, most plastic piping cannot be brought to

collapse unless the pipe is brought to a partial out-of-

round condition, or an external radial pressure is

added. If a vacuum line is to be installed underground,special care must be taken to assure a minimum of

deformation. Contact the pipe manufacturer for

assistance if this condition is encountered.




• As fluid flows through a piping system, it

experiences head loss depending on fluid velocity,

pipe wall smoothness and internal pipe surface area.

Pipe and fitting manufacturers, using the Hazen-

Williams formula, have calculated and have readily

available the friction loss and velocity data for all

their products. Valve manufacturers have calculatedliquid sizing constants (Cv values) for each type and

size of valve in determining the pressure drop for a

given condition.

• To determine the pressure drop through a valve, the

following equation is used:

Pressure Losses inPlastic Piping Systems

where:

∆ P = Pressure drop across the valve (psi)

Q = Flow through the valve (gpm)

S.G. = Specific gravity of the liquid

Cv = Flow Coefficient

∆ P =Q² • S.G.

Cv²




• Find the pressure drop across a 1 ½ PVC ball check

valve with a water flow rate of 50 gpm:

Cv for valve = 56 (from manufacturer’s manual)

Example

∆ P =Q² • S.G.

Cv²=

(50)² • 1.0

(56)²= 0.797 psi




1” Pipe

GPM Velocity (ft/sec) Friction Head (ft) Friction Loss (psi)

7 3.26 4.98 2.16

10 4.66 9.65 4.18

15 6.99 20.44 8.86

20 9.32 34.82 15.09

25 11.66 52.64 22.81

30 13.99 78.78 31.97

35 16.32 98.16 53.36

Sample Partial Listing of Flow Capacity and

Friction Loss for Sch. 80 PVC per 100 ft.

1 ½ ” Pipe


7 1.31 0.54 0.23

10 1.87 1.05 0.46

15 2.81 2.23 0.97

20 3.75 3.80 1.65

25 4.69 5.74 2.49

30 5.62 8.04 3.48

35 6.56 10.70 4.64

40 7.50 13.71 5.94

45 8.44 17.05 7.39

50 9.37 20.72 8.98




• Find the velocity and friction head loss of 1 ½ PVC

Schedule 80 pipe @ 25 gpm:

Using table:Velocity = 4.69 ft/sec

Head loss = 5.74 ft

Example

1 ½ ” Pipe


20 3.75 3.80 1.65

25 4.69 5.74 2.49

30 5.62 8.04 3.48




C Factors for Common Piping Materials

Constant (C) Type of Pipe

150 All Thermoplastics / New Steel

140 Copper / Glass / New Cast Iron / Brass

125 Old Steel / Concrete

110 Galvanized Steel / Clay

100 Old Cast Iron




• Hydraulic shock or water hammer is a momentary

pressure rise resulting when the velocity of the liquid

flow is abruptly changed. The longer the line and

higher the liquid velocity, the greater the shock load

from the surge. For the piping system to maintain its

integrity, the surge pressure plus the pressure

existing in the piping system must not exceed 1 ½

times the recommended working pressure of thepiping system.

• The following formula determines the surge

pressure:

Hydraulic Shock

where:

P = Maximum surge pressure (psi)

v = Fluid velocity (ft/sec)

C = Surge wave constant

S.G. = Specific gravity of the liquid

P = v S.G.-1 C + C2




Example• What would the surge pressure be if a valve were

suddenly closed in a 2” PVC Sch. 80 pipe carrying

fluid with a S.G. of 1.2 at a rate of 30 gpm and a line

pressure of 160 psi @ 70°F?

C = 24.2 (from Surge Wave Constant Table)

v = 3.35 (from Flow Capacity & Friction Loss Table)

P = vS.G.-1

C + C2










P = 3.351.2 - 1

24.2 + 24.22










P = 3.35 ( 26.6 ) = 90 psi










Total line pressure = 90 + 160 = 250 psi

Note: 2” PVC Sch. 80 pipe has a pressure rating of 400 psi at 73°F;

therefore, 2” PVC Sch. 80 pipe is acceptable for this application.

P = 3.35 ( 26.6 ) = 90 psi




Avoiding Hydraulic Shock• Fluid velocity < 5 ft/sec

• Actuated valves with specific closing times

• Start pump with partially closed valve in dischargeline

• Install check valve near the pump discharge to keep

line full

• Vent all air out of system before start-up




Thermal Expansion & Contraction• Thermoplastics compared to non-plastic piping have

relatively higher coefficients of thermal expansion.

For this reason, it is important to consider thermal

elongation when designing thermoplastic piping

systems.

• Use the following formula to calculate the

expansion/contraction of plastic pipe:

where:

ΔL = Expansion of pipe (in.)

y = Constant factor (in./10°F/100 ft)

T1 = Maximum temperature (°F)

T2 = Minimum temperature (°F)

L = Length of pipe run (ft)

ΔL = y (T1-T2) • L10 100




Example• How much expansion will result in 300 ft of PVC pipe

installed at 50°F and operating at 125°F? (y for

PVC = 0.360)

ΔL = y(T1-T2)

•L

10 100

ΔL = 0.36

(125-50)

•

300

10 100

ΔL = 0.3675

•300

= 8.1 in.10 100




Values of y for Specific Plastics

Material y Factor

PVC 0.360

CPVC 0.456PP 0.600

PVDF 0.948

PE 1.000




Managing Expansion /Contraction in Piping System

• Forces which result from thermal expansion and contractioncan be reduced or eliminated by providing piping offsets,

expansion loops or expansion joints. The preferred methodof handling expansion/contraction is to use offsets and, or expansion loops. Expansion joints require little space butare limited in elongation lengths and can be a maintenanceand repair issue. As a rule-of-thumb, if the total temperature

change is greater than 30ºF (17ºC), compensation for thermal expansion should be considered.




Expansion Loops & Offsets• Expansion Loop Formula

where:

L = Loop length (in.)

E = Modulus of elasticity at maximum temperature (psi)

S = Working stress at maximum temperature (psi)

D = Outside diameter of pipe (in.)

ΔL = Change in length due to change in temperature (in.)

L =

3 ED (ΔL)

2S




• What would the loop length be to compensate for 4”

of expansion of 3” CPVC Sch. 80 pipe with a

maximum temperature of 110°F ?(outside diameter

of 3” pipe = 3.50 inches; E=371,000; S = 1500)

Example

L =3 ED (ΔL)

2S

L =3 • 371,000 • 3.5 • 4

2 • 1500

L = 15,582,000 ≈ 72 inches3000




• If provisions are not made for expansion/contraction,

the resulting forces will be transmitted to the pipe,

fittings and joints. Expansion creates compressive

forces and contraction creates tensile forces.

• To calculate the induced stress of restrained pipe,

use the formula:

St = ECΔT

Thermal Stress

where:

St = Stress (psi)

E = Modulus of elasticity (psi x 105

)C = Coefficient of thermal expansion (in./in./°F x 105)

ΔT = Temperature change between the installation temperature

and max/min temperature, whichever produces the greatest

differential (°F)




Example• What is the induced stress developed in 2” Schedule

80 PVC pipe with the pipe restricted at both ends?

Assume the temperature extremes are from 70°F to

100°F.

St = ECΔT = (3.60 x 105) x (3.0 x 105) x (100-70)

St = 324 psi

Note: Steel pipe stress is approximately 15 – 20 times higher than most plastic

piping.




• To determine the magnitude of the longitudinal force,

multiply the stress by the cross-sectional area of the

plastic pipe. The formula is:

F = St • A

Longitudinal Force

where:

F = Force (lbs.)St = Stress (psi)

A = Cross-sectional area (in2)




Example• With the stress as shown in the previous example,

calculate the amount of force developed in the 2”

Schedule 80 PVC pipe? (cross-sectional area of 2”

pipe = 1.556 in2)

F = St • A = 324 psi • 1.556 in2

F = 504 lbs.



©2003, 2004, 2005 - Plastics Pipe and Fittings Association

Above-ground Design




Support Spacing• The tensile and compressive strengths of plastic

pipe are less than those of metal piping.

Consequently, plastics require additional pipe

support. In addition, as temperature increases,tensile strength decreases requiring additional

support. At very elevated temperatures, continuous

support may be required.

S t S i f TIPS S h d l 80 Pi (ft)*




Support Spacing of TIPS Schedule 80 Pipe (ft)*

Nominal Pipe

Diameter (in.)

CPVC PP PVC PVDF

60°F 100°F 140°F 60°F 100°F 140°F 60°F 100°F 140°F 60°F 100°F 140°F

½ 5 ½ 5 4 ½ 4 3 2 5 4 ½ 2 ½ 4 ½ 4 ½ 2 ½

¾ 6 5 ½ 4 ½ 4 3 2 5 ½ 4 ½ 2 ½ 4 ½ 4 ½ 3

1 6 ½ 6 5 4 ½ 3 2 6 5 3 5 4 ¾ 3

1 ½ 7 6 ½ 5 ½ 5 3 ½ 2 6 ½ 5 ½ 3 ½ 5 ½ 5 3

2 7 ½ 7 6 5 3 ½ 2 7 6 3 ½ 5 ½ 5 ¼ 3

3 9 8 7 6 4 2 ½ 8 7 4 6 ½ 5 ¾ 4

4 10 9 7 ½ 6 4 ½ 3 9 7 ½ 4 ½ 7 ¼ 6 4

6 11 10 9 6 ½ 5 3 10 9 5 8 ½ 7 5

8 11 11 10 7 5 ½ 3 ½ 11 9 ½ 5 ½ 9 ½ 7 ½ 7

* Listings show spacing (ft) between supports. Pipe is normally in 20-ft lengths. Use continuous support for spacing under three feet.




Pipe Support Spacing withSpecific Gravities Greater Than 1.0*

Specific Gravity Correction Factor

1.0 1.00

1.1 0.98

1.2 0.96

1.4 0.93

1.6 0.90

2.0 0.85

2.5 0.80

* Above data are for un-insulated lines. For insulated lines,

reduce spans to 70% of values shown.




Pipe Hangers• Use hangers that have a large bearing area to

spread out the load over the largest practical area.

The basic rules for hanging plastic pipe are: – Avoid point contact or concentrated bearing loads.

– Avoid abrasive contact.

– Use protective shields to spread the loads over large areas.

– Do not have the pipe support heavy valves or specialty fittings.

– Do not use hangers that “squeeze” the pipe.




Pipe Roll

& Plate

Adjustable

Solid Ring

Double-belt

Pipe Clamp

Single

Pipe Roll

Typical Pipe Hangers

Riser Clamp

Wrought Clevis

Roller Hanger




Pipe & Valve Supports

Supporting Plastic

Pipe Vertically

Continuous Support

with Structural Angle

Overhead Supportfor Valve

Shoe

Support

Trapeze SupportHanger with

Protective Sleeve

Valve Support

from Below




Anchors & Guides• Anchors direct movement of pipe within a defined

reference frame. At the anchoring point, there is no

axial or transverse movement. Guides allow axial

movement of pipe but prevent transverse movement.Use guides and anchors whenever expansion joints

are utilized and on long runs and directional changes

in pipe.




Anchoring

Pipe with

Metal Anchor

Pipe with

Concrete Anchor

Pipe with

Metal

Chain

Anchor

Pipe with Metal

Sleeve and Anchor




Anchoring & Guide Design Diagrams




• With thermoplastic piping having a thermal

conductance of 1/300 of steel and 1/2700 of copper,

minimum or no insulation may be required.

Insulation of Plastic Piping• To calculate heat loss or gain through plastic piping,

the following equation is used:

where:

Q = Heat gain or loss (Btu)

K = Thermal conductivity of the pipe

(Btu-in./ft2-hr-°F)

ΔT = Temperature difference of inside

and outside pipe walls (°F)

A = Surface area (ft 2)

x = Wall thickness (in.)

t = Time (hrs.)

Q =K t A • ΔT

x




Example• What is the heat loss over 1 hour of a 1-foot long

section of 2” PVC Sch. 80 pipe with a temperature

difference of 80°F?

Q =K t A • ΔT

=1.2 • 1 • 0.621 • 80

= 273.47 Btux 0.218

K = 1.2 Btu-in./ft2-hr-°F (for PVC)

D = 2.375 in. for 2” pipe

A = πDL = (3.141)(2.375 in.)(1ft/12in.)(1 ft) = 0.621 ft2

x = 0.218 in.




Example• What is the heat loss over 1 hour of a 1-foot long

section of 2” Carbon Steel Sch. 80 pipe with a

temperature difference of 80°F?

Q =K t A • ΔT

=321.4 • 1 • 0.621 • 80

= 73243.8 Btux 0.218

K = 321.4 Btu-in./ft2-hr-°F (for steel)

D = 2.375 in. for 2” pipe

A = πDL = (3.141)(2.375 in.)(1ft/12in.)(1 ft) = 0.621 ft2

x = 0.218 in.




Other Above-groundDesign Considerations




Cold Environments• Most plastic piping systems handle temperatures

below 0°F if the system liquid does not freeze.

However, the pipe flexibility and the impact

resistance decrease. This may cause the pipe tobecome brittle. Protect the pipe from impact if this

condition can occur. To prevent liquid freezing or

crystallization in piping, electric heat tracing may be

used and applied directly on the pipe within theinsulation. The heat tracing must not exceed the

temperature-pressure system design.




Hot Environments• When pressure-piping applications exceed 285°F,

the use of thermoplastic piping is limited. Make sure,

in temperatures above 100°F, that expansion/

contraction, reduced working pressures and supportspacing are considered.




Outdoor Environments• Most TIPS are formulated for protection against the

harmful ultraviolet rays from the sun. However, long

periods of exposure to direct sunlight can oxidize the

surface of the piping, causing discoloration andreduced impact resistance. To prevent these

phenomena, opaque tape or paint can be applied.

Be sure to use acrylic or water-based paints. Do not

use oil-based paints as they may cause harm tosome plastic piping.




Compressed Air • Except for specially designed and designated plastic

piping systems, most manufacturers do not

recommend their product for handling of or testing

with any compressed gases.




Below-groundConsiderations




Below-ground Design• Plastic pipe in most instances is considered a

flexible pipe rather than a rigid piping material.

Flexible pipe is pipe that is able to bend without

breaking and uses the pipe wall and buried mediumto sustain external loads. When installed properly,

plastic develops support from the surrounding soil.

• Pipe deflection or compression depends on any one

or a combination of three factors: – Pipe stiffness

– Soil stiffness (soil density along the sides of the pipe)

– Load on the pipe (earth/static/live)




Pipe Stiffness• Pipe stiffness is the force in psi divided by the

vertical deflection in inches. An arbitrary data point

of 5% deflection is used as a comparison of pipe

stiffness values in flexible piping. Each pressurepiping material has a different pipe stiffness value

that is based on the material’s flexural modulus. For

any given SDR, the pipe stiffness remains constant

for all sizes.




Soil Stiffness• Soil stiffness is the soil’s ability to resist compaction.

There is a formula (Spangler’s) to determine the “E”

values or deflection of buried flexible pipe in terms of

soil stiffness independent of pipe size. The “E” valueis also referred to as the modulus of soil reactions.

The soil backfill type and amount of compaction

directly affect these values.




Pipe Loading• Earth loads may be calculated using Marston’s load

formula. Static loads are calculated using

Boussinesq’s Equation. Live or dynamic loads are

also calculated using Boussinesq’s Equation, bymultiplying the superimposed load (W) by 1 ½.

There are many existing tables available from pipe

manufacturers for various piping materials listing soil

conditions, soil compaction, pipe stiffness values,maximum height of cover recommendations and

other useful data to design underground plastic

piping systems.



Trench Design & Terminology




Trench Design & Terminology

Nom. Pipe Sizes

(Diameter in.)

Number of

Pipe Diameters

Trench Width

(in.)

4 4.3 18

6 2.9 18

8 2.9 24

10 2.5 26

12 2.4 30

15 2.0 30

18 1.8 32

21 1.6 34

24 1.5 36

27 1.5 40

30 1.4 42

33 1.4 46

36 1.4 50

40 1.4 56

48 1.3 62




Minimum Cover of Buried Pipe• The following guidelines may be used when burying

plastic pipe: – Locate pipe below the frost line

– A minimum cover of 18 in. or one pipe diameter (whichever isgreater) when there is no overland traffic

– A minimum cover of 36 in. or one pipe diameter (whichever is

greater) when truck traffic may be expected

– A minimum cover of 60 in. when heavy truck or locomotive traffic

is possible



TIPS are...• Environmentally sound

• Easy and safe to install

• Reliable

• Long-lasting

• Cost-effective

03-ppfa_v2.3_engdsgn

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