design of water supply for plumbing

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    Design of WATER SUPPLYFOR plumbing system inbuilding

    Engr. Fortunato H. Amosco,fnampap,ce,pme,pee

    PSPE-National President

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    DESIGN OF WATER SUPPLY SYSTEM

    An Application of the Requirements of

    Uniform Plumbing Code and or Revised

    National Plumbing Codes of the Phils.

    DESIGN OBJECTIVES:

    The most important design objective in sizing thewater supply system is the satisfactory supply ofpotable water to al fixtures at all times, and atproper pressure and flow rate for normal fixtureoperation. This may be achieved only if adequatesizes of pipes and appurtenances are provided.

    The sizes established must be large enough toprevent occurrence of negative pressures in anypart of the system during periods of peak demandinorder to avoid hazard of water supply

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    contamination due to backflow andbacksiphonage from potential sources of

    pollution. Hence the sizing of building

    water supply systems is a matter of vital

    concern in protecting health and must be

    regulated by codes. Other important

    objectives in the design of water supply

    system are:

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    to achieve economical sizing of piping andeliminate over design.

    To provide against potential supply failure dueto gradual reduction of pipe bore with the

    passing of time such as may result fromdeposits of corrosion or hard water scale in the

    piping. To avoid erosion-corrosion effects and potential

    pipe failure or leakage conditions owing tocorrosive characteristics of the water and/or to

    excessive design velocities of flow. To eliminate water hammer damage and

    objectionable whistling noise effect in thepiping due to excessive design velocity of flow.

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    The water supply system should be designed inaccordance with the minimum pressure available at

    the public water main, or other source of watersupply pressure, and the minimum pressurerequired at all time at water outlets of the system,

    where the pressure at the water main in insufficientto maintain the minimum required at the highest

    water outlet of the system, a pressure booster pumpsystem, approved as to the capacity and reliability,or an automatically controlled water supply tank oreither the hydro pneumatic pressure type or the

    elevated gravity type should be provided.

    As a general rule, the minimum pressurerequired at the ordinary faucet of plumbing

    fixture is 8 psi.

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    PRELIMINARY INFORMATION

    REQUIRED FOR SIZING A SYSTEM:

    First, obtain the necessary or all information forestablishing a proper basis for sizing the

    building water supply system, such as:

    1. The kinds of piping materials to be installed inthe system should be determined. This is a

    matter of selection by the ownerof the building

    or an authorized representative, who maybe an

    Engineer, an architect or a contractor, for anexperienced person who will select the piping

    materials, has knowledge and experience about.

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    THE SIGNIFICANT

    CHARACTERISTICS WHICH MAY BE

    APPLIED TO INDICATE WATERCORROSIVELY AND SCALE

    TENDENCY FORMING SUCH AS:

    pH value CO2 content

    dissolved air content

    carbonate hardness

    Langelier index, and ryznar index

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    THE MOST APPROPRIATESOURCE OF THEABOVE MENTIONED IS THE LOCAL WATERAUTHORITY HAVING JURISDICTION OVER

    THE SYSTEM SUPPLYING WATER.

    2. Location and size of the water supply

    3. Developed length of the system

    4. Pressure data relative to source of supply

    5. Elevations6. Minimum pressure required to the highest outlet

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    MANUFACTURERS RECOMMENDATIONS

    FOR AVOIDING EROSION-CORROSION:

    Velocity limits recommended by pipe manufacturersto avoid accelerated deterioration of their piping

    materials due to erosion-corrosion should be

    observed. Recent studies have shown that extreme

    turbulence accompanying high flow velocities is animportant factor causing erosion-corrosion and that

    it is especially prone to occur where the water supply

    has high carbon dioxide content (in excess of 10

    ppm) and where it has been softened to zero

    hardness. Another important factor is very high

    temperature (in excess of 150F).

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    TO CONTROL EROSION-CORROSION

    EFFECTS IN COPPER WATER TUBES, AND

    COPPER AND BRASS PIPE, MANUFACTURERS

    RECOMMENDATIONS ARE AS FOLLOWS:

    Where the water supply has a pH value higher that

    6.9 and a positive scale-forming tendency, such as

    may be shown by a positive Langelier index, velocityshould be limited to no more than 8 fps. (2.4 mps)

    Where water has a pH value lower than 6.9 and may

    be classified as aggressively corrosive or where water

    supply has been softened to zero hardness by passagethrough a softener, velocity should be limited to no

    more than 4 fps (1.2 mps)

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    The 4 fps (1. 2mps) velocity limitshould be applied to all not water

    piping conveying water at atemperature above 150oF because ofthe accelerated rate of corrosion at such

    temperature. q = 60.8 d 21.2 x (P/L)1/2 for across and cover

    piping

    d = inside dia. If pH value < 6.9 velocity not more than 4bp

    pH > 6.9 velocity not more than 6 bps

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    Problem No. 1

    Given:

    WCWater Closet URUrinal

    All WC are 1.6 GPF

    All UR are 1.0 GPF

    Static pressure at meter74 psi

    Distance from meter to most remote outlet150ft.

    Elevation of highest outlet above meter40ft.

    All pipe is L Copper Design velocity per standard8 ft/sec.

    Note: Lavatory group and drinking fountains were not

    includes in the design as their demands are minimal.

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    From Chart: Revised National Plumbing Code of the

    Philippines

    Tabulation per sample diagram of Sizing Water System

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    DRAWING

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    Solution: The demand for this system is computed from the

    fixture:

    1. Unit values given in the tables

    Therefore: 15 x 8 fu = 120 fixtures units13 x 5 fu = 65 fixture units

    Total demand = 185 fixture units

    2. Distance from meter to most remote fixture = 150 ft

    3. Elevation of highest outlet above meter = 40 ft

    4. Minimum pressure at the meter = 74 psi

    5. From table, 185 f.u = 88 GPM; show tabulated

    for all pipe runs etc.

    6. Determine the total pressure available for friction loss in pound persq.

    inch (psi) per 100 feet or pipe

    a. Flushometric valve requires a minimum available pressure of 15 psito operate properly.

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    Therefore:

    Minimum pressure to be maintained =15 psi

    b. Total static pressure loss (head loss)This isdetermined by multiplying the elevation distance by 0.433

    Therefore:

    40 ft x 0.433 psi/ft = 17.2 psi

    c. Pressure loss through meter, filters, reducing valves,backflow preventers, etc. In this illustration, we have

    chosen a 2 disc meter.This meter has a pressure loss

    of 6.5 psi at 85 gpm.

    Therefore: Meter loss = 6.5 psi

    Total Pressure Loss = 38.7 psi

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    Therefore: (minimum static pressureTotal pressure loss)

    = 74 psi38.7 psi = 35.3 psi

    NOTE:The remaining pressure of 35.3 psi is the maximumamount of pressure we have available for pressure loss dueto

    friction in our system while maintaining the minimumpressure of 15 psi at the highest outlet. However, this 35.3psi

    of pressure must be distributed throughout the total lengthof the system, which in this case has a total length of 150ft.

    Determine now the pressure loss per 100 ft of pipe. Thetotal loss is 35.3 psi for 150 ft. of pipe, we calculate this way:

    (100 x 35.3) divided by 150 = 23.53 psi loss per 100 ft of pipe.

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    7. From the Copper tubing chart project 23.53

    psi up until it intersect with GPM horizontalline as demand. Note that it intersect above

    line of velocity of 15 ft/sec., which is almost

    16.5 ft/sec. as their rated flow.a. Since recommended velocity is 8ft/sec.,

    however, good Engineering practice would

    further reduce this to between 4-6 ft/sec. but

    since our design call for 8ft/sec, we movefurther along the 8 GPM line until it intersect

    with 8 ft./sec.

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    b. Note that the intersection of our new point isanother pipe size line. This will be our newstarting point which is pipe size 21/2 dia at 8

    ft/sec. the GPM capacity will be 120 GPM.Going down to our 8 ft/sec transverse line as itintersect with the 2 line, the maximum GPMis:

    2 pipe = 73 GPM

    1 = 42 GOM

    1 = 10 GPM

    3/2 = 12 GPM

    Note that as we follow the line to below 1 there

    are three dotted lines.

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    These represent wall thicknesses ofsmaller pipes.

    Please note that the charts and tables are

    also found in the Uniform Plumbing

    Code, and also in our Revised Phil.National

    Plumbing Code, however there is no

    problem similar or problem with solutionlike what I have discussed today.

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    Thank you. Good day!

    God Bless Us!