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BNBC 2020 · Part 8 — Building Services

Appendix O — Sizing of Cold Water Supply and Distribution Piping

Gazette pages 4980–4996 · Official gazette pages (PDF, 691 KB) — use for exact tables and figures.

The water distribution within the building may be an up0feed or down0feed system. The design principles are the same for both the systems. The principal difference in the calculation procedure is that in the up feed system the difference in elevation between the fixtures and the water supply main exerts the pressure that supplies water into the fixtures, but in the down-feed system the difference in elevation between the fixtures and the roof storage tank provides the pressure to overcome the pipe friction. The following are the recommended pipe sizing procedures: O.1 The sketch of the main lines, risers and branches serving different fixtures will have to be drawn. O.2 Determine the number and types of fixture that will be required on the basis of the Table 8.6.1 in Chapter 6. O.3 The demand weight of different fixture units may be computed in terms of water supply fixture unit (wsfu) in accordance with Table 8.O.1. O.4 The peak demand load (or maximum probable flow) in liter per minute may be estimated with the data obtained in Sec O.3 using Figure 8.O.1 or on the basis of the number of occupants according to their occupancy classification specified in Table 8.5.1. O.5 The equivalent length of the main lines, risers and branches will be determined. The equivalent length of different fittings may be estimated on the basis of the data presented in the Tables 8.O.2(a), 8.O.2(b) and 8.O.2(c) or from manufacturer's specification. The total equivalent length is the sum of the equivalent lengths of all pipes and fittings. O.6 The pressure loss through water meter may be determined on the basis of their operating characteristics as shown in Figure 8.O.6 (Disk type water meter). The data for other types of water meter may be obtained from the manufacturer. O.7 The minimum pressure required at different fixtures to produce adequate flow may be estimated on the basis of the type of fixtures or minimum size of supply pipe in accordance with Table 8.5.6. O.8 The average pressure drop in kPa per meter of equivalent pipe length may be computed as follows:

F p  ( P   9 . 807 H  f ) / L 8.O.1)

Where, F p = Average available pressure loss (kPa) per meter of equivalent length of pipe

P = Pressure (kPa) in the water main or zero for overhead gravity storage tank.

H = Height (m) of the highest fixture above the water main or difference (m) in elevation between storage tank and the fixture under consideration.

f = Pressure loss (kPa) through water meter or such other fittings plus pressure (kPa) required to produce adequate flow through the most remote fixture in upfeed system or the fixture under consideration in down-feed system.

L = Equivalent pipe length (m) * + sign is for down-feed system and - sign is for up-feed system

O.9       The pipe size may also be estimated from Figures 8.0.5 to 8.0.10 for different
          types of piping materials on the basis of the expected rate of flow determined in
          Sec 0.4 and the average pressure available for friction loss ( ) in Sec O.8.
O.10      Alternative simple procedure of pipe size computation has also been explained
          in the Sec 5.10.3.

Table 8.O.1: Water Supply Fixture Unit (wsfu) Values for Various Plumbing Fixtures

    Fixture or group       Supply Control                        wsfu
                                                 Cold            Hot            Total

Bath group                 Flush tank             4.5              3              6
Bath group                 Flush valve             6               3              8
Bathtub                    Faucet                 1.5             1.5             2
Bidet                      Faucet                 1.5             1.5             2
Combination                Faucet                  2               2              3
Kitchen sink               Faucet                 1.5             1.5             2
Laundry tray               Faucet                  2               2              3
Laundry                    Faucet                 1.5             1.5             2
Pedestal urinal            Flush valve             10              -             10
Restaurant sink            Faucet                  3               3              4
Service sink               Faucet                 1.5             1.5             2
Shower head                Mixing Valve            3               3              4
Stall or wall urinal       Flush tank              3               -              3
Stall or wall urinal       Flush valve             5               -              5
Water closet               Flush tank              5               -              5
Water closet               Flush valve             10              -             10
*      Fixture with both cold and hot water supplies, the weight for maximum separate
       demands may be considered 75% of total wsfu.

Table 8.O.2(a): Fitting Losses In Equivalent Metre of Pipe - Screwed, Welded, Flanged, Flared and Brazed Connections

Nominal                              Smooth Bend Elbows
  Pipe        90o       90o Long       90o        45o             45o   180o
or Tube      Std*        Rad.**      Street*      Std*       Street*    Std*
  Size
 (mm)

   10        0.43         0.27        0.70        0.21         0.34     0.70
   13        0.49         0.31        0.76        0.24         0.40     0.76
   19        0.61         0.43        0.98        0.27         0.49     0.98
   25        0.79         0.52        1.25        0.40         0.64     1.25
   32        1.01         0.70        1.71        0.52         0.92     1.71
   38        1.22         0.79        1.92        0.64         1.04     1.92
   50        1.53         1.01        2.50        0.79         1.37     2.50
   63        1.83         1.25        3.05        0.98         1.59     3.05
   75        2.29         1.53        3.66        1.22         1.95     3.66
   88        2.75         1.80        4.58        1.43         2.23     4.58
  100        3.05         2.04        5.19        1.59         2.59     5.19
  125        3.97         2.50        6.41        1.98         3.36     6.41
  150        4.88         3.05        7.63        2.41         3.97     7.63
  200        6.10         3.97          -         3.05             -    10.07
  250        7.63         4.88          -         3.97             -    12.81
  300        9.15         5.80          -         4.88             -    15.25
  350        10.37        7.02          -         5.49             -    16.78
  400        11.59        7.93          -         6.10             -    18.91
  450        12.81        8.85          -         7.02             -    21.35
  500        15.25        10.07         -         7.93             -    24.71
  600        18.30        12.20         -         9.15             -    28.67
* = R/D approximately equal to 1, ** = R/D approximately equal to 1.5
Table 8.O.2(b): Fitting Losses in Equivalent Metre of Pipe - Screwed, Welded,
Flanged, Flared and Brazed Connections
Nominal                 Smooth Bend Tees                                  Metre Elbows
  Pipe     Flow Thru            Straight-Thru Flow           90o EII   60o EII    45o EII   30o EII
 or Tube
                          No        Reduced      Reduced
   Size     Branch
                       Reduction        ¼             ½
  (mm)

  10        0.82        0.27          0.37           0.43    0.82      0.34        0.18     0.09
  13        0.92        0.31          0.43           0.49    0.92      0.40        0.21     0.12
  19        1.22        0.43          0.58           0.61    1.22      0.49        0.27     0.15
  25        1.53        0.52          0.70           0.79    1.53      0.64        0.31     0.21
  32        2.14        0.70          0.95           1.01    2.14      0.92        0.46     0.27
  38        2.44        0.79          1.13           1.22    2.44      1.04        0.55     0.34
  50        3.05        1.01          1.43           1.53    3.05      1.37        0.70     0.40
  63        3.66        1.25          1.71           1.83    3.66      1.59        0.85     0.52
  75        4.58        1.53          2.14           2.29    4.58      1.95        0.98     0.61
  88        5.49        1.80          2.44           2.75    5.49      2.23        1.22     0.73
 100        6.41        2.04          2.75           3.05    6.41      2.59        1.37     0.82
 125        7.63        2.50          3.66           3.97    7.63      3.36        1.83     0.98
 150        9.15        3.05          4.27           4.88    9.15      3.97        2.14     1.22
 200        12.20       3.97          5.49           6.10    12.20     5.19        2.75     1.56
 250        15.25       4.88          7.02           7.63    15.25     6.41        3.66     2.20
 300        18.30       5.80          7.93           9.15    18.30     7.63        3.97     2.44
 350        20.74       7.02          9.15           10.37   20.74     8.85        4.58     2.75
 400        23.79       7.93         10.68           11.59   23.79     9.46        5.19     3.05
 450        25.93       8.85         12.20           12.81   25.93     11.29       5.80     3.36
 500        30.50       10.07        13.42           15.25   30.50     12.51       6.71     3.97
 600        35.08       12.20        15.25           18.30   35.08     14.95       7.63     4.88
* = R/D approximately equal to 1, ** = R/D approximately equal to 1.5

Table 8.O.2(c): Valve Losses in Equivalent Metre of Pipe - Screwed, Welded, Flanged and Flared Connections

Nominal    Globe     60o – Y 45o –    Angle*       Gate         Swing       Lift
Pipe or                       Y                                Check**     Check

 Tube
  Size
 (mm)

   10       5.19      2.44    1.83     1.83         0.18         1.53
   13       5.49      2.75    2.14     2.14         0.21         1.83
   19       6.71      3.36    2.75     2.75         0.27         2.44    Globe Lift
   25       8.85      4.58    3.66     3.66         0.31         3.05        and
   32      11.59      6.10    4.58     4.58         0.46         4.27      Vertical
                                                                            Lift:
   38      13.12      7.32    5.49     5.49         0.55         4.88
                                                                          Same as
   50      16.78      9.15    7.32     7.32         0.70         6.10
                                                                           Globe
   63      21.05      10.68   8.85     8.85         0.85         7.63
   75      25.62      13.12 10.68      10.68        0.98         9.15     Valve**

   88      30.50      15.25 12.51      12.51        1.22         10.68
  100      36.60      17.69 14.34      14.34        1.37         12.20
  125      42.70      21.66 17.69      17.69        1.83         15.25
  150      51.85      26.84 21.35      21.35        2.14         18.30
  200      67.10      35.08 25.93      25.93        2.75         24.40
  250      85.40      44.23 32.03      32.03        3.66         30.50
                                                                            Angle
  300      97.60      50.33 39.65      39.65        3.97         36.60
                                                                            Lift:
  350      109.8      56.43 41.18      41.18        4.58         41.18
                                                                          Same as
  400      125.05     64.05 54.90      54.90        5.19         45.75     Angle
  450      140.3      73.20 61.00      61.00        5.80         50.33      Valve
  500      158.6      83.88 71.68      71.68        6.71         61/00
  600      186.05     97.60 80.83      80.83        7.63         73.20
  * These loses do not apply to valves with needle point type seat, ** Losses also
  apply to the in-line, ball type check valve.

Figure 8.O.1 Water supply demand for various load in water supply fixture units (Wsfu)

Figure 8.O.2(a) Direct connection of roof storage tank with public water main

Figure 8.O.2(b) System incorporating balancing roof tank and direct water main connection

Figure 8.O.2(c) System incorporating underground tank

Figure 8.O.3(a) Zoning floors (5) by intermediate tanks supplied by OH storage tank

Figure 8.O.3(b) Zoning floors (5) by intermediate tanks supplied by independent pumps

Figure 8.O.3(c) Gravity water supply system with pressure–reducing valves

Figure 8.O.3(d) Hydro-pneumatic system of water supply in a building

Figure 8.O.4 Hazen-Williams nomograph with roughness coefficient, C = 100

Figure 8.O.5 Friction loss through taps and tees

Figure 8.O.6 Loss of pressure through disc - type meter in kPa

Figure 8.O.7 Friction loss in fairly rough pipe

Figure 8.O.8 Friction loss in rough pipe

Figure 8.O.9 Friction loss in fairly smooth pipe

Figure 8.O.10 Friction loss in copper pipe

Source: Bangladesh National Building Code 2020, S.R.O. No. 55-Law/2020, Bangladesh Gazette (Extraordinary), 11 February 2021. Tables, figures and equations: refer to the linked gazette pages.