DESIGN DATA. Dry 105a. September 5, 2008

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September 5, 2008 Dry 105a 1. Description Dry and Preaction Systems require a dependable source of clean dry air under the proper pressure. The air supply must be adequate to restore normal air pressure within a time specified by the authority having jurisdiction. N.F.P.A. requirements is 30 minutes for dry pipe systems. Proper air regulation should be provided for all and is extremely important. If pressure is too low, the dry valve may accidentally trip when subjected to surges in water supply pressure. If pressure is too high, the time between the opening of a sprinkler and the flow of the water from the sprinkler may be unacceptably long. Very high pressure also can damage the dry valve. Design air pressure is specified by the dry valve manufacturer. Air supplies may be provided by plant air systems, individual air compressors with or without tanks, and a compressed gas (nitrogen or dry air) in cylinders. Where the plant air system is manually operated and may be shut down over weekends or holidays, an automatic maintenance air compressor may be used to maintain the required pressure. A maintenance air compressor may be used as a primary source on small. It is often desirable to provide a low air pressure alarm activated by an air pressure switch. The switch is set below the lowest design air pressure and above the expected tripping point of the dry valve in order to provide time to take corrective action in the event of low air pressure alarm. 2. Design Considerations Manual Filling A dry system using manual filling employs a piping system as shown in Fig. 1. The relief valve should be set at 5 PSI (34 kpa) in excess of the design air pressure. The small drain cock is closed when filling and left open when shut off valves are closed. This is to prevent any air pressure build-up in system in case of valve leakage. To automatically maintain the design air pressure, a maintenance air compressor may be installed. See Fig. 2. It is installed on the riser above the dry valve and piped directly to the system. The switch is adjusted to turn the compressor off when the design air pressure is reached. Automatic Filling The dry system is filled from a constant source of air such as an automatic air compressor and uses components as shown in Fig. 3. The air compressor pressure switch is set at high and low pressures above design pressure. The air pressure in the system is maintained by the air pressure maintenance device which is set at design pressure. The air maintenance device contains a 1/16 inch (.16 MM) orifice which restricts the flow of air into the system so that when a sprinkler opens, air pressure will not build up faster than it will discharge through a sprinkler. The bypass valve is kept closed and opened only to speed up the filling of the system piping to the required pressure in the required time. Capacity of Air Compressor The capacity of the system must be calculated in order to furnish the correct size air compressor. Determine the total length of the different pipe sizes and use the following table to calculate the capacity: Pipe Diameter Capacity Schedule 40 (1 to 6 ) US International Schedule 30 (8 ) Schedule 10 Gal / Ft L / m Gal / Ft L / m 1 DN25 0.045 0.559 0.049 0.608 1-1/4 DN32 0.078 0.969 0.085 1.043 1-1/2 DN40 0.106 1.316 0.115 1.428 2 DN50 0.174 2.161 0.190 2.360 2-1/2 DN65 0.248 3.080 0.283 3.515 3 DN80 0.383 4.756 0.434 5.390 3-1/2 DN90 0.513 6.370 0.577 7.165 4 DN100 0.660 8.196 0.740 9.190 5 DN125 1.040 12.915 1.144 14.206 6 DN150 1.501 18.640 1.649 20.477 8 DN200 2.660 33.032 2.776 30.472 For Metric Units 1 Ft. = 0.3048 M, 1 Gal. = 3.785L The approximate free air capacity of a compressor suitable for pressurizing a system to 40 PSI (276 kpa) in 30 minutes can be found by multiplying the system capacity as determined above by 0.012 for CFM (or by 0.0898 for L/M). Form No. F_011607 Replaces page 105a-e, dated February 9, 2007. (Revised Figure 1.)

Dry 105b September 5, 2008 Nitrogen Cylinder Gas Supply (See Fig. 4) Nitrogen may be used in place of air compressors. Nitrogen is supplied in pressurized cylinders in various sizes and pressures. Some of the most common are 122 Cu. Ft. at 1900 PSI (3455 Ltrs. at 13100 kpa), 225 Cu. Ft. at 2100 PSI (6372 Ltrs. at 14480 kpa), and 280 Cu. Ft. at 2300 PSI (7930 Ltrs. at 15859 kpa). The cylinders may be connected to system the same as described for manual or for automatic filling. When nitrogen cylinders are used as a primary air supply, spare cylinders should be furnished and located at dry valve location. To determine the approximate amount of nitrogen to be furnished, the following formula may be used: Vc = Where: For US Units: For Metric Units: PV PV Vc = 100 108 Vc = Volume of Cylinder (ft. 3 ) P = Pressure of System (PSIG) V = Volume of System (Gallons) Where: Vc = Volume of Cylinder (L) P = Pressure of System (kpa) V = Volume of System (L) Special attention must be given to systems employing a bottled-gas supply. Because only a limited amount of gas is available, small leaks which normally would go unnoticed in systems being supplied by mechanical compressors, can become critical to the system s overall performance. If the system is to function at temperatures as low as -40 F (-40C), and, if bottled nitrogen is the gas supply, the system is particularly susceptible to leakage, and special care should be taken to ensure against leaks throughout the entire system. Figure 1

September 5, 2008 Dry 105c Figure 2

Dry 105d September 5, 2008 Figure 3

September 5, 2008 Dry 105e Figure 4

This page Intentionally left blank Form No. F_011607 Replaces page 105a-e, dated February 9, 2007. (Revised Figure 1.)