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AMERICAN NATIONAL STANDARD K61.1-1981 <br /> \ and charged only in the open atmosphere or in 2.12.8 Excess flow valves or other protective <br /> buildings provided for that purpose. devices should be installed to prevent discharge <br /> s used for transferrin ammonia of the contents of containers if loading or <br /> 2.12.6 Pumps g unloading connectors or valves are cleanly <br /> shall be recommended and labeled for ammonia broken.Piping shall be sized so as not to restrict <br /> service by the manufacturer. flow to rates such that the protective devices will <br /> 2.12.6.1 Positive displacement pumps shall not function. If excess flow valves cannot be- <br /> be equipped with a pressure actuated by-pass installed to provide adequate protection,remotely <br /> valve on the discharge side of the pump. This operated internal or external shut-off valves <br /> valveshall operate to limit the pressure developed shall be installed. <br /> by the pump to the maximum for which the pump 2.12.9 Meters used for the measurement of <br /> is rated. Piping or tubing sized to carry the full liquid anhydrous ammonia shall be recom- <br /> capacity of the pump at the actuation pressure of mended and labeled for ammonia service by the <br /> this valve shall connect the discharge of this valve manufacturer. <br /> with the container from which ammonia is being <br /> pumped. If this line is capable of being valved 2.12.9.1 Liquid meters shall be designed for <br /> closed, an additional by-pass device shall be a minimum working pressure of 250 psig(1720 <br /> incorporated in the pump to by-pass back to the kPa). <br /> suction port.The pressure actuated by-passvalve 2,12.9.2 The metering system shall incor- <br /> and the return piping ortubing shall be installed ' porate devices that will prevent the inadvertent <br /> in accordance with the pump manufacturer's measurement of vapor. <br /> recommendations. <br /> 2.12.6.2 On the discharge side of the pump, 2.13 Tank Car Unloading Points <br /> before the relief valve line, install a pressure and Operations <br /> gage graduated from 0 to 400 psig(0-2758 kPa). 2,13.1 Provisions for unloading tank cars shall <br /> 2.12.6.3 Plant piping shall contain shut-off conform to the Regulations of the Department of <br /> valves located as close as practical to pump Transportation. <br /> v connections. 2.13.2 Unloading operations shall be per- <br /> 2.12.7 Compressors used for transferring or formed by reliable persons properly instructed <br /> refrigerating ammonia shall be recommended and made responsible for careful compliance <br /> and labeled for ammonia service by the with all applicable procedures. <br /> manufacturer. 2.13.3 Caution signs shall be so placed on the <br /> 2.12.7.1 Compressors,except those used for track or car as to give necessary warning to <br /> refrigeration, shall be designed for at least 250 persons approaching the car from the open end or <br /> psig(1720kPa)working pressure.Crank cases of ends of the siding.The signs shall remain in place <br /> compressors not designed to withstand system until the car is unloaded and disconnected from <br /> pressure shall be protected with a suitable pres- the discharge connections. <br /> sure relief valve. 2.13.4 The track of a tank car siding shall be <br /> 2.12.7.2 Plant piping shall contain shut-off substantially level. <br /> valves located as close as practical to compressor 2,13.5 Brakes shall be set and wheels blocked <br /> connections. on all cars being unloaded. <br /> 2.12.7.3 A pressure relief valve large enough 2,13.6 Tank cars of anhydrous ammonia shall <br /> to discharge the full capacity of the compressor be unloaded only at approved locations meeting <br /> shall be connected to the discharge before any the requirements of paragraphs 2.10.3 and 2.12.8. <br /> shut-off valve. <br /> 2.12.7.4 Compressors shall have pressure 2,14 Liquid Level Gaging Device <br /> gages at suction and discharge graduated to at <br /> least one and one-half times the maximum 4.1 Each container <br /> except those <br /> filled <br /> by <br /> wei <br /> pressure that can be developed. g 4ni pP approved <br /> id <br /> 2.12.7.5 Adequate means,such as drainable level gaging device. <br /> liquid trap, may be provided on the compressor 2.14.2 All gagingdevicesshall be arranged so <br /> suction to minimize the entry of liquid into the that the maximum liquid level to which the <br /> compressor. container is filled is readily determined. (See <br /> 2.12.7.6 Where necessary to prevent con- <br /> 2.3.2(g)] <br /> tamination,an oil separator shall be provided on 2.the 14.3 t to the atmosphere devices that require <br /> such then tory <br /> of <br /> the discharge side of the compressor. P P <br /> 15 <br />