WAC 296-826-60020
General specifications.
You must:
• Get owner authorization to use transfer containers.
• Make sure transfer containers are gauged and filled in either:
– Open atmospheres;
OR
– Buildings approved for that purpose.
• Make sure pumps used to transfer ammonia meet all of the following:
– Have a manufacturer's label for ammonia service
– Are designed for at least 250 psig working pressure
– Have a constant differential relief valve discharging into the suction port that:
▪ Is installed on positive displacement pumps;
AND
▪ Meets the pump manufacturer's recommendation for the settings and installation
– Have a pressure gauge graduated zero to 400 psig installed on the discharge side before the relief valve line.
• Make sure plant pipes with shut off valves are located as close as possible to the pump connections.
• Make sure meters used for measuring liquid anhydrous ammonia:
– Are recommended and labeled for ammonia service by the manufacturer
– Are designed for a minimum working pressure of 250 psig
– Incorporate devices that prevent unintended measurement of vapor.
• Do the following when transferring ammonia:
– Maintain ammonia at a temperature suitable for the receiving container
– Have at least one attendant supervise the transfer from the time connections are made to when disconnection occurs
– Do
NOT
use flammable gases or gases that will react with ammonia, such as air to unload tank cars or transport trucks.
• Make sure compressors used for transferring ammonia meet all of the following:
– Have a working pressure of at least 250 psig when transferring ammonia.
▪ If crank cases of compressors are not designed to withstand system pressure, then provide protection with a suitable safety relief valve
– Are connected to plant piping with shut off valves located as close as practical to compressor connections
– Have a safety relief valve that is both:
▪ Large enough to discharge the full capacity of the compressor;
AND
▪ Connected to the discharge before any shut off valve
– Have an oil separator on the discharge side, where necessary to prevent contamination
– Have a drainable liquid trap or other adequate method on the compressor suction to minimize the entry of liquids into the compressor
– Pressure gauges on the suction and discharge ends graduated to at least one and one-half times the maximum pressure that can develop.
• Protect loading and unloading systems in the event of hose severance by suitable devices where necessary, such as:
– Backflow check valves;
OR
– Properly sized excess flow valves.
Note:
If such valves are not practical, remotely operated shut off valves may be installed.
[Statutory Authority: RCW
49.17.010
,
49.17.040
,
49.17.050
,
49.17.060
. 06-10-067, § 296-826-60020, filed 5/2/06, effective 9/1/06.]