Cal. Code Regs. tit. 8, § 509
(a) No anhydrous ammonia shall be vented to the atmosphere during the transfer operation unless the vent is led to a safe point of discharge.
Anhydrous ammonia shall not be stored in or transferred into a container at a temperature lower than that shown on the nameplate.
Containers shall be charged or used only upon authorization of the owner.
(d) During the transfer of anhydrous ammonia, at least 1 attendant familiar with the installation shall remain in attendance at the controls necessary to stop the transfer operation. This attendant shall be considered familiar with the installation only after he has been provided with a set of operating instructions for the unloading operation and has been instructed through a minimum of 3 full cycles of operation. During the transfer of anhydrous ammonia into or from a transportation tank, the brakes of the transporting vehicle shall be set and the wheels blocked.
Provisions for unloading tank cars shall conform to the applicable recommendations contained in the DOT regulations. See 560(e) for Railroad Tank Car Loading and Unloading.
(f) All pumps and compressors used for the transfer of anhydrous ammonia shall be suitable for this service and shall be equipped with a pressure-actuated bypass valve and/or other acceptable device to prevent pressure in the transfer equipment of more than 400 psi unless the piping system is specifically designed for higher pressures. In no case shall safety relief valves used for this purpose be set to open at pressures of less than 325 psi or more than 400 psi.
(1) Pumps shall be designed for at least 250 p.s.i. working pressure. Positive displacement pumps shall have, installed off the discharged port, a constant differential relief valve discharging into the suction port of the pump through a line of sufficient size to carry the full capacity of the pump at relief valve setting, which setting and installation shall be according to the pump manufacturer's recommendations.
On the discharge side of the pump, before the relief valve line, there shall be installed a pressure gage graduated from 0 to 400 p.s.i.
Plant piping shall contain shutoff valves located as close as practical to pump connections.
(2) Compressors used for transferring or refrigerating ammonia shall be recommended for ammonia service by the manufacturer.
Compressors shall be designed for at least 250 p.s.i. working pressure.
Plant piping shall contain shutoff valves located as close as practical to compressor connections.
A relief valve large enough to discharge the full capacity of the compressor shall be connected to the discharge before any shutoff valve.
Compressors shall have pressure gages at suction and discharge graduated to at least one and one-half times the maximum pressure that can be developed.
Adequate means, such as drainable liquid trap, shall be provided on the compressor suction to minimize the entry of liquid into the compressor.
Where necessary to prevent contamination, an oil separator shall be provided on the discharge side of the compressor.
(g) The filling densities for containers that are not refrigerated shall not exceed the following:
Type of Container
Percent By Weight
Percent By Volume
Uninsulated
56
82
Uninsulated (see 509(h))
87.5
Insulated
57
83.5
D.O.T. In accordance with D.O.T. Regulations
(h) Uninsulated containers may be charged 87.5 percent by volume provided the temperature of the anhydrous ammonia being charged is determined to be not lower than 30° F or provided the charging of the container is stopped at the first indication of frost or ice formation on its outside surface and is not resumed until such frost or ice has disappeared.
Any container, including DOT cargo and portable tanks, shipped under DOT jurisdiction shall be filled according to DOT regulations.
(i) Every portable unloading facility shall comply with the following additional requirements:
(5) The portable unloading facility must be secured at the end of each period of operation; i.e., the point at which it becomes unattended, the end of a workday, etc.
The facility will be considered secured when all ammonia liquid is confined in the pressure vessel and the gas pressure in any hose is less than 25 psi.
(6) All pressure vessels, hoses, piping, fittings, etc., shall be as required elsewhere in these orders for anhydrous ammonia in the liquid state (high pressure).
Note: Portable transferring facilities for anhydrous ammonia is defined as any site at which anhydrous ammonia is transferred from one pressure vessel to another in which the compressor and receiving vessel are not permanently installed on concrete in accordance with Safety Section 501.
1. Amendment filed 12-8-72 as procedural and organizational; effective upon filing (Register 72, No. 50).
2. Amendment filed 3-28-75; effective thirtieth day thereafter (Register 75, No. 13).
3. Amendment of subsection (d) filed 5-6-77; effective thirtieth day thereafter (Register 77, No. 19).