The tank must be provided with a system of one or more pressure relief valves which can limit the tank pressure below 115 percent (110 percent if only one pressure relief valve is used) of the design pressure during operational emergency conditions other than fire and below 121 percent of the design pressure during operational emergency conditions that include fire. One of the pressure relief valves must be set to start to discharge at a pressure not in excess of the design pressure of the tank and all other pressure relief valves needed to limit the tank pressure below 115 percent (110 percent if only one pressure relief valve is used) of the design pressure during operational emergency conditions other than fire must be set to discharge at a pressure not in excess of 105 percent of the design pressure. All additional pressure relief valves needed to limit the tank pressure below 121 percent of the design pressure during operational emergency conditions including fire must be set to start to discharge at a pressure not in excess of 110 percent of the design pressure.
The pressure relief valves set to discharge below 105 percent of the design pressure of the tank must have a total relieving capacity in excess of the relieving capacity required to handle operating emergency conditions listed in item A. The total relieving capacity of all the pressure relief valves in the system must be the larger requirement of item A or B.
Where:
W = weight of vapors to be relieved in pounds/hour at relieving conditions
Qa = air flow in cubic feet per minute at standard conditions (60 degrees Fahrenheit and 14.7 psi)
F = fireproofing credit. Use F = 1.0 except when an approved fireproofing material of recommended thickness is used, in which case use F = 0.2
A = total surface area in square feet up to 25 feet above grade or to the equator of a sphere, whichever is greater
Z = compressibility factor of ammonia at relieving condition (if not known, use Z = 1.0)
T = temperature in degrees R (460 + temperature in degrees Fahrenheit of gas at relieving conditions)
M = molecular weight = 17 for ammonia
L = latent heat of ammonia at relieving conditions in Btu per pound
C = constant based on relation of specific heats
(C may be obtained from the following table)
(If K is not known, use C = 315)
K | C | K | C | K | C |
1.00 | 315 | 1.26 | 343 | 1.52 | 366 |
1.02 | 318 | 1.28 | 345 | 1.54 | 368 |
1.04 | 320 | 1.30 | 347 | 1.56 | 369 |
1.06 | 322 | 1.32 | 349 | 1.58 | 371 |
1.08 | 324 | 1.34 | 351 | 1.60 | 372 |
1.10 | 327 | 1.36 | 352 | 1.62 | 374 |
1.12 | 329 | 1.38 | 354 | 1.64 | 376 |
1.14 | 331 | 1.40 | 356 | 1.66 | 377 |
1.16 | 333 | 1.42 | 358 | 1.68 | 379 |
1.18 | 335 | 1.44 | 359 | 1.70 | 380 |
1.20 | 337 | 1.46 | 361 | 2.00 | 400 |
1.22 | 339 | 1.48 | 363 | 2.20 | 412 |
1.24 | 341 | 1.50 | 364 |
Shut-off valves of adequate flow capacity may be provided and used to facilitate inspection and repair of pressure relief valves. If a shut-off valve is provided, it must be arranged so that it can be locked or sealed open and it may not be closed except by an authorized person who must remain there while the valve remains closed and who must again lock or seal the valve open when leaving the station.
Pressure relief valves must comply with items A and B.
Atmospheric storage must be provided with vacuum breakers of adequate capacity to respond to anticipated rates of liquid withdrawal and to rapid atmospheric changes so as to avoid damage to the container. Ammonia gas may be used to provide a pad.
Pressure relief valves used to protect other systems at refrigerated storage installations must discharge to the open air.
Minn. R. agency 105, ch. 1513, SYSTEMS USING STATIONARY, PIER-MOUNTED, OR SKID-MOUNTED ABOVEGROUND OR UNDERGROUND, NONREFRIGERATED STORAGE, pt. 1513.0450
Statutory Authority: MS s 18C.121