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Federal regulations · Through 2026-08-25 · Newer source version available

46 CFR 154.451: Design vapor pressure.

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Where this section sits in the code
  1. Title 46—Shipping
  2. CHAPTER I—COAST GUARD, DEPARTMENT OF HOMELAND SECURITY
  3. SUBCHAPTER O—CERTAIN BULK DANGEROUS CARGOES
  4. PART 154—SAFETY STANDARDS FOR SELF-PROPELLED VESSELS CARRYING BULK LIQUEFIED GASES
  5. Subpart C—Design, Construction and Equipment

The Po (kPa) of an independent tank type C must be calculated by the following formula:

Po = 196 + AC(ρ) 3/2

where:

A = 1.813 (σm/ΔσA) 2;

σm = design primary membrane stress;

ΔσA = (allowable dynamic membrane stress for double amplitude at probability level Q = 10−8) 53.9 MPa (7821 psi) for ferritic and martensitic steels and 24.5 MPa (3555 psi) for 5083-0 aluminum;

C = a characteristic tank dimension that is the greatest of h, 0.75b, or 0.45 l;

where:

h = the height of the tank or the dimension in the vessel's vertical direction, in meters;

b = the width of the tank or the dimension in the vessel's transverse direction; in meters; and

l = the length of the tank or the dimension in the vessel's longitudinal direction, in meters; and

ρ = the specific gravity of the cargo.

Collected 2026-08-27T02:26:22Z. Source file · JSON

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