Reference Proper Pigging  ·  HydroTech Testing Services

Reference

Formulas, constants, and definitions

Appendix B and Appendix D, published openly, with calculators that carry the same arithmetic.

Plate VI
window segment 1 segment 2 segment 3 elevation
Plate VI. Segment-break screening. The allowable elevation range slides along the profile, and a new test segment begins wherever the window is exhausted. In the worked gas example the window is 203 feet.
Plate VII
−40 °F drying time outlet dew point soak rebound
Plate VII. Drying reads as a falling outlet dew point punctuated by soak-test rebounds. Post-soak rebounds should diminish as removable moisture is reduced; final acceptance requires the drying to cross the criterion and the final post-soak reading to remain within it.

B.1Core relations

Hoop stress
S = P D / 2t  →  P = 2 S t / D
Internal area
A = π (D − 2t)² / 4
Fill volume
V = L × A, field form V ≈ 0.0408 d² L in gallons
Hydrostatic gradient
ΔP = 0.433 × SG × Δh, fresh water SG = 1.0
Pressurisation volume
ΔV = V ΔP [ (D/(Et))(1 − ν²) + C ]
Pressure-temperature
ΔP = ΔT [ γ − 2(1 + ν)α ] ÷ [ (D/(Et))(1 − ν²) + C ]
Real-gas law
PV = ZnRT, R = 10.7316 psia·ft³/(lb-mol·°R)
Elastic PV slope
dP/dV = 1 ÷ ( V [ (D/(Et))(1 − ν²) + C ] )

B.2Constants

Table 2. Constants and properties. Steel properties are taken as constant; water properties are temperature dependent and must be read at the test temperature.
QuantitySymbolValueNote
Young’s modulus, steelE29 × 10⁶ psiconstant
Poisson’s ratio, steelν0.3constant
Linear expansion, steelα6.5 × 10⁻⁶ /°F= 1.17 × 10⁻⁵ /°C
Compressibility of waterC≈ 3 × 10⁻⁶ /psitemperature dependent
Volumetric expansion, waterγ≈ 1.3 × 10⁻⁴ /°Fnear 68 °F; near zero at 39 °F
Fresh water gradient—0.433 psi/ftmultiply by SG
Molecular weight, nitrogenMW28.01 lb/lb-molN₂
Standard conditions—14.7 psia, 60 °F14.73 psia also in tariff use

B.3Regulatory anchors

Verify against the current text of the Code of Federal Regulations before use.

49 CFR 195.304
Liquid test at not less than 125 percent of MOP for four continuous hours, plus four hours at not less than 110 percent if the line is not visually inspectable.
49 CFR 192.505
Gas strength test held at least eight hours where operating stress is 30 percent SMYS or more, at the class-location test factor.
49 CFR 192.503
Maximum hoop stress permitted during gas-medium testing, by class: natural gas 80/30/30/30; air or inert gas 80/75/50/40.
49 CFR 192.506
Spike hydrostatic pressure test, added by the 2019 gas transmission rule.
49 CFR 195.306
Conditions under which alternative test media are permitted on liquid lines.
192.517 & 195.310
Test records, retained for the life of the pipeline.

Glossary and calculators

Thirty-five terms, from air lock to tracer gas, defined as a test crew uses them. The calculators carry the relations above, and the same arithmetic is available offline in the HydroTech Pocket Engineer application.

Glossary, A to Z Calculators The Pocket Engineer