The following material is reproduced from the PPSA publication "An Introduction to Pipeline Pigging", and contains the following sections:
(1) configuration pigs, which measure the pipeline geometry or the conditions of the inside surface of the pipe; and
(2) in-line inspection tools that use non-destructive testing techniques to inspect the wall of the pipe for corrosion, cracks, or other types of anomalies.
AGA | American Gas Association |
API | American Petroleum Institute |
ASME | American Society of Mechanical Engineers |
BS | British Standard |
DICA | Direction Des Carburants (France) |
DIN | German Standards |
DNV | Det Norske Veritas (Norway) |
EMAT | ElectroMagnetic Acoustic Transducer |
GRI | Gas Research Institute (US) |
ILI | In-line inspection |
ISO | International Standards Organization |
IP | Institute of Petroleum (UK) |
MAOP | Maximum allowable operating pressure |
MFL | Magnetic-flux leakage |
NACE | National Association of Corrosion Engineers (US) |
NDE | Non-destructive evaluation |
NDT | Non-destructive testing |
NPD | Norwegian Petroleum Directorate |
OPS | Office of Pipeline Safety, a division of the US Department of Transportation (DOT) |
SMYS | Specified minimum yield stress |
TUV | Technischer Uberwachungs Verein (Germany) |
UCD | Ultrasonic Crack Detection |
UT | Ultrasonic testing |
UTWM | Ultrasound Wall Thickness Measurement |
The following are descriptions of imperfections anomalies, defects, and conditions that are found in natural gas transmission pipelines. The definitions have been obtained from different technical references and dictionaries, but have been selected as relating to pipelines. The descriptions are intended to be generic, but may apply to other structures and materials. The ultimate goal is to provide a common language within the pipeline-pigging industry, world-wide.
(b) general internal: metal loss due to chemical or other attack on the steel from liquids on the inside of the pipe. Electrochemical attack can also occur on local cells, but this condition is less frequent.
(c) pit: local concentrated cell corrosion on the external or internal surfaces that results from the generation of a potential (voltage) difference set up be variations in oxygen concentrations within and outside the pit. The oxygen-starved pit acts as the anode, and the pipe surface acts as the cathode.
(d) selective corrosion: a localized corrosion attack along the bond line of electric-resistance welds (ERW) and flash welds (FW), that leads to the development of a wedge-shaped groove that is often filled with corrosion products.
(e) stress-corrosion cracking: a progressive intergranular and/or transgranular cracking that results from a combination of applied tensile stress, cathodic protection currents, and a suitable corrosive environment.
(b) girth weld: cracks in the weld or weld zone of the butt weld that connect sections of pipe.
(c) seam weld: cracks in the weld or weld zone of the longitudinal seam weld of the pipe.
Also see:
1 inch (in) | = 25.40 millimetre (mm) |
= 2.540 centimetre (cm) | |
= 0.0254 metre (m) | |
1 foot (ft) | = 304.80 mm |
= 30.480 cm | |
= 0.3048 m | |
1 mile | = 1.6094 kilometre (km) |
1 mm | = 0.0394 in |
1 cm | = 0.3937 in |
1 m | = 39.370 in |
= 3.2808 ft | |
= 0.6214 miles |
1 barrel | = 42 US gallons (liquid) |
= 34.9909 Imperial gallons | |
= 5.6146 cubic feet (cu ft) | |
= 158.9871 litre (L) | |
= 0.1590 cubic metres (cu m) | |
1 US gallon (liquid) | = 0.0238 barrel |
= 0.1337 cu ft | |
= 0.00379 cu m | |
= 3.7854 L | |
1 US gallon (liquid) | = 0.0038 cu m |
= 0.8327 Imperial gallons | |
1 Imperial gallon | = 0.0286 barrel |
= 0.1605 cu ft | |
= 277.4171 cubic inches (cu in) | |
= 4.5460 L | |
= 0.0045 cu m | |
= 1.2009 US gallons (liquid) | |
1 L | = 0.001 cu m |
= 1000.0000 cubic centimetres (cu cm) | |
= 0.2200 Imperial gallons | |
= 0.2642 US gallons (liquid) |
1 mile/hour (mph) | = 0.0167 miles/min |
= 0.0003 miles/sec | |
= 88.000 ft/min | |
= 1.4667 ft/sec (fps) | |
= 1.6094 kilometres/hour (km/h) | |
= 26.8225 m/min | |
= 0.4470 m/sec | |
1 kilometre/hour (km/h) | = 0.01667 kilometres/minute |
= 0.0003 kilometres/sec | |
= 16.6667 m/min | |
= 0.2778 m/sec | |
= 0.6214 mph | |
= 54.6800 ft/min | |
= 0.9113 ft/sec | |
1 ft/sec | = 0.6818 mph |
= 1.0973 km/h | |
= 0.3048 m/sec | |
1 m/sec | = 3.6000 km/h |
= 2.2369 mph | |
= 3.2808 ft/sec |
1 pound (lb) | = 0.4536 kilograms (kg) |
1 kg | = 2.2046 lb |
1 barrel | = 349.9860 lbs |
= 158.7512 kg | |
1 US gallon | = 8.337 lbs |
= 3.7820 kg | |
1 Imperial gallon | = 10.0122 lbs |
= 4.5420 kg |
1 cu in | = 0.283 lbs |
= 0.128 kg | |
1 cu ft | = 489.0 lbs |
= 221.8 kg | |
1 cu cm | = 0.008 kg |
= 0.017 lbs | |
1 cu m | = 7810 kg |
= 17300 lbs |
1 ft head water @ 60°F | = 0.4335 pounds/square inch (psi) |
=0.0305 kilogrammes/square centimetre | |
= 0.0299 bars | |
= 0.3048 m of water | |
1 m of water | = 0.1000 kg/sq cm |
= 0.0967 bars | |
= 3.2808 ft of water | |
1 psi | = 0.0689 bars |
1 bar | = 14.5039 psi |
1 Newton | = 0.225 lbs |
1 lb | = 4.448 Newtons |
Flow in a pipeline: | m/sec = (brl/day) / 275d2 |
ft/sec = (brl/d) / 83.82d2 | |
where d = inside diameter of pipe in inches |