## RathGibson

## Technical Info

RathGibson is continually striving to bring our customers tubing and pipe to fit the most specific needs.

## Sizes, Gauges, and Weights

## Testing

RathGibsonâ€™s products undergo comprehensive quality testing. When you choose a RathGibson product, you can be assured that it is of the highest quality. Learn More

## Glossary

Tubing and pipe glossary of terms. Learn More

## Pressure Data

### Collapsing Pressure for Tubing Subject to External Pressures

ASTM tubing and pipe specifications do not include any recommended service or collapsing pressure for tubes subject to external pressure. The formulas below were developed to predict lap welded tubing failure due to external pressure by R. T. Stewart (Dean of the Mechanical Engineering department of the University of Pittsburgh). The predictions are reported to be accurate if the tube length between supports is greater than 6 times the diameter.

Lap welded tubing would normally be expected to fail before butt welding tubing due to the inherent bending moment created by the lap joint. This moment will not exist for butt welded tubing. Working pressures or allowable pressures are arrived at using a safety factor (SF) to reduce the pressure from a level where collapsing failure is very likely to where an acceptable level of risk is achieved. This is a complex matter in which many issues must be considered such as: personnel hazard assessment and general safety; corrosion; fatigue; fabrication changes (bends, flares); codes and insurance; seismic stability; and temperatures, to name a few. A number of these issues are addressed in a free publication (NÂ° 9024) from the Nickel Development Institute (NiDI). These formulas are merely a tool for estimation or prediction under ideal conditions near room temperature. Note that actual values may vary from these theoretical calculations for a number of reasons. Tubing that is out of round for any reason would be expected to fail prematurely relative to ideal circumstances or estimates.

A significant source of real-world collapsing type failures is thermal distortion caused by partial filling (or ID boiling) in horizontal tubulars in a heat exchanger environment. This type of situation can cause failures even with positive internal pressures, making these calculations moot.

It is interesting to note that material strength is not a factor in these formulas; this is common for buckling type calculations or predictions.

Actual wall thickness or conservative wall estimates should be used. For example 16 gauge or 0.065" average wall tubing is likely to measure 0.060" thick, or near the low end of the allowable range. Actual pipe ODs should be used rather than Nominal Pipe Sizes (3 nps is nominally 3.5" OD).

##### Machinery's Handbook 25, page 271

P = 86,670*T/OD - 1386 for P > 580 psi

P = 50,210,000*(T/OD)3 for P < 580 psi

**Where:**

P = Theoretical OD Collapsing Pressure (psi)

T = Wall Thickness (in)

OD = Outside Diameter (in)

SF = Safey Factor (generally 1.5-10, 1 for collapsing pressure)

## Bursting or Working Tubing or Pipe Pressures

### Barlow's Formula

ASTM tubing and pipe specifications do not include any recommended service or burst pressure requirements. However, Barlow's formula is commonly used in the industry to approximate or predict the bursting pressures of ductile thin wall tubular [(Wall/ID) < 0.1] or cylindrical materials due to ID pressurization, and generally yields conservative results or predictions. Other calculations are appropriate to heavy wall and brittle materials.

Working pressures or allowable pressures are arrived at using a safety factor (SF) to reduce the pressure from a level where bursting failure is very likely to where an acceptable level of risk is achieved. This is a complex matter in which many issues must be considered such as: personnel hazard assessment and general safety; corrosion; fatigue; fabrication changes (bends, flares); codes and insurance; seismic stability; and temperatures, to name a few. A number of these issues are addressed in a free publication (NÂ° 9024) from the Nickel Development Institute (NiDI). Barlow's formula is merely a tool for burst estimation or prediction under ideal conditions at room temperature. Note that actual values may vary from these theoretical calculations for a number reasons.

Many engineers will use the ultimate tensile strength (UTS) to calculate a bursting pressure estimation and use the yield strength (YS) and a safety factor (SF) when arriving at a working pressure estimation. Using the yield strength and no safety factor (SF=1) will calculate an approximate theoretical pressure at which the tubing will begin to plastically deform.

Actual wall thickness or conservative wall estimates should be used. For example 16 gauge or 0.065" average wall tubing is likely to measure 0.060" thick, or near the low end of the allowable range. Actual pipe ODs should be used rather than Nominal Pipe Sizes (3 nps is nominally 3.5" OD).

##### Barlow's Formula:

P = (2*S*T / OD*SF)

**Where:**

P = ID pressure (psi)

T = Wall thickness (in)

OD = Outside Diameter (in)

SF = Safety factor (generally 1.5 â€“ 10, 1 for collapsing pressure)

S = Material strength (psi)