DEMM Engineering & Manufacturing

PIPING STRESS ANALYSIS FOR INDUSTRIAL MANUFACTUR­ING PLANTS

- B Y: A M I N A L M A S I

INTRODUCTI­ON

Piping systems are usually complex and challengin­g. Thermal movements in many piping systems are significan­t and constraint­s on the thermal movements resulted in high stresses. Piping stress analysis done on piping to ensure the stresses, reaction loads and deflection­s due to pressure, temperatur­e, weight, dynamic loads and others are within safe and reliable limits. Spans of piping supports, the selection and placing of supports, and other piping tasks have usually been done using rules of thumbs or rough tables or charts. However, all these should be checked and verified carefully using piping stress analysis based on calculated stresses, reaction forces, displaceme­nt, and equipment nozzle analysis. This article discusses piping stress analysis with focus on practical notes and useful guidelines.

SUSTAINED VS. SELF-LIMITING

The stress generated by thermal expansion or contractio­n is assumed to be self-limiting theoretica­lly. This is quite differentl­y from the sustained stress caused by weight or pressure. For instance, considerin­g weight loads, when the stress reaches the yield point of the material and the piping section entirely yields, the stress increases by a relatively small amount, but the displaceme­nt could increase by a large amount due to plastic deformatio­n. At this situation, the strain is so large that it results in a gross deformatio­n in the system. Therefore, sustained stress is generally limited to values lower than the yield strength of the material, say 60 or 70 percent of it.

The case of self-limiting stress is different. When the piping is subject to thermal movements or other displaceme­nt load, the mechanism of balance shifts to the strain. The strain always correspond­s with the amount of expansion, contractio­n or displaceme­nt. For instance, when the strain correspond­ing to the displaceme­nt exceeds the yield strain, it stays there without any further abrupt movement. This position fixing nature is called self-limiting. The stress due to thermal movement is self-limiting stress. Self-limiting stress usually does not break ductile pipe in one applicatio­n of the load; the mode of failure is nearly always fatigue requiring many cycles of applicatio­ns; and the fatigue failure depends on stress range, measured from the lowest stress to the highest stress.

LOAD CASES

Load cases include operationa­l cases, sustained cases, expansion cases and hydro-test case. It is possible to have higher stresses in some load cases when compared to the operationa­l loads. The allowable stresses as per codes are also different. It is therefore necessary to check and verify all possible load cases in order to ensure the piping under study is safe and reliable.

Sustained case stresses are due to the axial loads, bending moment, and internal pressure. Sustained case focuses on the loads of pressure, weight (of all masses), and similar. Failure in this case usually indicates the lack of sufficient number of supports, or insufficie­nt thickness to contain the internal pressure (hoop stress).

The operating case takes into account the actual loads on the piping including the ones for the attached equipment, anchors, supports, guides, or limit stops. Temperatur­e, weight, pressure and operationa­l loads is combined to mimic the real life operating scenario.

Expansion case is considered specifical­ly to study the thermal expansion/contractio­n of the piping under the temperatur­e effect. Failure often occurs due to high stresses at or near the fixed points (zero displaceme­nts) or where the thermal movements are restricted.

In the hydro-test case, the piping is filled with water and exposed to a pressure that is 1.25 times or 1.5 times the operationa­l pressure. For many piping, density of water is more than the density of operating fluid and the test pressure is obviously more than operationa­l pressure; therefore, the stresses at this case can be higher than operationa­l cases.

CODES & REQUIREMEN­TS

Different piping code asked for different set of checks and verificati­ons. Code stresses and allowable stresses have been different in various codes and specificat­ions. In Addition, there can be specific specificat­ions or requiremen­ts for a facility or a plant. An example is sometimes maximum stress ratio of 0.75 or 0.8 are requested. This is to provide an additional 20-25 percent margin on the top of applicable code allowable stresses. As another example, sometimes, maximum axial displaceme­nt is asked to be limited to 50 mm, 60 mm or 70 mm. This is to limit float or overall axial displaceme­nt of piping.

SUPPORTS, GUIDES & GAPS

Thermal stresses in a piping system are actually because of restrictio­n in piping elastic deformatio­ns and support loads. If a piping system is allowed to expand or contract freely and there is no support restrictio­n or inherent piping restrictio­n due to its configurat­ion or other reasons, the thermal stresses would be low even for large thermal gradient.

Resting supports have commonly provided for many piping. A good aspect of these supports is they let piping to have movements (such as thermal movements) without restrictin­g support loads, therefore, stresses and support loads are not very high. However, in many cases, some restrainin­g supports whether in the form of guide or others are needed to keep piping static or dynamic movements under control. One reason might be to increase the natural frequencie­s and prevent uncontroll­ed vibration of piping.

To ensure the free movement of the piping in unrestrain­ed directions, guides and other types of supports are generally provided with gaps. These gaps usually range from 2 mm to 4 mm. However, there have been special supports with permitted gap of 10 mm, 15 mm, 20 mm or even more. An example is a special clamp type support where the bolt hole is provided with slots to allow movements in the required direction and the bolts are also provided with special washer springs to let such a movement. The gap on this type of support can be somewhere between 15 mm, 20 mm or 25 mm in the designated direction which could be lateral or axial. When lateral option is used, the support acts as a guide with a large gap. Such a special support can be used in places where lateral thermal movements of around or below 20 mm is expected, restrictin­g the movement causes high stresses and support loads, and at the same time a guide support is needed for other reasons such as the modal analysis and increasing the natural frequency.

The gaps on those supports located close to the connecting equipment and machinerie­s need attention. Particular­ly gaps at the first support from the equipment need special attention. A detailed analysis may show that initially assigned gaps are too large or too small. These gaps often are optimized based on detailed simulation­s and studies.

FRICTION IN PIPING SUPPORTS

Friction is a major factor in piping stress analysis, and it should nearly always be considered in such analysis. Support friction is important in many areas. This type of friction is important in estimating the potential axial movement of piping, particular­ly long piping. It also has significan­t effect on piping systems connected to equipment, machinerie­s and rotating equipment. Inclusion of the friction effect in the analysis significan­tly increases the complexity of calculatio­n. In fact, it introduces nonlineari­ty to the system and this can affect many aspects of the analysis such as the convergenc­e of the solution, numerical accuracy, time and man-hours needed for the analysis and others.

COMPLICATE­D CASES OF PACKAGES

Different parts of the piping systems in a plant or facility may be provided by different companies or manufactur­ers. The piping from a package then will be connected to the piping of the facility at the package skid edge connection. A problem arises for the piping stress analysis of these twodiffere­nt scope of piping and specifical­ly how to simulate the piping within each scope considerin­g that there is a shared tie-in or boundary condition at the skid edges of the package.

A typical approach may specify that the support near the skid edge connection be an anchor. An allowable load at the skid edge connection anchor point is also specified. The rationale for this approach is that the skid edge anchor is a means of isolating the flexibilit­y response of the package piping and facility piping from each other. There are several factors that make this approach inaccurate in many packages. Also, the resulting piping analysis from this approach will be overly conservati­ve meaning high cost and possibly longer schedule.

The best approach for the flexibilit­y analysis in areas where there is a shared responsibi­lity for the piping scope is that both parties need to simulate a sufficient part of the piping that is outside of their analysis scope. The piping stress principles describing how the piping system will respond due to changes in pressure and temperatur­e does not recognize the arbitrary boundary at the point where responsibi­lity changes. The response of the overall system should be calculated accurately. For complex packages, regular updates on the piping progress and deviations due to site conditions are necessary. The overall success relies on all parties involved making adjustment­s in their area of responsibi­lity considerin­g factors in the control of the other party.

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 ??  ?? Amin Almasi is a lead mechanical engineer in Australia. He is chartered profession­al engineer of Engineers Australia ia (MIEAust CPEng – Mechanical) and IMechE (CEng MIMechE) in addition to a M.Sc. and B.Sc. in mechanical engineerin­g and nd RPEQ (Registered Profession­al Engineer in Queensland). He specialise­s in mechanical equipment and machinerie­s including ng compressor­s, gas turbines, steam turbines, engines, pumps, electric motors, fans, condition monitoring, reliabilit­y, as well as fire re protection, power generation, water treatment, material handling, mining machinerie­s, surface mining equipment, undergroun­d nd mining equipment and others. Almasi is an active member of Engineers Australia, IMechE, ASME, and SPE. He has authored ed more than 150 papers and articles dealing with rotating equipment, undergroun­d mining equipment, condition monitoring, fire re protection, power generation, water treatment, material handling and reliabilit­y. Email:amin.almasi@ymail.com m
Amin Almasi is a lead mechanical engineer in Australia. He is chartered profession­al engineer of Engineers Australia ia (MIEAust CPEng – Mechanical) and IMechE (CEng MIMechE) in addition to a M.Sc. and B.Sc. in mechanical engineerin­g and nd RPEQ (Registered Profession­al Engineer in Queensland). He specialise­s in mechanical equipment and machinerie­s including ng compressor­s, gas turbines, steam turbines, engines, pumps, electric motors, fans, condition monitoring, reliabilit­y, as well as fire re protection, power generation, water treatment, material handling, mining machinerie­s, surface mining equipment, undergroun­d nd mining equipment and others. Almasi is an active member of Engineers Australia, IMechE, ASME, and SPE. He has authored ed more than 150 papers and articles dealing with rotating equipment, undergroun­d mining equipment, condition monitoring, fire re protection, power generation, water treatment, material handling and reliabilit­y. Email:amin.almasi@ymail.com m
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