Saturday, July 21, 2018

PURPOSE OF PIPE SUPPORTS: A small article for beginners

For proper working of the piping system it has to be supported properly. The major purpose of pipe support is described below:
  • TO SUPPORT WEIGHT OF PIPE-DURING OPERATION & TESTING:
Supports are required to support the line during all conditions i.e. during operation as well as during testing. In case of vapour line this difference will be very large due to hydro testing. Supports should be designed for this load (unless otherwise decided in the project). Sometimes line is capable of having longer span but load coming on the support may be very large (especially with large diameter pipe lines). Then to distribute the load uniformly, more number of supports should be provided with smaller span. Note: 1. it may be noted that during testing condition there is no thermal load. 2. All spring supports are locked during testing.
  • TO TAKE THE ‘THERMAL OR EXPANSION LOAD’:
Whenever thermal expansion is restricted by support, it introduces additional load on the support. Support restraints must be designed to take this load in addition to all other loads.
  • TO TAKE THE ‘ OCCASIONAL EARTH QUAKE LOAD’:
The earthquake is normally associated with horizontal acceleration of the order of 1 to 3 m/sec2. This is around 10% to 30% of the gravitational acceleration and introduces horizontal force of about 10 to 30% of the vertical load (or supported mass). While designing support this should be taken care.
  • TO TAKE ‘HYDRAULIC THRUST IN PIPING’ :

The hydraulic thrust (Fig. 1) in the pipeline is present at certain point such as pressure reducing valve, relief valve, bellows etc.
If the control valve has large pressure differential and line size is more, then this force can be very high.

Figure showing thrust force

Fig. 1: Figure showing thrust force
The support should be provided and designed to take this load, otherwise this will load the piping system and may cause failure.
  • TO ABSORB ‘VIBRATION OF PIPING SYSTEM’ :
When the pipe is subjected to moving machinery or pulsating flow or very high velocity flow, pipe may start vibrating vigorously and ultimately may fail, particularly if span is large. To avoid this it may be required to introduce additional supports at smaller span apart from other requirements. It may not take axial load, but must control lateral movements.
Wind introduces lateral load on the line. This load is considerable especially on large diameter pipes and increases as line size is increased. This load tends to sway the line from its normal position and line must be guided properly against it to avoid any kind of malfunction. In case of large diameter overhead lines, supported by tall support extended from floor, wind load introduces large bending moment and should be considered critically.
  • TO SUPPORT THE SYSTEM DURING ‘TRANSIENT PERIOD OF PLANT AND STANDBY
CONDITION: Transient condition refers to the start-up or shutdown condition in which one equipment may get heated up faster and other one get heated slower. Due to this the expansion of one equipment which in normal operation will get nullified, may not get nullified and exert thermal load on supports.


Operating- Standby Condition
Fig. 2: Operating- Standby Condition
Standby condition is also similar. If there are two pumps, one being standby and both connected in parallel (as shown), design and operating temperature of both the connections will be same. But the expansion of two parallel legs will not be nullified because at a time only one leg will be hot and another being cold.
  • TO HAVE ‘NOISE CONTROL’ :
In most of the plants, noise is resulting from vibration and if such vibrations are controlled, noise is reduced to great extent. In such lines, between clamp (i.e. support) and pipe, asbestos cloth is put to absorb vibration and avoid noise.
Noise due to pulsating flow can be reduced by using a silencer in the line. Still if it is not below acceptable level acoustic enclosure may be used. Insulation over line also helps in reducing the noise.
  • TO SUPPORT THE SYSTEM DURING ‘MAINTENANCE CONDITIONS’ :
When for maintenance certain equipment or component like valve is taken out, remaining system should not be left out unsupported.


Figure showing support addition during maintenance activities
Fig. 3: Figure showing support addition during maintenance activities
Referring to the FIG-3, support ‘S1’ will be sufficient but when valve ‘V1’ is taken out for maintenance there will not be any support for vertical leg. Therefore second support ‘S2’ may be required to take care of such condition.
  • TO SUPPORT THE SYSTEM DURING ‘SHUTDOWN CONDITIONS’ :
In shutdown condition all equipment may not be in the same condition as in operating condition. For example, refer the pump discharge line in FIG-4, Point A is resting, Point B & C are spring supports and Point D is the pump discharge nozzle. The springs are, designed based on weights considering the weight of fluid as well as pipeline and thermal movements. But during shutdown condition the fluid may be drained and the pipe becomes lighter. Hence the spring will give upward reaction and shall load the nozzle ‘D’ beyond permissible limit.


Use of Limit elements in spring during shut down
Fig. 4: Use of Limit elements in spring during shut down
In this case a limit stop is used which will not allow the Point C to move up above horizontal level. (However it will allow downward movement during operating condition).
  • TO SUPPORT THE SYSTEM FOR ERECTION CONDITIONS :
Erection condition can be different than the operating condition which should be considered while designing supports.
For example for normal operation a long vessel supported by three supports, S1, S2 & S3 is shown in FIG-5. If support S2 is higher, than all load will act at S2 only. During erection if level of S2 is lower than entire load will be divided into two supports S1, S2 only. Therefore foundation of S1, S2 & S3 should be capable of taking such conditions.


Vessel supported at three supports.

Fig. 5: Vessel supported at three supports.

A pipe line supported by S1, S2 & S3 taken from vessel is shown in above FIG – 6. During operation there will be no weight at S2 & S3 (as it is only guide), but wind condition will be there. Loads due to such conditions must be considered while designing the supports.


Pipe supported from vessel cleats.
Fig. 6: Pipe supported from vessel cleats.

TO REDUCE VIBRATION AMPLITUDES.

Piping Stress Job Interview questions for you: Part 1

The following list will provide few interview questions asked in different interview for a Piping Stress Engineer post. Hope you will be able to find the answers from ASME B 31.3 and any piping stress text books or from piping hand book. In case you could not find out a specific answer reply in comments section. This is the part one of the collection. Keep checking the website regularly for other parts.
1) How to make critical line list or flexibility log? How will you decide critical line list with help of ASME B31.3?
2) How to decide Stress critical systems for analysis using Caesar II?
3) Which lines can be eliminated from formal Stress analysis?
4) Can you make a typical Sketch & supporting for column piping? How to decide how many load bearing clip supports to be used?

5) Draw a typical Sketch & supporting arrangement for tank farm piping? How tank Piping analysis is different from normal pressure vessel connected piping system analysis?
6) What is SIF? Formulas for In plane, outplane sif for elbow (B31.3)?
7) Value of sif, flexibility factor for Bend?
8) What are the necessary documents required for stress analysis?
9) Why a Spring hanger is used? Can you write the formula for spring HL, CL & variability?
10) What are the different types of supports used in piping systems?
11) What do you know about Expansion joints and thier types? When these come into picture?
12) What are the normal types of load cases? Write the load cases for a typical stress system using static method of seimic and wind?
13) What is slug flow? What parameters are required to calculate Slug force?
14) What are the dynamic restraints? What is snubber and when do you use a snubber?
15) What is the minimum swing allowed in top mounted hanger? What will you do if that amount exceeds in a typical piping system?
16) What is cold pull and why it is used?
17) What is difference between Variable Hanger and Constant Hanger? What is the variability of Constant Spring hanger?
18) What are the inputs required for stress analysis? What do you check in Caesar analysis of a piping system?
19) What do you mean by the term “liberal stress”?
20) What is hot-cold philosophy for pump? Have you heard the term Pump alignment?