Piping Stress Analysis (PSA Group)
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Piping & Pipeline Stress Analysis
Piping Stress Analysis Training
CAESAR II Static Training
CAESAR II Dynamic Training
Special Support Design by FEA
Special Item Design

E-mail: ir.psa.co@gmail.com
Tel: (+98)912 816 2070
@Akbar_Daneshvar
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Input Echo:
The input echo allows the user to select which portions of the input are to be reported in this output format. All basic element data (geometry), operating conditions, material properties, and boundary conditions are available in this report option.

Miscellaneous Data:
This report displays the Allowable Stress Summary, Bend Data, Nozzle Flexibility Data, Pipe Report, Thermal Expansion Coefficients used during analysis, Bill of Materials, the Center of Gravity Report, and Wind and Wave input data.

Warnings Report:
All warnings reported during the error checking process are summarized here.
Supporting of piping on Pipe Racks and Pipe Ways involves providing rest, guides, limit stops and anchors in a piping header.
Guides ⬇️

Guides on a pipe header shall be arranged as shown in following diagram.
supporting_pipe_rack_header_with_expansion_loop.jpg (696×181)
supporting_pipe_rack_header_without_expansion_loop.jpg (696×212)
Notes : ⬇️⬇️

1. “L1” is the minimum length necessary to permit the piping maximum thermal expansion of 120 mm.
2. “B” is the dimension of loop as per stress analysis.
3. Pipe racks and pipe ways usually have spans of 6 to 8 Meters.
So for pipes 6″ and smaller, guides are required on each main beam.
For pipes more than 6″ NPS, guides on alternate beams can be provided.
Rest Supports ⬇️⬇️

Maximum distance between supports shall not be higher than allowed particular material of construction at particular operating conditions. Refer company standards for the same.

1. Maximum allowable spans for metallic piping.
2. Maximum allowable spans for Cupro-Nickel Piping.
3. Maximum allowable spans for Plastic Piping.
Sloped Piping ⬇️⬇️

For all pipes which require a slope towards a definite direction, the max allowable span should be such that max deflection of pipe is less than the level difference between two adjacent support points, in order to avoid pockets.
Supporting Small lines from Big Lines ⬇️⬇️⬇️

For small bore piping, intermediate supports from adjacent large bore piping may be required as an allowable span for small bore piping can be is less than the distance between two consecutive supports.

Following figure shows how larger lines in a pipe rack are used to support a group of smaller lines that may not be adequately supported because of the bent spacing.
intermediate-pipe-support.png (328×117)
The un-insulated line is U-bolted to the supporting steel; the insulated line has its shoe welded to the steel.

The smaller lines then rest on the steel. When an insulated line is used for support, the growth of the line at the proposed support point must be checked. Its growth could become restricted by this type of support, and it may be better to use another line for this application.

The adjacent pipe chose as a supporting pipe must have diameter at least three sizes greater than the supported pipe, and never less than 4″.
Example : ⬇️⬇️⬇️

# Supporting Pipe : 4″ / 6″ / 8″
# Corresponding Supported Pipe : 1.5″ / 2″ / 3″

Using Dummy Support

Following figure shows the correct way to support a line that has exceeded its allowable span.
pipe-rack-dummy-support.png (472×202)
A common mistake is to extend the 10-in process line over the rack bent and cap it, when the line should have been run as if a support problem did not exist.

A smaller piece of pipe or dummy leg could then be welded to the elbow for support (a hole should not be cut in the process line).
Supporting of Pipes of a Distillation Tower ⬇️⬇️⬇️
supporting-of-pipes-of-a-distillation-tower-768x402.jpg (768×402)
Supporting of pipes on a distillation tower is a critical activity involving stress analysis of almost all lines. Following points must be taken care of while supporting pipes of a distillation tower.
Piping shall be grouped as far as possible for the ease of supports. Piping shall be supported from cleats welded on the vessel as far as possible. Proper guides at recommended intervals shall be provided for long vertical lines.

Piping support cleats for safety valves shall be independent meant for safety valves only & shall be designed considering impact loading during popping off. Utility Connection nozzles shall be from side/top.
The stress analysis requirements for supports and guides in piping connected to distillation towers and vertical vessels are as follows : ⬇️

1. The rest support must be as close as possible to nozzle. If there is a horizontal spool immediately adjacent to the nozzle, the rest support will be done shown in the sketch below.
2. The guides along the vertical run will be spaced as shown in the sketch below.
3. Ease of erection is also to be considered when positioning and spacing the guides, therefore it will be useful grouping the guides for a number of pipes at a common elevation. This criteria is valid also for columns with reinforcing rings, whereby positioning the guides on the rings, it is not necessary the welding on the shell.
4. For larger diameter piping (NPS >= 16″) standard distances between the guides are not established since support system is generally based on the stress analysis requirements.
Vertical_Vessel_Pipe_Supports.jpg (457×617)
caesar-tutorial-1.pdf
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caesar-tutorial-1.pdf