Expansion Loop Design and Calculation Details
We'll discuss the technical details of this important component and empower engineers with the knowledge to design effective expansion loops. We'll provide expert tips and tricks based on industry experience to optimize the performance of expansion loops. Join us as we explore the expansion loops and enhance your understanding of piping systems.
It is important to perform a flexibility check on the lines situated on long pipe racks, especially for pipes that transport fluids with high temperatures. These lines tend to cause excessive expansion at the end of the pipe racks. To prevent or control this expansion, a line stop is essential at the center of the line or the native zero point of the line where the expansion is zero.
After that, you need to inspect the expansion distance at the end of the pipe racks. If the expansion at the far end of the pipe rack is enough to handle, the length of the pipe shoe should be kept longer to accommodate thermal expansion growth. However, if the expansion is too long, you should consider a design that includes an expansion loop.
Also, it's important to take into account the flexibility of the branch connections, especially at the far end of the racks. If the main line's expansion is high, you may need to reconsider the branch connection design to make it more flexible or install an expansion loop. If you have multiple branch connections, this could end up being quite costly for you. It is preferable to use an expansion loop on the main line instead.
In some cases, you can consider using an expansion loop to account for occasional forces, especially seismic loads. In case the seismic loads on the stopper support are high, we can divide the load by using an expansion loop on the rack.
When designing an expansion loop, consider all the lines that require an expansion loop should be located close to each other. The largest expansion loop must be located outside the other loops with less growth.
Expansion Loop Calculation
Let’s have an example;
D=24” L=42m Tope=343 C Tamb=-17 C H=? W=?
Once we put the figures in the formula we will figure out that the results are as below;
H=9,141.5m
Wmax=13,702m
Comparing the existing length (42m) with the calculated expansion loop sizes, we can see that the height is too long. The H value should be close to the pipe rack width.
We should add one more expansion loop to reduce the height of the loop. This means that the length will be reduced to half.
Let’s look at the result if the pipe rack width is 6 meters;
L=21m (two expansion loops considered so, the length of the two anchor points is reduced to half)
Result: H=6.5m Wmax=9.7m Wmin=3.23m
So, Two expansion loops are sufficient for a 6m wide pipe rack, otherwise we need additional structure to support the expansion loop.
You can read the blog related to Pipe Supports and Restraints from the link.
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This blog is intended as a guide to determining the minimum safe spacing of plants and equipment in Oil Refineries, Petrochemical Complexes, and similar installations.
The spacing recommendations will apply in the absence of Clients' standards or supplement such standards where necessary. They are based on current industry practice.
The spacing recommendations aim to ensure that available plot areas are used economically without affecting personnel safety or plant vulnerability.