Seeking help and cooperation for CAESAR II pipeline stress analysis
Thread Content
I have a question for everyone: regarding LNG storage tanks, since the equipment is equipped with valves as well as various pipes, how should the junctions between these pipes be handled? Is it possible to set fixed supports at the boundary, using this as a design condition without providing specific loads to the system pipes for calculation? If it must be provided, since it is a low-temperature pipeline, only stress analysis can be carried out. Professionals who are interested may contact me; it doesn’t matter whether they are from a company or an individual. I’m waiting online.
If the storage tank is fixed with foot screws, the equipment nozzle serves as an anchor.
If it can be designated as a national standard, they can be separated. Each specific issue needs to be analyzed individually; factors such as pipe diameter and bracket type must all be taken into consideration. Therefore, everything needs to be taken into consideration: whether it can be divided and how it should be divided.
Would you like to know about the interfaces between CAESARII and SP3D, PDMS, AutoPipe, as well as interface file handling? As well as full-featured software for stress analysis; you can search using the following title: “ProAS-CII pipeline stress analysis tool for perfect data processing of stress interfaces when interfacing with PDMS and SP3D files” or via the following link: https://bbs.hcbbs.com/thread-3281766-1-1.html (Source: Haichuan Chemical Industry Forum)
It’s worth exploring, worth learning*:victory: