Can someone please educate me about Logic configuration of redundant safety integrated systems?

In API 1111 to calculate the buckling check unity factor, an installation safety factor f1 of 3.33 is used. But since for the pipeline parameters under consideration the unity check is more than 1, we would like to take advantage of using a lower safety f...

I'd like to start this discussion regarding the requirements and considerations for the design and installation of equipment in petroleum and chemical facilities. I know there are ways that companies and industry standards give specific requirements, but...

Is it correct to say that since LOPA uses numbers, the results express the precise risk of the scenario?

What are possible safety plans/procedures Operations should consider for offshore environment?