Facilitating a HAZOP #2 (Hazard and Operability Studies)

[@OG-kc4nw]

This is the best video I have ever encountered in Safety Engineering! Thanks!! From Perth, Western Australia :)

[@tilekshektibayev8717]

Great video, very informative! Please, keep it up, waiting for your other explanations on HAZOP

[@nomsoanyatonwu1728]

fantastic job bro, keep it up

Thank you very much Mr. Tobi for sharing your knowledges, it help us a lot to better understand the techniques and improvements our skills....i just watched your video about the PHAST software......and wanted to ask you if you going to make another videos in order to deepen understanding this wonderful software PHAST and SAFETI..It would be great for us, because there are few information about it...any way..congratulation for your job..excelent!

[@GeniusProcess8051]

Great job Tobi! well done!

[@varunpandya2938]

Nice explained

[@gregoriyrogerg6296]

Hi, Tobi! Thanks a lot for this video! I wanna add a couple of questions about this P&ID. What is the reason to install PSV on a discharge line of the pump? We can simply use a pump with discharge pressure less than discharge line strength. For this case, for example, we need discharge pressure about 25 m of water column, so if we use a line with design pressure 6 bars, nothing happens to the line. This is much easier and cheapper. What do you think? And taking this into consideration we can ask: what is a reason to control pressure at the entrance of T-5301? We've already decided to use a pump with low discharge pressure, so if we take away all hydraulic losses between the pump and T-5301 from the pump head, we get just a low value of pressure before T-5301. Taking into account the size of this tank, we can be sure that nothing happens to it. What is your opinion?

[@AliAli-eu6oy]

Excellent

[@jieyangxu2453]

legend！

[@FazliddinNurmagomedov]

Hi, Tobi. Where is part 3 of this video?

[@rasheedyusuf4396]

Please how can I reach you ?

[@salemrachdi8704]

Hi, HAZOP #3 & 4 please