I am asking with reference to the vibrations, and erosion happening on the inlet & exit of the heat exchanger piping elbows. All what our Process Engineers are saying is that there hasn't been any issue on their side.

Please enlist all PetroMarvels in Articles & Publications forum.
That would facilitate commenting.

Any update on the release?

PetroStreet wrote: 19 Feb 2026, 09:20 We have been working on a product card for the initial release which is under development, and soon you will hear from us here, and on clampox.com.

Now just to have a quick understanding...

That is something you do when validating the corrosion control program as well including:
Corrosion inhibitor injection systems
Filming amines / neutralizers
Oxygen scavengers

Coupons are required to confirm before injection (worst case) and after injection (effectiveness).

Process engineers,
How can one know if the flow across the tubes of a heat exchanger is turbulent in nature?
Point me towards the reliable engineering calculations /equations to estimate that.

Dlew,
You may want to consider a very good course here:
https://www.udemy.com/course/piping-eng ... hatgpt.com
Would cost you $19.99 damages with some 11 hrs+ learning experience.
Suggested to me by one of my young colleagues.

Look what I have got!
Listing in a way that you print and put it in your office for quick reference.

You can get this: https://www.sciencedirect.com/science/a ... 071630574X

Temporary repairs are required to be managed very well.
Internal thinning, damage mechanism is active all throughout and with no finite time of converting that to a permanent one would actual pose a risk.
Corrosion rates, associated piping inspection, localized monitoring, there are quite a lot of ...