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Very Good explanation ✅

Thanks, very informative

Dear Sir, kindly need your permission to download this video for my presentations.. Thanks in advance

Great summarized information for students and curious people about the Oil and Gas Industry. Congrats 👏👏👏👏👏

Thank you

Hi could u please explain how cascade function works with low override function. There are two controllers the output of LV is in % and output of FIC will be in nm3/hr how the low selector will select low value from two diff inputs ?

Offshore oil rig layout at mat jack type rig

Worst voice ever.

Nice explanation, Thank you

very informative

Looks very straightforward

Thanks 👍👍👍👍👍

Good stuff

Awesome content

Thanks for sharing

Useful ❤

where is amine tower ?

very clear presentation

Great, thanks 👍

Nice explanation. Thank you.

It would be easier to understand if you used your own voice!

Very usefull thanks so much.

Thanks very clear explanation well done

Thanks for your videos, why OPsuction is going down from 100 to 80% while the error between SPsuction and PVsuction is positive?

Why you are don't talking about condebser apove the still culomn? Rich gly don't go directly to the surge drum!

Can you share to me the Excel Simulator that you used in this video to me? Or how I can get it?

nice

Thank you for the useful information

I'm watching Understanding PID Control part 4 on MATLAB channel but can't understand what Process gain is. Thank for this video, I got it

Where can I find this tuning simulator ?

I like this.I like it a lot.

hi could you please explain how to get tau D value to get the tightest control without noise?

Glycol filter used activated carbon?

Thank you so much mr, it helps me great 🖐🖐✊

Simple yet very detailed and well explained

Nice descriptive video, please add short description of instrumentation (PCV,LIC,PIC,TT,TIC)

Thanks for your sharing, the information is very useful and easy understanding

Thank you

What it's meant by HHP ?

Kindly provide an feedforward control also

Is it true that control valve direct and reverse action depends on the fail close or fail open condition? if yes, then how to decide control action.

This video is amazing👌,Can you explain what is time constant for second order systems?

Nice explanation. Currently I'm working for the maintenance of Gas Dehydration Unit. So it will more helpful to understand the process system.

Very useful, thank you so much

override control system: two control loops, two inputs (process variables), two outputs; only one of them is selected am I right?

it's my first time to understand it as clearly as that, thanks a lot!

proportional term of PID controller: the change in OP is directly proportional to the change in PV. integral term of PID controller: the change in OP is directly proportional to the accumulated change in PV over a period of time. derivative term of PID controller: used with slow process variables such as temperature so that the controller can act more quickly.

Process gain: the ratio between percent change of process variable to percent change of output. dead time: time needed for the tank level (process variable) to start changing after the valve starts opening (output start changing). time constant: time needed for the tank level (process variable) to reach 63.2% of the total tank level (process variable) change.

Everything okay,what will happen if the PV is less than the setpoint in both controller (Direct &Reverse) you explained about higher PV than setpoint what about lower PV please explain 🙏🙏