Hi, how do you monitor and confirm the concentration of TEG both lean and rich?

Please i need this process flow sheet

Sir, where will be pressure drop take place. Kindly explain that. Because from dehydration column rich TEG 30°C 30 bar, after the control valve suddenly the pressure drop to 5bar how, from where it drop. Kindly please explain.

thank you for this educational video ^^

Superb 👍

Very good for learning!

i have a doubt, how fuel gas absorb water particles

Wonderful Sir .

Excelent! Thank you!

Nicely explained 🎉

Very informative video. Thanks Nick!

Hi Nick , thanks for your support and my. Question is wether we can add or subtract the friction loss in discharge, I think we can add friction loss in discharge....

What do we do IF we set 99.5 % wt of TEG to be used as an absorbent in the ABSORBER COLUMN? Would you happen to have any advice?

P discharge should be p statuc plus pressure drop

Hi nick. Appreciate if you could do this kind of explaination on other system as well (fuel gas system, compression system, gas dehydration system, etc)

You have said 1 bar is equal to 10.2m but in NPSHa calculation you are mentioning 10.2m for 0 bar

Very informative ❤❤❤

1atm is 0 barg is that correct

Addition of ∆P in Discharge pressure required😊

Hi, Mr.Nick How to know if the pump requires minimum recirculation line? I don't understand clearly. I have this idea that this minimum recirculation line is related to turndown ratio advised by vendor. Could you explain clearly?

Thank you for this video

Great. Thanks Nick

A very good explanation. Thank you Nick.

nice biriyani 😀

Nicely explained.

Thank you Sir for your super teaching and informations in this video... You clarified many points in my mind in the Gas dehydration Unit

u have whtassap numnber

Please help me explain where the Fuel gas flows when it absorbs water from the stripping column @all

Hi Nick. Thank you very much for your video. I have a question, if i put a pressure gauge at a suction side of the pump. If I substract the vapor pressure of the liquid from the reading of pressure gauge will I get NPSHA? Thank you again.

Thank you for your thourough and excellent work

Thank you

clear and detailed lecture. thank you.

Very nice explanation, thank you

I love the way you explained the whole process and broke it down to a layman's understanding. Wonderful, I must say! 👏👏👏

Kim Jong-un

Any video to explain gas dewpointing please

Hi. If we have pressure gauges on an existing system on the discharge and the suction, we can just look at them right? We don't need to calculate, am I understanding it correctly?

Thank you brother. Very nice ❤❤❤

Please share more

Very nice explanation brother ❤

Very nicely explained in a simple manner, I use it for training junior operators. I request if you can do one for gas sweetening.

The water can deliver at 50m Head from a pump, if we can use glycol instead of water in the same pump. Is any variation in head

Is NPSH calc applicable for closed loop systems? I only saw open loop examples and nothing for closed system

Hi all, anyone has an excel sheet for pump sizing they can share? Thanks

tnx good

Thanks

Hi Mr. Nick !!! Greeting's. How come vessel operating under atm press became 10.2 bar G pressure in your calculation?

so good thanks

Good day sir. I really appreciate your video. I was wondering if I could contact you and ask a few questions because I’m considering doing something like this for my final year research project. I saw somewhere that nitrogen gas can be used for the stripping of almost lean glycol and I wanted to ask if other mostly inert gases like co2 or Ar could be used in the stripping column

Iam now Fully understand how this system works iam new to oil and gas, your explanation like a professor. Aneongaseo