Hi, how do you monitor and confirm the concentration of TEG both lean and rich?
@khanzahid397426 күн бұрын
Please i need this process flow sheet
@geraldraja3302Ай бұрын
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.
@vrbaac1641Ай бұрын
thank you for this educational video ^^
@rajamohandass.s96842 ай бұрын
Superb 👍
@nursharmilla53252 ай бұрын
Very good for learning!
@antoebenezar82734 ай бұрын
i have a doubt, how fuel gas absorb water particles
@nimrasiddiq34614 ай бұрын
Wonderful Sir .
@fadlohaddad40004 ай бұрын
Excelent! Thank you!
@Aru_wealth5 ай бұрын
Nicely explained 🎉
@cchandran845 ай бұрын
Very informative video. Thanks Nick!
@raphaelragu6 ай бұрын
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....
@AriesSatriyo-INA-646 ай бұрын
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?
@AriesSatriyo-INA-646 ай бұрын
I meant., how to SET at HYSYS v12.1?
@mojtabaimanfar42676 ай бұрын
P discharge should be p statuc plus pressure drop
@ummifatihahlotffi26696 ай бұрын
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)
@simbusvs22106 ай бұрын
You have said 1 bar is equal to 10.2m but in NPSHa calculation you are mentioning 10.2m for 0 bar
@shreyaskv40096 ай бұрын
In NPSHa calculations he has taken 0barg so that means 1.01325 Bara = 10.2m WC
@firstlookmensworld71277 ай бұрын
Very informative ❤❤❤
@alagusundaramkarthi66057 ай бұрын
1atm is 0 barg is that correct
@alagusundaramkarthi66057 ай бұрын
1 atm is 1.01325 bar g
@nicksengineering9877 ай бұрын
@@alagusundaramkarthi6605 1 ATM = 1.01325 bar A but not bar g. 0 barg = 1.01325 bara = 1 ATM
@077rdm7 ай бұрын
Addition of ∆P in Discharge pressure required😊
@rarkei_9 ай бұрын
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?
@nicksengineering9877 ай бұрын
If you study API610, you will find out.
@abengineers9209 ай бұрын
Thank you for this video
@NedumEze9 ай бұрын
Great. Thanks Nick
@nagendrasingh8409 ай бұрын
A very good explanation. Thank you Nick.
@shabrazk518210 ай бұрын
nice biriyani 😀
@sourabhpatil407410 ай бұрын
Nicely explained.
@ARyan-og1wt10 ай бұрын
Thank you Sir for your super teaching and informations in this video... You clarified many points in my mind in the Gas dehydration Unit
@user-lj5uq7hk1z11 ай бұрын
u have whtassap numnber
@anglinh749711 ай бұрын
Please help me explain where the Fuel gas flows when it absorbs water from the stripping column @all
@asnalishamsho234311 ай бұрын
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.
@nicksengineering9877 ай бұрын
Yes, correct.
@ARyan-og1wt Жыл бұрын
Thank you for your thourough and excellent work
@theinhan3103 Жыл бұрын
Thank you
@rathinamperiyaiah966 Жыл бұрын
clear and detailed lecture. thank you.
@raphaelragu Жыл бұрын
Very nice explanation, thank you
@omowaleolaakerele3514 Жыл бұрын
I love the way you explained the whole process and broke it down to a layman's understanding. Wonderful, I must say! 👏👏👏
@MoussaMou-uj6oc Жыл бұрын
Kim Jong-un
@raouf-tek Жыл бұрын
Any video to explain gas dewpointing please
@poker5147 Жыл бұрын
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?
@josephrajakumar6246 Жыл бұрын
Thank you brother. Very nice ❤❤❤
@josephrajakumar6246 Жыл бұрын
Please share more
@nicksengineering987 Жыл бұрын
Haha thanks
@josephrajakumar6246 Жыл бұрын
Very nice explanation brother ❤
@darwinkishore Жыл бұрын
Very nicely explained in a simple manner, I use it for training junior operators. I request if you can do one for gas sweetening.
@shanmugasundaramnarbavi1911 Жыл бұрын
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
@nicksengineering987 Жыл бұрын
The Head is the same assumed that the viscosity and pump speed are the same. of course, the denser fluid will affect pump efficiency due to hydraulic friction loss, motor power efficiency, etc.
@slengoslengaw8510 Жыл бұрын
Is NPSH calc applicable for closed loop systems? I only saw open loop examples and nothing for closed system
@slengoslengaw8510 Жыл бұрын
Hi all, anyone has an excel sheet for pump sizing they can share? Thanks
@nicksengineering987 Жыл бұрын
There are many sheets on the internet. You can easily find but you need to verify its calculations.
@khadimhussain4524 Жыл бұрын
tnx good
@ahmedomerismail7730 Жыл бұрын
Thanks
@nandakumar-oc7gy Жыл бұрын
Hi Mr. Nick !!! Greeting's. How come vessel operating under atm press became 10.2 bar G pressure in your calculation?
@ASIFKHAN-ui7jp Жыл бұрын
so good thanks
@Miraclemac Жыл бұрын
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
@suntech18 Жыл бұрын
Iam now Fully understand how this system works iam new to oil and gas, your explanation like a professor. Aneongaseo