Good morning, I would like to ask the following regarding the exercise described in this video. I am using hysys v14, when I run the simulation it does not converge when including the side stripper for the diesel. I have observed a difference in the performance of the products, especially with respect to gasoline and diesel. What could be the reason for the difference in performance theoretically calculated by hysys between its results and mine.
Hello. How to reduce the amount of vapor at the top of the rectification column? The type of trays, their efficiency? I have a lot of top reflux in model the unisim program. I am asking for an answer and best regards.
Very Nice Video.Would like to highlight small observation ,For Kerosene Pump Around Loop ,Draw off stage(Stage -8) & Return stage(Stage-9) is not in line with presentation data.You may cross check and update accordingly for consistency purpose.If the corrections are updated ,the Kero PA draw off temperature would increase to final value of 184.6 Degree C.
Thank you very much for this observation. It was probably an oversight on my part. Others should kindly take note of this. Thank you very much Mr Sandeep
Bonjour j'ai besoin de faire le schéma suivant : crude oil -heater -separature -Atm distillation unit-vacucm distillation unit - Cracker . can you help me ,
Good morning, I would like to ask the following regarding the exercise described in this video. I am using hysys v14, when I run the simulation it does not converge when including the side stripper for the diesel. I have observed a difference in the performance of the products, especially with respect to gasoline and diesel. What could be the reason for the difference in performance theoretically calculated by hysys between its results and mine.
Thank you, this has been very useful. Could you also maybe provide the resources you've utilised in the description box?
Hello. How to reduce the amount of vapor at the top of the rectification column? The type of trays, their efficiency? I have a lot of top reflux in model the unisim program. I am asking for an answer and best regards.
Please do you have a video about vacuum distillation ?
Thanks a lot sir, it's really helpfull!!!
Very Nice Video.Would like to highlight small observation ,For Kerosene Pump Around Loop ,Draw off stage(Stage -8) & Return stage(Stage-9) is not in line with presentation data.You may cross check and update accordingly for consistency purpose.If the corrections are updated ,the Kero PA draw off temperature would increase to final value of 184.6 Degree C.
Thank you very much for this observation.
It was probably an oversight on my part.
Others should kindly take note of this.
Thank you very much Mr Sandeep
@@geniuscreed369 please may i get your E-mail address . thank you
Nice one knowledge is power
Thk you , I tried it but when I added the kerosene Pump around it didn’t converge
It was SOLVING ….
Bonjour
j'ai besoin de faire le schéma suivant : crude oil -heater -separature -Atm distillation unit-vacucm distillation unit - Cracker . can you help me ,
Very informative
Thanks a lot sir!
Sir, I saw you showing your Final year design project on LinkedIn. Could you please make a detailed tutorial on that as well?
I'll see what I can do.
But it might not be soon.
Thanks.
Genius Creed thanks sir
How can I contact you?
you can send us an email
your soft is very soft and hard to hear.