Відео

thank you for the informative video. Can you share the pdf? the access is denied.

Can you send me the link of this paper

Sir , the video was really useful...but why balance is made in the end stage with heat pump and cryogenic duty..can you please tell

Amazing tutorial! Thank you!

Hi sir, i need some clarification: 1. At 7:01, shouldnt it be "M to Heater" instead of "M- to Cooler".. The component that u use to is to heat up methane. 2. 2ndly, at @1:55, u mentioned that the cascade cycle uses propane to cool down the NG at first stage. However, in this simulation, u use methane instead. 3. What is the fucntion of "Bal-1", "Bal-2" and "Bal-3"? Thank you

Thank you so much this is so helpful ❤❤❤

thanks for the video, how do you calculate absorber and stripper stages. thanks

سلام عليكم ممكن تواصل إذا امكن

hello, from where did you get the plant data? I have heard that the amine temperature is usually higher than the sour gas temperature when it enters the contactor but not in this case

The video is very useful but the sound is not clear and you are talking quick. If you can record the new one for TEG unit and you start to do the simulation should talk each step.

Hi Assi I have little bit confusion that due to the increase in aromatics RON is also increasing with you sad that both are inversely proportional please clarify

بحبك <3

Thanks for your help

Could you please send me the presentation on PFD format?

Amazing Simulation. Thanks Dr. Mohammad Assir.

How can I remove H2 from C1. C2. C3

Hi assi, im beginner with this app, if you don't mind, can you give me tutorial to fill component and reaction in this method(CCR) please?

How can we separate H2 from Co2?

Can I have a copy of your FCC component list? Thanks

Hello Engineer, Could you provide me with the word document and the Aspen Hysys file? I am trying to simulate a gas plant for my university project and I need information. If so, if you can help me, I would greatly appreciate it. By the way, very good explanation and contribution with your video. Thank you very much

hello sir, i appreciate your knowledge about this software, but i wonder why doesnt the main fractionator have the Gasoline cut?

hello sir, i appreciate your knowledge about this software, but i wonder why doesnt the main fractionator have the Gasoline cut?

Hi Can I have plant of NRU Process that you simulate by refinery hysys ? Or pdf that describe this process?

Sir, do you have biogas simulink model using anaerobic digestion?

The solution to the column with the current specifications does not converge. The process that i am simulating is identical but the regenrator just keeps solving

please you word give me

Dear Eng., can I have those word files please?

I could learn a lot from you. Thank you

thank very much

ممكن اتواصل معاك؟

Please am currently working on production of hydrogen gas plant using bitumen as a raw material....I will like to share ideas with you. Thanks and best regards

Assalamu Alaikum. Mr. Mohammed, Can you please help me with the link of the first video? seems like this is not the beginning and i could'nt find the first video on youtube. I'm a final year student of Chemical engineering (undergraduate) and working on simulation of crude oil hydrodesulphurization process as my project.

The valve with high pressure drop & separator , could these component only simulate the effect of the JT valve alone ?

Do I need to simulate all the 3 processes combined in order to simulate the effect of the JT process ? Or this vedio discusses a real plant has all the three processes ?

Thank alot. Coulf you please send me hysys file? thanks

Please how can we add the feed if we don't have the composition ( instead we have the feed properties )

Please how can we add the feed if we don't have the composition ( instead we have the feed properties )

Please how can we add the feed if we don't have the composition ( instead we have the feed properties )

Hello, Is it possible if you send me the reference? Thank you so much, Br

I am not sure if you are gonna read this after released this video 4 years ago. But I wanted to ask can we just use one distillation for methane process? or do we need to have 3 different distillation for each methane, ethane and propane? And what if we only have one same composition after the pretreatment process

Sir, Would you please upload the document that you have shown in video in the comment section?

Can you share the document you're showing to explaing everything? Or give the refenrence to that document?

Can u please tell me what changes should i make for mass flow of 1000barrel/day in this simulation? I really need your help and this video made my day thanks for making it

Thank you so much

Thank u so much

Hello, maybe you can do it on aspen plus??

This can be done on Aspen plus in the same way?

Hi how are you? Could you send me this simulation file, please, is for my tesis. Thanks my email: ignacio.germain@usach.cl

Thank You!