@@ChemicalEngineeringGuy I load and discharge chemical barges on the Houston Ship channel. Long ago when I believed my calling was structural engineering I first earned an associate's degree in Drafting and Design because I wanted to work with Engineers from the ground up. After working with them 10 years I found out that they were only fond of themselves. So I found a comparable salary with a simpler way of life in barge tankering. Lol I said all this to ask why does Sodium Sulfide (Spent Caustic) 9/10 contain h2s?
I am designing amine regenerator and i am using steam for stripping co2 but i am straggling with the equilibrium data do i use co2 and amine data or co2 and h2o data? Can you help me with that 🙊
Is there another way where the liquid from the regenerator doesn't go straight to the reboiler and a tee to the heat exchanger and the reboiler is upstream of the pump?
yeah, technically speaking, but remmeber that unit operations within unit operaitons can be also assigned as "unit operations" for instance, reactors that require heating or cooling, will be seen as a "single" unit as well
great work with the annotations, takes me back to university days - keep up the sterling work!
-great! I will!
there is where I'm at now
Good explanations from a great chemical engineer
Thnx mate!
Very good video my friend. Only now I realized I used the same picture of yours on my post on LinkedIn :)
Make no worries! It is a free image by Wikipedia XD
Excellent!! heve you a video with the chemical behavior of the amine and H2S? thanks for the information.
Thank you very much, your method of teaching is very effective! Thanks again!
Thanks! Im glad you found it useful XD
@@ChemicalEngineeringGuy I load and discharge chemical barges on the Houston Ship channel. Long ago when I believed my calling was structural engineering I first earned an associate's degree in Drafting and Design because I wanted to work with Engineers from the ground up. After working with them 10 years I found out that they were only fond of themselves. So I found a comparable salary with a simpler way of life in barge tankering. Lol I said all this to ask why does Sodium Sulfide (Spent Caustic) 9/10 contain h2s?
Very informative video 👍👍👍
kudos!
Thank you very much. Very simple explanation
Is H2S & CO2 gas after separation will release to surrounding or become the byproduct?
What is the limitations of gas flow and h2s percentage
Great explanation. Thanks
Does the process generate any efluents/residues?
for sure, there must be always an extra feed since the process is not 100% reversible
thanks for sharing, its very informative, Great Job
Thank!
Thank you very much ..!!
Really productive ❣️
I am designing amine regenerator and i am using steam for stripping co2 but i am straggling with the equilibrium data do i use co2 and amine data or co2 and h2o data? Can you help me with that 🙊
Well, you already stated, you are using water + CO2, but remember that CO2 binds to amine as well... meaning that you need both of them :)
Is there another way where the liquid from the regenerator doesn't go straight to the reboiler and a tee to the heat exchanger and the reboiler is upstream of the pump?
Nice presentation
Thanks
Спасибо тебе огромное !!!
can i use plate heat exchanger instead of the reboiler, any difference?
Theoretically, but normal operation is with reboiled to favor liquid vapor interaction
Hello,
For a small scale hydrogen production plant which is better psa (pressure swing adsorption) or amine washing absorption?
what is the size?
Wonderfully explained.
Try to provide animation if possible
Will do! Currently Im on a low budget :P
in this process not exit any pollutant ( like sulfur dioxide ,nitrogen oxides ) , does it applicable stack testing for this process?
Do you have simulation in Aspen of this process?
Hi, I do have some of them, but no for this one specifically
When adjust function is used in Hysys? Could you show an example in an amine case?
You will adjust for the required value, it is used when you need to fix an input only
Excelente información! Gracias por compartir tu conocimiento. Estoy interesado en tus cursos. Dónde podría comunicarme contigo? Saludos desde Dubai.
here: contact@chemicalengineeringguy.com
Sir how it's unit operation if the CO2 forms H2co3 ? Wouldn't it be unit process??
yeah, technically speaking, but remmeber that unit operations within unit operaitons can be also assigned as "unit operations" for instance, reactors that require heating or cooling, will be seen as a "single" unit as well
why do we ensure a lower temp for absorber than in stripper?
lower temperature make dissolution of gases into liquids better
Could you Please upload video of Condensate stabilisation unit and process at offshore production platform
will try, but most likely until next year! Sorry!
can you add caption to ur videos pls
try CZcams's automated! captions take too long =(
could you please do an example of mass balance on this system.
Will try to find one
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Presentation is so bad
can you be more specific?