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Reactor Design In G-L-L-S System.


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#1 R.Shevlin

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Posted 17 November 2017 - 02:59 PM

Dear all,

For a design project I need to design a CSTR to convert nitrobenzene to para-aminophenol by catalytic hydrogenation using Pt/C. 

The nitrobenzene exists as a dispersed organic phase inside a continuous phase of sulfuric acid. I have obtained the rate of reaction and was going to use the design equation for a CSTR but my supervisor told me that because the reaction only takes place inside the dispersed phase that I need to model each nitrobenzene drop like a small PFR and use a different design equation for calculating the reactor volume. 

I don't really understand why and was hoping someone could explain this to me.



#2 deepankar.uict

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Posted 27 March 2018 - 12:59 AM

Wow! Small world. I wrote a small paper on this very topic. Here is the link to it, take a look and please let me know if you find the info useful. 

 

https://pubs.acs.org...cs.iecr.6b03744


Edited by deepankar.uict, 27 March 2018 - 01:00 AM.


#3 Nikolai T

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Posted 29 March 2018 - 01:59 AM

Hello,

 

Could you please upload full arcticle?

 

Regards,

Nikolay



#4 deepankar.uict

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Posted 30 March 2018 - 12:22 AM

Full article. 

Attached Files



#5 Nikolai T

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Posted 30 March 2018 - 01:45 AM

Thank you very much!

 

Regards,

Nikolai






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