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#1
Posted 31 December 2017 - 01:36 AM
#2
Posted 01 January 2018 - 11:14 AM
I don't have that paper so I don't know what exactly is in there.
% conversion of each feed component is the result of kinetics and catalyst volume.
In any case conversion can not be more than total equilibrium would allow, but that would require an infinite catalyst volume.
I don't have kinetic data for catalytic reforming reactors.
#3
Posted 09 January 2018 - 11:42 PM
I am Bindu studying BTech Final year Chemical engineering. I am doing project on acetic acid production from methanol and carbon monoxide so I selected cativa process.To do simulation through hysis or unisim. I need a Kinetic data regarding the Cativa process for the production of acetic acid from methanol by using iridium complex catalyst and the flowsheet contains cstr reactor and 2distillation columns. Please send me kinetic data to my email id: bindhumoulika303@gmail.com
Thanks and regards
#4
Posted 07 January 2024 - 03:12 PM
I am Lawrence Mtech student doing a group design project on design of plant for production of acetic acid from natural gas, we chose methanol carbonylation process any relevant work to help with our hysis simulation will be appreciated
#5
Posted 07 January 2024 - 03:13 PM
#6
Posted 07 January 2024 - 10:51 PM
Hi,
Not a good idea to disclose your email address, spammers at the corner.
Delete it.
Breizh
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