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Langmuir Hinshelwood Hougen Watson (LHHW) of Steam Methane Reforming || Aspen Plus 

Chemiopedia
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This video is about the simulation of the Langmuir Hinshelwood Hougen Watson (LHHW) of Steam Methane Reforming in Aspen Plus.
@ 00:17 Introduction to SMR reaction and it’s kinetics
@ 00:40 Rearranging Keq according to requirement
@ 01:11 Calculating A and B for forward reaction
@ 02:03 Calculating A and B for reverse reaction
@ 02:17 Calculating A and B for adsorption term
@ 02:50 LHHW kinetics assistant by Chemiopedia
@ 03:45 Same example using LHHW kinetics assistant
To download the LHHW kinetics assistant: chemiopedia.co...
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Опубликовано:

 

15 сен 2024

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Комментарии : 36   
@tts9931
@tts9931 2 года назад
wonderful, thank you so much
@Chemiopedia
@Chemiopedia 2 года назад
Glad you liked it!
@pepijnNLgod
@pepijnNLgod 2 месяца назад
Thank you, this is exactly what I was looking for. Is there any chance you can help me out with the following: I am trying to get the exponents of each reaction for the driving force, When I use the format in Aspen with the A/B parameters and adsorption constants and exponents, if i enter 0, 1, or stoichiometry at the driving force exponents I get errors everytime that indicate my kinetics are faulty.
@Chemiopedia
@Chemiopedia 16 дней назад
Kindly share screenshots at chemiopedia@gmail.com
@dumbsiteful
@dumbsiteful 2 года назад
very helpful. Thank you. Where do you add the values A and B in aspen?
@Chemiopedia
@Chemiopedia 2 года назад
These values of SMR is not added in Aspen in any video.
@akashkrishnadoss757
@akashkrishnadoss757 Год назад
how to enter kinetic data if the model is mentioned in both partial pressure and concentration in the paper
@Chemiopedia
@Chemiopedia Год назад
can you share further information at support@chemiopedia.com
@redagalih
@redagalih 11 месяцев назад
Very helpful. Please recheck that the k1 in that unit should be 1.17e+12 not 1.17e+15
@Chemiopedia
@Chemiopedia 11 месяцев назад
Both values are correct based on unit of reaction rate. If you are considering rate in kmol/(kgcat s) then 1.17e+12 is correct value. To have unit mol instead of kmol, 1.17e+15 will be used.
@ganser96
@ganser96 3 года назад
Very helpful tool thank you. I have a problem with co2 methanation kinetics in Aspen any chance can you make a tutorial about Haldor-Topsoe TREMP ?
@Chemiopedia
@Chemiopedia 3 года назад
Can you share some details here: info@chemiopedia.com
@Lqtan16
@Lqtan16 Год назад
Hey Erkan, I am doing similar stuff too. Do you want to chat and discuss?
@KaranSharma-gn1nn
@KaranSharma-gn1nn 2 года назад
i tried to put these values in Aspen plus and followed the same steps you recommended in the previous (methanol) video but I am not getting any reaction the reactants are not reacting at all any idea why?
@KaranSharma-gn1nn
@KaranSharma-gn1nn 2 года назад
please help!!!
@lilhost5487
@lilhost5487 2 года назад
Информативно, очень помогло. Но можно сделать видео по моделированию LHHW в AspenPlus c паровой конверсией метана)
@Chemiopedia
@Chemiopedia 2 года назад
Comment in English please.
@Chemiopedia
@Chemiopedia 2 года назад
Comment in English please.
@patriceamrolalaei6487
@patriceamrolalaei6487 2 года назад
hi thanks, pls make video for another kinetic of reforming reaction ch4 + 2h2o ==> 4h2 + co2 im waiting for it .
@Chemiopedia
@Chemiopedia 2 года назад
The SMR video, will be available soon including the above reaction. Don't forget to subscribe.
@umairhassankaust1939
@umairhassankaust1939 2 года назад
Hi. I simulated the same process using the given parameters but the conversion is really really low (0.001%). I changed flow rate, temp, and pressure but observed no effect. Any idea why I am getting low conversion?
@manishmaurya6296
@manishmaurya6296 Год назад
Umair, did you find the reason for getting low conversion in SMR? Can you share it here?
@umairhassankaust1939
@umairhassankaust1939 Год назад
@@manishmaurya6296 couldn't figure it out
@redagalih
@redagalih 11 месяцев назад
The k1 should be 1.17e+12 not e+15 and it would affect k1/K1 too
@rasheede.o4824
@rasheede.o4824 6 месяцев назад
Could you show the values for adsorption constant and driving force
@pepijnNLgod
@pepijnNLgod 2 месяца назад
@@rasheede.o4824 Yeah, I need the driving force ones too!
@sydneytebele5252
@sydneytebele5252 3 года назад
Can you give a link or reference to the paper where you got these Kinetics?
@Chemiopedia
@Chemiopedia 3 года назад
www.sciencedirect.com/science/article/abs/pii/S0016236121006463
@sydneytebele5252
@sydneytebele5252 3 года назад
Thanks, thumbs up for video 👍
@Chemiopedia
@Chemiopedia 3 года назад
Thank you. Don't forget to subscribe
@patriceamrolalaei6487
@patriceamrolalaei6487 2 года назад
pls simulate a steam reforming methane process in aspen plus
@Chemiopedia
@Chemiopedia 2 года назад
The SMR video, will be available soon. Don't forget to subscribe.
@patriceamrolalaei6487
@patriceamrolalaei6487 2 года назад
@@Chemiopedia hi I've been waiting since u told me, and i have another question. Is the kinetic of co in LTS & HTS different than the kinetic co in reformer?
@patriceamrolalaei6487
@patriceamrolalaei6487 2 года назад
I check your article but u just discussed about the kinetics in reformer
@Chemiopedia
@Chemiopedia 2 года назад
Sorry for delay. SMR process is basically a part of the next upcoming series of video. Due to some unforeseen circumstances, the series get delayed. You are requested to write us at support@chemiopedia.com. I will share the customized link of the SMR video with you. Remember, you will not allowed the share the content to anyone else.
@Chemiopedia
@Chemiopedia 2 года назад
Kinetics of LTS and HTS will be different than the kinetics in the reformer as shift convertors utilizes different catalysts.
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