Відео

bro i doing the same simulation in dwsim but its saying the [30-7-24 1.50.36 AM] Error in 'Absorber': Index was out of range. Must be non-negative and less than the size of the collection. Parameter name: index pLEASE HELP

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Hi, Thank you for the informative and useful videos. Could you help me with the Aspen Plus Dynamic? I've been struggling for a week trying to converge the file that works perfectly in Aspen Plus

Thank you for your useful videos. We want chapter 8 and 9 completely ASAP. Please make longer videos. Thank you!

Thank you for your useful videos. We want chapter 8 and 9 completely ASAP. Please make longer videos. Thank you!

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thank you sir for this video

Thank you for your efforts!!!!!!!!!!!!!!!!!!!!

In key component recoveries section asks for the mole fraction. However, you used mass fraction in this particular problem. Is that okay?

sir in case which the stages that we don't know, how you determine the stages of the absorber/stripper in HYSYS? since we know if the distilation we can use shortcut column but not with absorber/stripper

Hello Mohammad, Thank you so much for all your efforts. Can you please upload more videos about dynamic simulation using AspenHysys or Aspen plus? thanks

Could you explain why deltaT(min) is the 20 degC? Is it not (50-20) =30 degC?

good

Super expansion sir

Ur videos sir are very helpful, continue the good work, thank you 👏

Good Job. is possible to create the flow sheeting for cement industry?

Great video !!!!

Thanks for the aport ans share valuos material

I am from Chile , i Will share with my school of eng chemistry , do you.offer courses of handle of softwares of processes about syatems or instrumentation ,control industrial, thanks for your aport

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Good going

where is that channel?

very helpful

Sir aapka distillation design and troubleshooting ka Full course available ho to ..I am interested..Aapke video very helpful hai....respect🙏🏻

Thank you for your content. I have a question on how to resolve the imbalances in mass and energy balances?

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Sorry sir if my English is not very good. Can I know where the reference for this process comes from? is it a patent? may I ask for the source

Hi, I already followed your steps. But I can't get results for hydraulic plots. How can I improve this Sir,?

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PROCESS MODELING AND SIMULATION LAB LIST OF EXPERIMENTS: 1. Estimation of dew point and bubble point temperature of a hydrocarbon mixture 2. Simulation of flash drum 3. Design of ditillation column 4. Optimization of a flow sheet or process 5. Determination of temperature profiles for heat exchanger 6. Concentration profiles for reactor 7. Simulation of Jacketed CSTR 8. Simulation of process 9. Simulation of evaporator/ distillation column/ extraction process

CHEMICAL REACTION ENGINEERING LAB LIST OF EXPERIMENTS 1. Determination of activation energy of the given reaction using adiabatic reactor 2. Analysis of kinetics of liquid phase reaction in acbatch reactor with equimolar mixture. 3. Analysis of kinetics of liquid phase reaction in a batch reactor with non-euimolar mixture. 4. Evaluation of the performance of isothermal mixed flow reactor. 5. Evaluation of the performance of mixed flow reactor in series 6. Evaluation of the performance of plug flow reactor 7. Evaluation of the performance of mixed flow reactor followed by plug flow reactor 8. Resdence time distribution studies in mixed flow reactor 9. Resdence time distribution studies in plug flow reactor

sir could you please upload some chemical Engineering Lab experiments PROCESS DYNAMICS AND CONTROL LAB LIST OF EXPERIMENTS 1. I & II Order System Dynamics 2. Interacting & non interacting Systems 3. Flapper - Nozzle system 4. Control valve characteristics 5. Level control system 6. Flow control system 7. Pressure control system 8. Control of a thermal system 9. Design of control system for a given process 10. Simulation of a closed loop system 11. Demo Experiment using Aspen Software of a given process

But liquid 2 is defined as the heavy liquide and liquide 1 as the light liquid. I suppose Liquid 2 will have the heigher molar fraction in cyclohexane the most heavy molecule

kindly provide us HTRI crack download for learning purpose also provide guidance for installtion plz !!

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very nice, thanks

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Sir please make video of design condenser in EDR and if I need to design double pipe HE which is not in EDR so can I design it by using S & T HE

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THANK YOU SO MUCH LOVE YOU XOXO

hey i have a question please response!, the compresor says it 4000 kw, but in reality it is 40 kw? because 4000 kw is absurd

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Great going sir

Good

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hi sir, how can practice of like that problem I want pdf of problem

Good one. I am a beginner. I understood and implemented your examples quite easily. Well, my purpose of learning these simulations is to finally simulate a system consisting of solar energy and Rankaine cycle. I am postdoc candidate. If you want to collaborate with me, you are welcome. Your expertise in Hysys will be asset for me.

Great Explanation