![Mohamad Rezi Abdul Hamid](/img/default-banner.jpg)
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Mohamad Rezi Abdul Hamid
Malaysia
เข้าร่วมเมื่อ 22 ก.ย. 2015
Hello, my name is Rezi. This channel is dedicated to learning process simulation software (e.g., Aspen Plus) and general chemical engineering discussion.
If you like my videos, please consider subscribing to this channel.
A new video will be uploaded every week or two-weeks (depends)
Check out my research website: mohamadreziabdulha.wixsite.com/mysite
If you like my videos, please consider subscribing to this channel.
A new video will be uploaded every week or two-weeks (depends)
Check out my research website: mohamadreziabdulha.wixsite.com/mysite
Engineering Drawing Compilation (Group Project ENG3201)
A compilation of drawing (detail and assembly drawing) prepared by students from my AutoCAD class
มุมมอง: 45
วีดีโอ
Water Network Synthesis (Tyre-to-Fuel Process) - Part 2
มุมมอง 692 หลายเดือนก่อน
A short video on how to create water network using water pinch analysis. Case study tyre-to-fuel process as an example
AutoCAD 3D Modelling (Sweep, Helix, Viewbase, etc.)
มุมมอง 1763 หลายเดือนก่อน
Short demo on applied 3D object in AutoCAD
Water Network Synthesis (Tyre-to-Fuel Process) - Part 1
มุมมอง 563 หลายเดือนก่อน
A short video on how to create water network using water pinch analysis. Case study tyre-to-fuel process as an example
AutoCAD 3D Modelling - Primitive & Applied 3D Object
มุมมอง 1513 หลายเดือนก่อน
A short demo on 3D modelling using AutoCAD
Engineering Drawing (Pictorial Projection)
มุมมอง 1754 หลายเดือนก่อน
A short lecture on various pictorial projection
AutoCAD 2D Modelling - Multiview Projection (3rd Angle Projection)
มุมมอง 3774 หลายเดือนก่อน
Short demo on how to prepare multiview drawing as part of class practical session
Consequence Analysis of Toxic Gas Dispersion (ALOHA & MARPLOT)
มุมมอง 3444 หลายเดือนก่อน
A quick demo on how to do a quick consequence analysis on chlorine gas dispersion when there is a loss of containment. It is a free software to download. I don't have access to a more fancy software. Demo start at 18.43
Short ChemE Video - Linearized Arrhenius Equation (Might Be Useful to 1st Year Student)
มุมมอง 366 หลายเดือนก่อน
Short ChemE Video - Linearized Arrhenius Equation (Might Be Useful to 1st Year Student)
Aspen Plus - Define Petroleum Fraction (Pseudocomponent, Assay, Blend) - Pt 1 of 3
มุมมอง 2347 หลายเดือนก่อน
A short demo video on how to define, specify, and analyze petroleum fraction.
Aspen Energy Analyzer (Part 3) - Forbidden Matches, Network Optimization, etc.
มุมมอง 5457 หลายเดือนก่อน
Part 3 (final part) of the Aspen Energy Analyzer video - focuses on exploring the remaining features of the software such as forbidden matches, network optimization, design suggestion, and many more.
Pinch Analysis - Problem Table Method (1st Video of 2024)
มุมมอง 2277 หลายเดือนก่อน
Short video on how to determine minimum cold and hot utility using Problem Table method
Aspen Plus - Lignocellulosic Biomass Gasification Part 2
มุมมอง 1.6K8 หลายเดือนก่อน
Many people have been requesting me to do simulation of biomass gasification/pyrolysis so here it is. Very long video so I decided to divide the video into 2 parts. One of the reason is because I like to talk/explain and if I don't provide reasoning/assumption for my selection, it would not do justice on people who would like to know my train of thoughts.
Aspen Plus - Lignocellulosic Biomass Gasification Part 1
มุมมอง 1.7K8 หลายเดือนก่อน
Many people have been requesting me to do simulation of biomass gasification/pyrolysis so here it is. Very long video so I decided to divide the video into 2 parts. One of the reason is because I like to talk/explain and if I don't provide reasoning/assumption for my selection, it would not do justice on people who would like to know my train of thoughts.
Aspen Energy Analyzer (Part 2) - Create Heat Exchanger Network
มุมมอง 1.2K8 หลายเดือนก่อน
Part 2 of 3 part video on Aspen Energy Analyzer V12.1
Pinch Analysis - Prepare Hot & Cold Composite Curve Manually
มุมมอง 1.8K8 หลายเดือนก่อน
Pinch Analysis - Prepare Hot & Cold Composite Curve Manually
Aspen Energy Analyzer (Part 1) - Creating Composite Curve
มุมมอง 1.4K9 หลายเดือนก่อน
Aspen Energy Analyzer (Part 1) - Creating Composite Curve
ChemE Go Green Demo Video - From Fish Waste to Pet Food
มุมมอง 939 หลายเดือนก่อน
ChemE Go Green Demo Video - From Fish Waste to Pet Food
Metal Organic Framework Membrane for Gas Separation - Presentation Recording
มุมมอง 25511 หลายเดือนก่อน
Metal Organic Framework Membrane for Gas Separation - Presentation Recording
Engineering Drawing - Interpret P&ID of Pressure Vessel
มุมมอง 62211 หลายเดือนก่อน
Engineering Drawing - Interpret P&ID of Pressure Vessel
Lab Session 7 (ENG3201 & ECH3907) - Yesterday Was Public Holiday!!!!
มุมมอง 221ปีที่แล้ว
Lab Session 7 (ENG3201 & ECH3907) - Yesterday Was Public Holiday!!!!
Not About Aspen or AutoCAD. Just a ViDeO oF mY CaT
มุมมอง 165ปีที่แล้ว
Not About Aspen or AutoCAD. Just a ViDeO oF mY CaT
Lab Session 6 (ENG3201 & ECH3907) - Good Luck and Have Fun!!!!
มุมมอง 351ปีที่แล้ว
Lab Session 6 (ENG3201 & ECH3907) - Good Luck and Have Fun!!!!
Aspen Plus - Add Stream Sell/Purchase Price & Setup New Currency
มุมมอง 768ปีที่แล้ว
Aspen Plus - Add Stream Sell/Purchase Price & Setup New Currency
Aspen Plus - Model Palette or Flowsheet Disappeared + Add Stream Flag
มุมมอง 9K2 ปีที่แล้ว
Aspen Plus - Model Palette or Flowsheet Disappeared Add Stream Flag
Aspen Plus - Extractive Distillation of Acetone-Tetrahydrofuran Mixture
มุมมอง 9472 ปีที่แล้ว
Aspen Plus - Extractive Distillation of Acetone-Tetrahydrofuran Mixture
Manuscript Writing - Prepare Nice Figure (XRD Pattern) Using MagicPlot
มุมมอง 4032 ปีที่แล้ว
Manuscript Writing - Prepare Nice Figure (XRD Pattern) Using MagicPlot
Aspen Plus - Liquefaction of N-Butane (Heat Exchanger)
มุมมอง 3712 ปีที่แล้ว
Aspen Plus - Liquefaction of N-Butane (Heat Exchanger)
Aspen Plus - Coal (Nonconventional Component) Drying RSTOIC Block
มุมมอง 2.6K2 ปีที่แล้ว
Aspen Plus - Coal (Nonconventional Component) Drying RSTOIC Block
clutch
Can i use pressure swing to separate ethanol & ethyl acetate? The desired product is at least 99.7% purity of ethyl acetate.
is this software free??
yes, the software is free to download
awesome
wow thanks ...it has helped me alot
Can you do a wet fgd process, showing how to remove the gypsum by product.
NYC video some drawings are very hard can u tell me how to start that drawing and end easily
my thanks
thank you✧*。٩(ˊωˋ*)و✧*。 you're just the savior (´இωஇ`)
When feeding kinetic data, it requires concentration exponents. The following error is popping up: "REAC-DATA not complete: REACNO = 1. At least one exponent for the reactant must be specified."
Hi i need a big help regarding aspen hysys pls distillation column not converging 🥲
Your videos are more informative iI am really thankful to you, I was really so worried about Aspen plus and there is no proper guidance it took 2 months to find your video and channel, this kind of informative and true TH-camrs should be promoted and suggested at the top or searching bar, I am really very thankful to you my you more success in your career and you life and split more easiness for other beginners like your this work.
thank you for this video its really helpful i was struggling to find anything on the internet about this and explaining in detail like u did so thank you very much
14:34
15:48
Thank you so much. Just a little suggestion, Sir. As I know the magnitude of DT Min is not so arbitrary, to decide whether it shall be 5 degC or 10 deg C. There is a minimum value of it. If you set the DT min too low, you will end up with having only cold end network as your video (network that only require cold utilities, it is undesirable in design point of view). Anyway, I am also new in this field. Your video help me a lot to understand about aspen energy analyzer interface. Thank you !!
Configuration B Reboiler has also reboiler duty = 42 MW
To simulate decomposition
29:30
thank you so much ]
mantap.....
can you make all table calculation table in exel
nice video, excuse me where can we get This book in PDF learn asp en plus in24 hours
Waouuuu Nice video
thank you for sharing. could you tell me how to show or check the enthalpy of each stream above/below pinch point
Hi thank you for your sharing, I have some questions,1/ how to make aspen energy analyzer show the enthalpy value of each stream above/below the pinch?2/ how to identify the cost parameter?
Can we just assume the delta Tmin? Or there is calculation for the 25 celcius heat load placement before obtain delta Tmin
You can use any delta Tmin as long as it is greater than zero..in fact, different processing will have different recommended delta Tmin. For example, low temperature/cryogenics will use small deltaT min. In my case i just simply use 10oC
My POV, the recommended value for delta t min is shown in graphs (Cost or Area vs Delta T min) in textbook (PINCH ANALYSIS FOR ENERGY AND CARBON FOOTPRINT REDUCTION) is around 10 to 20. This typically will give maximum efficiency with little to no drawbacks. Hope that helps.
Hey,Sir. How can you help me, I want to model a coal dryer simple plant ?
Can i know what is the pressure at absorber?
Thanks for sharing, as for the first part, can't wait for the third part.
hey, can you help me out. i want to design a coal dryer , our coal contains a lot of moisture , how can you help me?
@17:51 = 4*(150 - 135) = 60 kW (not 20 kW)
Awesome...thank you very much I trying this simulation from 2 month.....again thanks ...keep it ...can you start series for petroleum refining all process on Aspen plus....cdu,fccu, hydrogen manufacturing,hydrotreater....can you recommend any course that help me for this simulation
Great Video. Thank you so much. Do you happen to have an unblocked version of the table that I can access please
@10:00 because the stoichiometric coefficients must be in molar basis.
Thank you so much, waiting for the second part.
thanks :)
Very nice explanation. In addition I like to request to manage subtitles in such way that it can be stopped. Many times it becomes impossible to read original text in back ground specially equations.
Please link to the textbook
Could you please explain how to determine the pressure of HP column?
very useful conceptual tutorial
You just saved my life lol great intro
2011, 2035, 2012 are line numbers btw. DESIGN: 11,032 kPag/FV@343C/-29C probably design pressure under full vacuum at temperature
GREAT EXPLANATION BY YOU MAN
hi i have nonconventional solid how to define the Stoichiometric coefficients for drying
I am using HCOALGEN and DCHARTIGT to define my biomass. I added the HCOMB coming from calorimeter experiment (19 MJ/KG). However, the value I got in ASPEN is (-3.5). I wanted to study the effect of energy content change on the process... However, whatever number I write, it does not affect on the process yield or Syngas in gasification. Is that logical? I will truly appreciate your help.
poggers video