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KG Engineering Solutions
Germany
เข้าร่วมเมื่อ 25 ก.ค. 2021
Welcome,
You are developing a process and need simulations? Let me know your individual requirements in an email. I will answer you within the next few days.
kg.engineering.solutions@gmail.com
All Aspen simulations can be downloaded for a donation. After completing the donation, you will be redirected to the download page:
www.paypal.com/donate/?hosted_button_id=YNKPF59PG3SKW
All Ansys simulations from this channel and channel Process Engineering with CFD can be downloaded for a donation. After completing the donation, you will be redirected to the download page:
www.paypal.com/donate/?hosted_button_id=LA65BVQD8F34N
You are developing a process and need simulations? Let me know your individual requirements in an email. I will answer you within the next few days.
kg.engineering.solutions@gmail.com
All Aspen simulations can be downloaded for a donation. After completing the donation, you will be redirected to the download page:
www.paypal.com/donate/?hosted_button_id=YNKPF59PG3SKW
All Ansys simulations from this channel and channel Process Engineering with CFD can be downloaded for a donation. After completing the donation, you will be redirected to the download page:
www.paypal.com/donate/?hosted_button_id=LA65BVQD8F34N
Aspen Plus: ethyl acetate production process via esterification of acetic acid and ethanol
Ethyl acetate is widely used for the production of lacquers and surface coating resins with a world annual production capacity higher than 3 million tons.
Ethyl acetate is mainly produced via the esterification of acetic acid and ethanol.
In this video, the conventional process of esterification will be simulated using Aspen Plus.
Source: Branislav Šulgan, et al. Multi-Aspect Comparison of Ethyl Acetate Production Pathways: Reactive Distillation Process Integration and Intensification via Mechanical and Chemical Approach. Processes, 8, 12. 2020. doi.org/10.3390/pr8121618
For a small donation you can download the Aspen Plus file from the following link:
www.paypal.com/donate/?hosted_button_id=2R2ZMTL62A7RL
All Aspen simulations in this channel can be downloaded for a donation. After completing the donation, you will be redirected to the download page:
www.paypal.com/donate/?hosted_button_id=YNKPF59PG3SKW
kg.engineering.solutions@gmail.com
Ethyl acetate is mainly produced via the esterification of acetic acid and ethanol.
In this video, the conventional process of esterification will be simulated using Aspen Plus.
Source: Branislav Šulgan, et al. Multi-Aspect Comparison of Ethyl Acetate Production Pathways: Reactive Distillation Process Integration and Intensification via Mechanical and Chemical Approach. Processes, 8, 12. 2020. doi.org/10.3390/pr8121618
For a small donation you can download the Aspen Plus file from the following link:
www.paypal.com/donate/?hosted_button_id=2R2ZMTL62A7RL
All Aspen simulations in this channel can be downloaded for a donation. After completing the donation, you will be redirected to the download page:
www.paypal.com/donate/?hosted_button_id=YNKPF59PG3SKW
kg.engineering.solutions@gmail.com
มุมมอง: 148
วีดีโอ
Aspen Plus: Simulation of pyrolysis of waste tires with a kinetic model
มุมมอง 374หลายเดือนก่อน
Approximately 1.5 billion tires are produced each year which will eventually enter the waste stream representing a major potential waste and environmental problem. However, there is growing interest in pyrolysis as a technology to treat tires to produce valuable oil, char and gas products. In this video, a kinetic model for pyrolysis of tires will be simulated in Aspen Plus. For a small donatio...
Aspen Plus simulation of an amine scrubbing system for biogas upgrading
มุมมอง 4152 หลายเดือนก่อน
Amine scrubbing is one traditional method of biogas upgrading. Amine scrubbing is characterized by low methane slippage and its capability to provide a high purity renewable methane product. In this video, an amine scrubbing system for biogas upgrading will be simulated using Aspen Plus. For a small donation you can download the Aspen Plus file and the PowerPoint file from the following link: w...
Aspen Plus: Conversion of CO2 and recycle gas from a FT process into synthesis gas via RWGS
มุมมอง 4453 หลายเดือนก่อน
Reverse water gas shift (RWGS) reaction is a possible way to generate synthesis gas for Fischer-Tropsch synthesis. In this video, we will simulate the conversion of CO2 and recycle gas from a Fischer-Tropsch process into synthesis gas via RWGS. The RWGS will be simulated at 800 °C and ambient pressure. For a small donation you can download the Aspen Plus file and the PowerPoint file from the fo...
Aspen Hysys: Three Phase Separator; Recycle-Gas, FT-Oil and Water Separation
มุมมอง 1904 หลายเดือนก่อน
This video introduces into the three-phase separation in Aspen Hysys. The product in the video th-cam.com/video/fUTrkLVRQ1s/w-d-xo.html is separated into water, oil and gas. For a small donation you can download the Hysys File from the following link: www.paypal.com/donate/?hosted_button_id=MDD8YRWGWXJRW kg.engineering.solutions@gmail.com
Aspen Hysys Two Phase Separation Wax Separation from Fischer Tropsch Product
มุมมอง 2394 หลายเดือนก่อน
This video introduces into the two-phase separation in Aspen Hysys. The Fischer-Tropsch product in the video in the info cards is separated into wax and gas phase by Aspen Hysys. For a small donation you can download the Aspen Plus file, Hysys File, and the files of the video th-cam.com/video/kHEMp1mSsi0/w-d-xo.html from the following link: www.paypal.com/donate/?hosted_button_id=NHQLL86WTRRAY ...
Aspen Plus: Simulation of Fischer Tropsch Synthesis using the ASF Relationship, Rstoic, and Fortran
มุมมอง 1.1K6 หลายเดือนก่อน
The Fischer Tropsch synthesis is both a CO hydrogenation reaction and a polymerization reaction. In the first reaction, C-O bonds are broken, and new C-H bonds are formed. In the second reaction, C-C bonds are formed, and the hydrocarbon chain grows. The product distribution approximately follows a statistical function called the Anderson-Schulz-Flory (ASF) relationship. The ASF model states: t...
Aspen Plus: Economic Analysis of the Production of Acetic Anhydrid
มุมมอง 1.9K7 หลายเดือนก่อน
This video shows an economic analysis of the production of acetic anhydrid with Aspen Plus. Source: Kamal I.M. Al-Malah. Aspen Plus: Chemical Engineering Applications. John Wiley & Sons. 2017. All Aspen simulations in this channel can be downloaded for a donation. After completing the donation, you will be redirected to the download page: www.paypal.com/donate/?hosted_button_id=YNKPF59PG3SKW kg...
Aspen Plus: Autothermal Reforming of Natural Gas
มุมมอง 1.1K8 หลายเดือนก่อน
The autothermal reforming process consumes both steam and oxygen to convert natural gas into syngas. In fact, ATR is a combination of an exothermic partial oxidation (POX) process and an endothermic steam methane reforming (SMR) process neutralizing the heat supply/demand thermodynamically. In this video, we simulate an ATR. Reference: A.O. Oni, K. Anaya, T. Giwa, G. Di Lullo, A. Kumar. Compara...
Characterization of Molecules Using Aspen Properties
มุมมอง 2358 หลายเดือนก่อน
In this video we will estimate the properties of Benzamide with Aspen Plus as if it were not present in the Aspen Plus databanks. The we will compare the estimated properties with the properties of the molecule is in the Aspen Plus databanks. We use the following data for the estimation: Melting point of Benzamide: 130 °C Normal boiling point of Benzamide: 288 °C Density of Benzamide: 1.341 g/c...
Aspen Plus Biomass Crushing
มุมมอง 3979 หลายเดือนก่อน
This video simulates a biomass crusher. All Aspen simulations in this channel can be downloaded for a donation. After completing the donation, you will be redirected to the download page: www.paypal.com/donate/?hosted_button_id=YNKPF59PG3SKW kg.engineering.solutions@gmail.com
Approximate and ultimate analyzes of more than 1000 biomass samples
มุมมอง 1939 หลายเดือนก่อน
The excel file contains approximate and ultimate analyzes of more than 1000 biomass samples. For a small donation you can download the excel file from the following link: www.paypal.com/donate/?hosted_button_id=RETALH3SWADAY kg.engineering.solutions@gmail.com
Aspen Plus: synthesis of high density polyethylene by polymerization of ethylene
มุมมอง 6349 หลายเดือนก่อน
In this video, synthesis of high density polyethylene by polymerization of ethylene is simulated by Aspen Plus. All Aspen simulations in this channel can be downloaded for a donation. After completing the donation, you will be redirected to the download page: www.paypal.com/donate/?hosted_button_id=YNKPF59PG3SKW kg.engineering.solutions@gmail.com
Aspen Plus: water De Souring system by an electrolyte system
มุมมอง 24410 หลายเดือนก่อน
A sour water stream, which contains 0.20 wt% CO2, 0.15wt% H2S, and 0.1wt% NH3 at a temperature of 8°C and pressure of 1 atm with a mass flow rate of 5000 kg/h, is to be treated by a dry steam at 1.1 atm and a mass flow rate of 1500 kg/h. Source: Kamal I. M. Al-Malah, Aspen Plus: Chemical Engineering Applications, Wiley, 2017. All Aspen simulations in this channel can be downloaded for a donatio...
Aspen Plus: Simulation of a Chemical Looping Combustion System
มุมมอง 2.3Kปีที่แล้ว
Chemical-looping combustion (CLC) is a technology that creates an almost pure CO2 stream. A CLC system typically consists of two parallel processes, the fuel reaction and the air reaction, each taking place in separate fluidized bed reactors. A metal oxide is employed as the oxygen carrier (OC) to transport the oxygen from the air reactor to the fuel reactor. Typical OC species include Fe2O3 / ...
Aspen Plus: Simulation of an internal combustion engine powered by syngas
มุมมอง 1.4Kปีที่แล้ว
Aspen Plus: Simulation of an internal combustion engine powered by syngas
Aspen Plus: Fischer-Tropsch Process using an estimated Distribution of Hydrocarbon Products by ASF
มุมมอง 1.4Kปีที่แล้ว
Aspen Plus: Fischer-Tropsch Process using an estimated Distribution of Hydrocarbon Products by ASF
Aspen Plus: Simulation of a hydrogen liquefaction cycle
มุมมอง 1.8Kปีที่แล้ว
Aspen Plus: Simulation of a hydrogen liquefaction cycle
Aspen Plus: Simulation of H2S and CO2 Removal from Syngas by Cryogenic Distillation
มุมมอง 4.1Kปีที่แล้ว
Aspen Plus: Simulation of H2S and CO2 Removal from Syngas by Cryogenic Distillation
Aspen Plus: Simulation of Cryogenic Air Separation
มุมมอง 4.2Kปีที่แล้ว
Aspen Plus: Simulation of Cryogenic Air Separation
Aspen Plus: Simulation of Fluidized Bed Reactor for Chemical Looping of Synthesis Gas
มุมมอง 2.8Kปีที่แล้ว
Aspen Plus: Simulation of Fluidized Bed Reactor for Chemical Looping of Synthesis Gas
Aspen Plus: Simulation of Biomass to Biochar, Biooil, and non-condensable Gases
มุมมอง 5Kปีที่แล้ว
Aspen Plus: Simulation of Biomass to Biochar, Biooil, and non-condensable Gases
Aspen Plus: Regression of experimental liquid liquid equilibrium data
มุมมอง 733ปีที่แล้ว
Aspen Plus: Regression of experimental liquid liquid equilibrium data
Aspen Plus: Estimation of heat of combustion, heat capacity, enthalpy and density of biomass
มุมมอง 2Kปีที่แล้ว
Aspen Plus: Estimation of heat of combustion, heat capacity, enthalpy and density of biomass
Ansys Fluent: Simulation of Methanol Air Atomizer
มุมมอง 472ปีที่แล้ว
Ansys Fluent: Simulation of Methanol Air Atomizer
ASPEN PLUS: Reactive distillation process for a representative blend of crude bio oils
มุมมอง 717ปีที่แล้ว
ASPEN PLUS: Reactive distillation process for a representative blend of crude bio oils
Aspen Plus: Calculation of the current voltage polarization curve of a PEM electrolysis stack
มุมมอง 4.4Kปีที่แล้ว
Aspen Plus: Calculation of the current voltage polarization curve of a PEM electrolysis stack
MatLab: The finite volume method (video 02), euclidean norm, spectral norm,condition number,residual
มุมมอง 203ปีที่แล้ว
MatLab: The finite volume method (video 02), euclidean norm, spectral norm,condition number,residual
Aspen Plus: Ammonia Recovery from Biogas Digestate by Air Stripping
มุมมอง 4.7Kปีที่แล้ว
Aspen Plus: Ammonia Recovery from Biogas Digestate by Air Stripping
Aspen Plus: Equilibrium Analysis of Acid Base Reactions
มุมมอง 713ปีที่แล้ว
Aspen Plus: Equilibrium Analysis of Acid Base Reactions
bad mesh
for reynolds number of 90000 is it better to model it as k-w?
The video was very helpful. What paper was the simulation based on? I would like to check the results against the paper.
This is so helpful.. Can you please provide some sources for literature review..
Nice one..should have shown some pfd or process description
Thanks. See the cited paper.
its clear-cut explanation sir, thank you. but how do we connect this to CSTR using PID controller?
how can i contact u. i need ur suggestion ( pyrolysis of waste tire with aspen plus v11 ). email pls
kg.engineering.solutions@gmail.com
Is this unit is a part of chlor alkali plant???
Hi sir Thank you for this helpful video I have done all the steps but still there is some errors in compressor as well as mass balance Could you help me to figure out what is the problem?
Hello, I have a problem. The autor uses calculator blocks for pH, Temperature and other inhibitions, but in your model, the calculator block isn't.
What is thermal coupling
What is thermal coupling
Thanks for the video, it is very useful. If I wanted to increase the air inlet flow to obtain greater oxygen flow (approximately double the value in this video) what parameters should I modify? I thank you immensely.
I donated and I got the simulation file and pdf, though in the pdf, it doesn't have sufficient information and the simulation file is unable to open. could you please help me on this sir..Thankyou.
Which Aspen Plus version do you have?
Great work, awesome, Thank you very much for sharing your wonderful work. Please make kind of useful videos do not stop.
How do you deduce the point where mass transfer is limiting?
Thanks for this video. Can this process be applied to any biomass, at least if we know the composition of biomass?
You're welcome. You must know the composition of the products.
it would be nice to have audio with this
Hello, loved to watch your vid with effort. I have a question, why molar mass of biomass is 1kg/kmol? Can you tell me the reason why?
Hello, thanks. Aspen Plus treats the non-conventional biomass as if it has molecular weight of 1 kg/kmol.
Great video please make sure not to add any music else I like it alot
Why your absorber is an heat exchanger ?
See doi:10.1016/j.apenergy.2011.05.018
Hey man please could you share the citations for the kinetic parameters and such? We desperately need them for our university project
Hey, I didn't use a kinetic model in this video.
Hey I was wondering if you could share the source(s) for the various syngas to liquid reactions
Hello sir, I am getting the following required data incomplete error ---- Calculator Block C-1 Block: DRIER Model: RYIELD Block: B2 Model: RYIELD VAPOR PRESSURE MODEL PL0XANT HAS MISSING PARAMETERS: PLXANT/1ST ELEMENT (DATA SET 1) MISSING FOR COMPONENT 4-ETH-02 PLXANT/1ST ELEMENT (DATA SET 1) MISSING FOR COMPONENT METHY-04 PLXANT/1ST ELEMENT (DATA SET 1) MISSING FOR COMPONENT (E)-2-01 PLXANT/1ST ELEMENT (DATA SET 1) MISSING FOR COMPONENT BENZA-01 ****PROPERTY PARAMETER ERROR ERRORS ENCOUNTERED IN CALCULATION OF VAPOR-LIQUID K-VALUES USING OPTION SET RKS-BM FOR KVL. ! Calculations stopped because of missing property parameters ---- how it can be eliminated
What is HHVML - 0 J/kmol that is used to compute the chemical energy of hydrogen?
Please write me the sequence in which 0 J/kmol is used
Thank you for the video , I just wonder how did you choose 2.55 mole/sec for the H2 stream and 1 for CO2 ? Best Regards .
Your're welcome. I varied the H2/CO2 ratio until I got a suitable H2/CO for the FT synthetic.
THANK U, it works!
No please calculate y plus value Ansys
Not using any website
Can you upload a video of the whole simulation process described in the paper?
I want to know that there is the velocity value of 1m/s in reference value. But on boundary you define 0.06m/s.
The reference value is not relevant for the results, so I didn't change it.
Dear, thanks for the video, it will be very helpful. I'm simulating a plant of methanol production via CO2 hydrogenation based on an article, can you help me with the simulation?
Hi, you're welcome. Please email me how I can help you.
Sir how can i make this cycle by using waste heat
Thank you so much from Thailand!
You are welcome😀
Dear sir Can you please make same rankine cycle according to reference paper i am facing Some problem while trying to make rankine cycle according to reference paper.
As soon as I find time for the simulation I will try it.
I keep on getting an error from the second flasher! Saying that its not in balance, I assume its from the recycling streams. How could I fix that?
same status :(
@@Dinotaeng I had the same problem. You can easily resolve it by specifying S12 and S13 as tear streams (recycle streams) in the Tear tab under convergence.
Great video, do you have any video for the Aspen simulation of Pyrolysis process using Kinetic model?
Dear Juniors ,who come to see the videos from ME CUET,Bangladesh ,be cautious to take thesis on biomass gasification simulation topic as B.Salam Sir not like at all this type of simulation . So try to add practical experiment with this topic.
I completed successfully my undergrade thesis .I mailed u for help but u couldn't help me directly as u have paid group.I am the first of my Mechanical Department of CUET,Bangladesh, done the thesis on ASPEN PLUS simulation .So that time was difficult for me to work on this topic lonely.But Ur free utube videos as well as @HotSpot videos helped me a lot throughout last one year to did my thesis.Thank u very much.
Many errors are occuring in our model Can u please help with this sir
Great video. I read the original paper, and the authors have used Aspen Custom Modeler to simulate the stack. At least, that paper is peer-reviewed. How do you know for sure that modeling the electrolysis stack using the R-stoic is correct? How do you ensure the accuracy and appropriateness of your method? Please let me know, thanks.
Hi, thank you. I did not write anywhere that I simulated the model from the paper you mentioned. I wrote in the presentation that the video proposes a model of an alkaline electrolysis system.
@@kgengineeringsolutions Thanks for the reply. Can you let me know how you ensured the accuracy of the model you proposed?
@@alexrider606 You're welcome. The equations I used in this video are from the two publications I cited. If you want to check the accuracy of the equations, you should do a literature search. For further questions, do not hesitate to write to me.
Hi there, I observed your calculation of the fractional conversion of water in the Excel file. There, you divide the mass flow of water per hour, by 0.65*900. What is this fractional mass flow you divide it by?
Hi, 0.65: mass fraction of H2O. 900: mass flow of KOH-H2O
Hey, sir can you please help me i am working on now a solar assisted biogas plant project for graduation project by using dwsim software, are you familiar with the dwsim software? Can you please share for me your email.
i downloaded the simulation , what version is it ?
V12
I am puzzled as to how the temperature can arbitrarily be "estimated". And the given relief temperature is grossly incorrect as if it is pressurized to above 6 bars, the temperature will obviously be higher than the stream temperature i.e 108 degree C. that brings me to my question. when I was simulating an external fire case for water, we assume the saturation point is when it vaporizes and relieves through the valve. and we estimated the saturation temperature to be very much greater than the calculated relieving temperature value. need some guidance on that. thanks in advance.
How can we calculate the dimensions ?
Great video, If I integrate this electrolyte system with the gasification process, then the suggested ELECNRTL equation of states may not be useful. Can you please suggest a better method for the combined process model?
great tutorial! how was the experimental data measured?
Thanks. Unfortunately, I don't know any more.
hi! i would love to have the simulation files but your link doesnt allow me to donate from india!
Hi, please contact me by email
@@kgengineeringsolutions I’ve emailed you sir
@@kgengineeringsolutions I have sent you a mail sir. It would be great if you could send it asap.
can you a rate based model distillation for acid gas capture?
Thank you so much can you share the ppt
You're welcome. See the video description. You can download it for a small donation.