Activity for Mehul Sutariya
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Mehul Sutariya modified a comment on discussion Help
Error "This application requires a Java Runtime Environment 8 or higher 1.8.0" I am not able to see any log file. Edit: As soon as I click okay it redirects me to https://www.java.com/en/download/
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Error "This application requires a Java Runtime Environment 8 or higher 1.8.0" I am not able to see any log file.
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Globonote requires a Java SE 8 and my corporate pc has Amazon Corretto JRE 8. But i am not able to run globonote with JRE 8. Is there any possiblity to run it with Amazon Corretto JRE 8? I am using any platform zip file as portable app.
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Hello everyone, I am working on developing a process for green H2 generation via electrolysis using a KOH solution (Water - KOH system). However, I am facing a challenge as there is currently no thermodynamics model available for the H2O-KOH system in DWSIM. I have looked into using the Reaktoro model for aqueous solutions, but it does not currently support KOH in DWSIM. I am seeking advice on how to proceed. Does anyone have suggestions for adding KOH compatibility to Reaktoro? Alternatively, are...
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Hey Frank; Please look at the attached screenshot, with the same condition; I run it three time but it gives me different result every time. I don't have that much experiance in these stuff but is it acceptable? or i am makeing some mistakes. Or it is a bug.
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Valve-01 in attached simulation give different result at every run. Not able to understand the problem. Please help me.
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VOTE: orangefox best recovery i ever use
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Thank you Daniel. Now it is working perfectly on classic UI.
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Whenever I click on open python script editor; error "Object reference not set to an instance of an object." occure. I already installed ironpython, as well as I also set path for that. I use the latest version on DWSIM on windows 10 with classic UI. In cross platfrom it work perfact. System.NullReferenceException: Object reference not set to an instance of an object. at DWSIM.UnitOperations.EditingForm_CustomUO_ScriptEditor.btnHighlightSpaces_Click(Object sender, EventArgs e) in C:\Users\Daniel\source\repos\DanWBR\dwsim5\DWSIM.UnitOperations\Editing...
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Thanks for your experties Mr. Frank. I started work on process modeling and simulation at starting of my 3rd year of chemical enginerring. So can you help with some material or books?
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referance doi: 10.1021/ie9012387
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i got a error in CSTR 'index was out side the bounds of array' can any one help me to solve that problem DWSIM 5.6u9, windows 10
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The name and the unit of the x-axis are cut and when i try to change the page setting it only effect on this same graph plot (only size are vary of this image) Actually i want to save that graph for my simulation study for my internship project report but due to that i have to draw the graph by using excel. But by the way; thanks for providing this powerful sensitivity analysis tool.
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The name and the unit of the x-axis are cut and whem i try to change the page setting it only effect on this same graph plot (only size are vary of this image) Actually i want to save that graph for my simulation study for my internship project report but due to that i have to draw the graph by using excel. But by the way; thanks for providing this powerful sensitivity analysis tool.
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oh thanks i got it but i found one other problem or may be small bug have a look to attached image
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there is any way to save a tabulated data sheet generated by the sensitivity analysis tool??
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hello; I try to convert the Fortran membrane model created for the aspen plus into the DWSIM python script; I have to use the UNIQUAC model for the calculation of enthalpy and other properties. I have a compound fraction data, total mole flow rate, temperature and the phase (two homogeneous phases are there; one is pure liquid and one is pure vapor phase; data are there for both phase) https://pubs.acs.org/doi/abs/10.1021/ie801428s base flowsheet and Fortran coding(page no 3488(5th of pdf); calculation...
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hello; I try to convert the fortran membrane model created for the aspen plus into the DWSIM python script; I have to use the UNIQUAC model for the calculation of entalpy and other properties. I have a compound fraction data, total mole flow rate, temperature and the phase (two homogeneous phase are there; one is pure liquid and one is pure vapor phase; data are there for both phase) https://pubs.acs.org/doi/abs/10.1021/ie801428s base flowsheet and fortran coding(page no 3488(5th of pdf); calculation...
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while using a create and connect button to generate the material stream it gives me an error "conversion from string to "" to type boolean is not valid"
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hello, can any one help me, on how to find the enthalpy of liquid or vapor by using temeprature, pressure, mass(or mol) fraction and flowrate; by using selected property package inside the scripter
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here in this screen shot you cleary see that the conversion of icon is not fully devloped
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i set the reaction parameter as phase: mixture and the basis as: molar concentration But it auto change by DWSIM although i enter the volueme of the CSTR it till gives me an error that cstr volume is not define
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i set the reaction perameter as phase: mixture and the activity as: molar coefficint But it autochange by DWSIM although i enter the volueme of the CSTR it till gives me an error that cstr volume is not define
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i got a error in kinetic reaction, when ever i use number other than 1 it give me error like that "given key is not present"
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while downloading other connected software. it gives me a error that connection is not available
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error in 5.3 NRTL: missing perameter for binary pair
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it works
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Sry for the misunderstanding but in that column, i going to separate ethanol water only, feed stream has 0 mole fraction of ethylene oxicide,
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Sry for the misunderstanding but in that column, i going to separate ethanol water only, feed stream has 0 mole draction of ethylene oxicide,
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Sry for the misunderstanding but in that column, i going to separate ethanol water only, fess stream has 0 mole draction of ethylene oxicide,
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error in 5.3 NRTL: missing perameter for binary pair
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error in 5.3 NRTL: missing perameter for binary pair
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i figure out the problem, it is type of weired error i modify the setting of date shown by windows(i make in dd-MMM) after reset it, it works
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i got error while saving file, i also try as admin but same problem, also reinstall it.
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i got error while saving file, i also try as admin but same problem, also reinstall it.
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i got error while saving file, i also try as admin but same problem, also reinstall it.
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heat exchanger hot and cold fluid outlet temprature perameter
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heat exchanger hot and cold fluid outlet temprature perameter
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heat exchanger hot and cold fluid outlet temprature perameter
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heat exchanger hot and cold fluid outlet temprature perameter
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i use a solution inspector to show the detail calculation of my projects' flowsheet but it dose not show me any kins of formula etc. it show me a line like this
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i use a solution inspector to show the detail calculation of my projects' flowsheet but it dose not show me any kins of formula etc. it show me a line like this (https://drive.google.com/file/d/15d1pQsIy70YubqCyXzvtLfOrAc79Q0I3/view?usp=sharing)
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i use a solution inspector to show the detail calculation of my projects' flowsheet but it dose not show me any kins of formula etc. it show me a line like this (https://drive.google.com/file/d/15d1pQsIy70YubqCyXzvtLfOrAc79Q0I3/view?usp=sharing)
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i use a solution inspector to show the detail calculation of my projects' flowsheet but it dose not show me any kins of formula etc. it show me a line like this (https://drive.google.com/file/d/15d1pQsIy70YubqCyXzvtLfOrAc79Q0I3/view?usp=sharing)
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i use a solution inspector to show the detail calculation of my projects' flowsheet but it dose not show me any kins of formula etc. it show me a line like this
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