Hi, none of them are Codes. In any case, there is no specific standard for Gas sweetening process.

Hi, I use many references for my videos, but you can look for GPSA Electronic Databook or Grundfos Pump Handbook

@@jefersoncostaengineer Thanks sir for the information

You can get the ebook at jefersoncosta.com/vijaysarathy

Thanks a lot 😍

Hi, I have training for P&ID where I teach basic commands (essential) to update P&ID drawing without being a AutoCAD user. More information on this link: hotmart.com/en/club/inprocessbooster/products/1557662 I do not have dedicated training to AutoCAD, sorry. 😅

There is a specific tool to deal with polymers called "Aspen polymer". In any case, you can use hypothetical component if it fit your needs 😇

Thanks for letting me know 😁

Hi Steven, you do not have this option. The main purpose of Aspen Plus is Heat and material balance, not equipment design 😅 With exception to HX where Aspen Plus can be linked to EDR, and PRD using the Safety Analysis.

Hi, to be able to simulate an absorption process you need to find the components and use the appropriate thermodynamic package in the process simulator. I am not familiar with H2O-LIBR single stage vapor absorption. But you can start verifying the conditions above 😇

Hi, you have two options to have a better experience, increase your internet quality and/or your screen size. All videos are uploaded in 720p and can be watched without losing quality resolution up to a 32" TV screen. 😇

Ola, para gerar um grafico de envelope no Unisim voce precisa associar uma utility a sua corrente a ser analisada. Com base na composicao da corrente e no pacote termodinamico utilizado o unisim vai montar o grafico e disponibilizar os dados em tabela. Se voce quiser pode exportar os/copiar os dados para excel e trabalhar com eles do modo que for necessario.

@@jefersoncostaengineer obrigado pelo retorno..

Hi, if you are interested in doing a master in France, you can try an application for IFPEN program. More information on their website 😇. Eventually, you can get a sponsorship.

Thankyou for responding. Are you suggesting the IFP school?

I am having a hard time finding masters degree in chemical engineering. France is one of the biggest hubs in europe when is comes to chemical industry. Why are there very less programs available for masters? Additionally it would be great if suggest few more for masters. I really appreciate your insights and experience. Thankyou

correct 👍

You did my day Mariana. Merci 😄

Hi, unfortunately the spreadsheet is not available for sharing. Sorry 😅

Thanks a lot for letting me know 😄.

Thanks a lot 😍

You did my day. Thanks a lot for your feedback 😍

Hi, it will depending on what you are doing and how much accurate you need to be on your calculations. For instance, are you planning to size the exchanger inlet nozzle? use the saturated vapor density. Is it for nozzle outlet, use saturated condensate density. Do you need to perform pressure drop calculation on tubes? you can start with an average density between saturated vapor and condensate. if you need to be more accurate, eventually you will need to split the exchanger in section and apply the correct density for each section. In summary, first let clear what you need do, later, identify the level of accuracy you need to achieve, and finally, select the parameters to comply with both previous conditions 😇

Thanks for sharing your comment 😁

Merci mon ami 😍

Hi, I do not use COCO software. You can use DWSIM to simulate water gas shift reactions.

Thanks a lot for making my day 😍

I will consider your request for future videos 😇

Hi, let me verify the news. I will check if can add something from the chemical process engineering and plant design point of view😇 Thanks for suggesting new themes to the channel 😁

Hi, when verifying safety scenarios the chemical process engineer must evaluate multiple scenarios and decide which one is applicable for the case. This video is dedicated for tube rupture 😇

Hi, you can find the telegram channel on this link t.me/jefersoncostaengineer. All my social media can be found in www.jefersoncosta.com 😇

Excellent Mojtaba. Do you have any experience with job abroad? Share with us 😇

That is an option, but to be sincere I prefer to walk because I use my time better this way :)

Hi Fabian, safety matrix like the ones used in HAZOp links likehood with severity. The intersection between them permits the user to evaluate the level of risk. Cause and effect matrix in the other hand, links actions trigged by an specific cause. In summary, C&E matrix is for action evaluation, while Safety matrix is for risk evaluation. 😇

I m chemical engineering , Translate text with your camera I changed the concentration of the distillation tower with a new design

You can download from this link jefersoncosta.com/free-process-simulation-software-download

Thanks my friend. Yes, I am back 😁

You both are amazing..... Your knowledge and explanation method are fantastic

@@Sqb1998 thanks my friend, here to help! keep supporting the community :)

@@jefersoncostaengineer nice to see you back!

In general, the pipe size will be the same as the rupture disk size. Detailing piping sizing depends on relief destination.

Looking at plant design sequencial steps, design pressure will never be greater that MAWP because we inform design pressure in the datasheet. And based on design pressure and temperatura, vendor will perform Wall thickness calculation to reach a value iqual or greater than design pressure. MAWP is calculate based on material thickness.

@@jefersoncostaengineer Thank you so much

Thank for the suggestion. I will consider for future videos 😇

Instead of thanking him for sparing some of his time to share the knowledge and expertise he has with us for free?

Noted. I will verify what I can prepared related to Flaring. Thanks a lot for the suggestion 😁

@@jefersoncostaengineer Much appreciated Jeferson!

Merci Hussein 😄

Noted. I will return with more about my personal experiences soon 😇

Thank my friend 😁

Yes, they can. However, it depends on many factors. From candidate side it is important to have Patience, persistence and a plan.