gustavochm

Hey Danlira, Sorry about my late response, I've been busy 🥲. I have to say that I am not an expert on generating saturation envelopes. For what I see the...

Hey Danlira, So basically, the bubble and dew points functions included in phasepy include two methods to solve the phase equilibria. 1. The first method uses an Newton method to...

> I'm working on my own phase envelope printer. Will make the code available later after I test it properly and package it... > >  That looks...

Hi [YouHyin](https://github.com/YouHyin), This is something I didn't consider before. when I implemented this SAFT I only included the second-order parameters of the following paper: Haslam, A. J., González-Pérez, A., Di...

Hi [YouHyin](https://github.com/YouHyin), Thank you for coding this. I'm afraid I haven't had the time to go through it yet. Once the functions are available on that file they should be...

Hi [YouHyin](https://github.com/YouHyin), Just an update here. I pushed an updated version of sgtpy into PyPI. The new version includes molecular parameter obtained in the following articles: [Febra et al. (2021)](https://doi.org/10.1016/j.fluid.2021.113002),...

Have you updated to the most recent version? When updating the code, I realized there was a bug when adding new association interactions to the new database. Basically, there were...

Hi [YouHyin](https://github.com/YouHyin), I'm glad to see that for DEA, it is working as expected now. I understand your point about MAPA; the thing is that I coded the second-order interactions...

Hi [YouHyin](https://github.com/YouHyin), Thank you for your question. I coded both SAFT-VR-Mie and SAFT-gamma-Mie to be used with "n" numbers of components. I know most examples are written for binary mixtures,...

Hi [YouHyin](https://github.com/YouHyin), Let me know if I got this right. Let's take plot (d) as an example. This is a mixture of diethanolamine, CO2, and water. - The weight fraction...