Wahab Maqbool

6 Questions 2 Answers 0 Followers

Questions related from Wahab Maqbool

Changing Aspen Plus non-conventional component into a mixture of few conventional compounds?

I have performed a bio-refinery simulation on Aspen Plus using non-conventional components. Now, what I am willing to do is to specify one of the product (non-conventional) into a mixture of some...

13 February 2020 5,713 4 View

Solubility data requirement for supercritical gas extraction process design?

Hello, Please let me know that is solubility data of compound in supercritical phase is sufficient to model the gas extraction process or liquid phase composition (CO2 solubility in compound) is...

12 October 2016 6,247 3 View

Phase behavior modeling of high-pressure system in Aspen Plus?

I want to model the supercritical separation process in aspen plus. This involves phase behavior modeling of supercritical CO2-Solid and supercritical CO2-Liquid systems. I know how to use Aspen...

31 January 2016 7,242 2 View

How can I do MATLAB curve fitting to a custom model with two independent variables?

I have data in which response is dependent upon two variables. Three data series are given:[x1, y1], [x2, y2], [x3, y3]. On excel (file attached) I have made XY scatter plot which gives three...

24 May 2015 2,845 1 View

What does the solubility y * 10^6 means (for caffeine solubility in supercritical CO2)? usually in solubility data table 3rd column is y * 10^n?

For example I am attaching a solubility data table of caffeine with CO2. What does this y * 10^6 means? what are the units here? Thanks

02 February 2015 1,862 2 View

How can we model the solubility of compounds present in hydrothermal liquefaction bio-oil with supercritical CO2?

We have bio-oil of varying composition. We want to model supercritical fluid extraction system by accounting the solubility of different compounds of bio-oil like alcohols, phenols and sugars...

21 January 2015 9,424 1 View