No,Nanoparticles are in pure state and they want to absorb asphaltene dissolved in toluene. I want to have data on molar volume and surface tension of nanoparticles in pure state (i.e. before absorption)
Hi .how can i calculate the molar volume and surface tension of nanoparticles ? shoud i have to calculate? or these parameters is available in tables or sth?
Hey guys
we know damkohler number indicate the volume of reactor. if this number be small, what happen to design of reactor? ( its influence on design of reactor)
Hi , this is my equation :
μA= μA0 + RTlnaA
A is the asphaltene in toluene solution . i want to calculate μA in different temperatures. where can i get μA0 and aA? tables? other equations?
μA0 is the standard chemical potential of asphaltene and aA is the asphaltene activity in solution.
I think yes, solution is ideal. if its ideal,what is the fugacity of asphaltene in solution equal to? ( i mean which equation should I use? ), and why determining fugacity of asphaltene on nanoparticles is complicated?
Yes, for a better understanding, these images show what i need
For the fugacity of asphaltenes in the solid and liquid phase, i don't know what equations of state can be used to include fugacity coefficients?
after doing this, i use the equation that encluding Z, instead of fugacity...
What do you mean by simply can not? what i have to do? Do you know what equations should I make instead of fugacity of asphaltenes on solid and in solution?
Hi guys
I want to model the adsorption of asphaltenes on nanoparticles from a thermodynamic equilibrium solution ( this is my thesis ). from this way, I want to show how much asphaltene is adsorbed on nanoparticles at different temperatures and pressures (without using of isotherms of...