[gmx-users] Heat of vap
Elisabeth
katesedate at gmail.com
Mon Apr 4 00:49:39 CEST 2011
>
> Elisabeth wrote:
>
>> Dear David,
>>
>> I followed your instructions and calculated Heat of vaporization of my
>> alkane once with one molecule in gas phase (no cutoff) and once with
>> equivalent number of molecules as in liquid phase as Justin suggested.
>> Results are as follows:
>>
>>
> To get heat of vaporization, you shouldn't be simulating just a single
> molecule in the gas phase, it should be an equivalent number of molecules as
> you have in the liquid phase.
>
> Hello David and Justin,
My explanation was not clear. Below is the results for liquid phase and for
gas phase I tried two cases: one single molecule and the other time for
equivalent number of molecules as in liquid phase and thats why results are
very similar. ( However Justin says one single molecule is not correct. I
think when cutoffs is set to zero only bonded terms are treated and even
where there are many particles in gas phase to get energies per mole of
molecules i.e g_energy -nmol XXX must be used so values should be colse to a
single molecules case.. please correct me! Anyway results for gas phase are
close and this is not the issue now).
Liquid phase:
Energy Average Err.Est. RMSD Tot-Drift
-------------------------------------------------------------------------------
LJ (SR) -27.3083 0.01 0.296591 -0.0389173
(kJ/mol)
Coulomb (SR) 6.00527 0.0074 0.122878 0.00576827
(kJ/mol)
Coul. recip. 5.59559 0.0032 0.0557413 0.00316957
(kJ/mol)
Potential *34.6779 * 0.025 1.03468 -0.11177
(kJ/mol)
Total Energy 86.4044 0.026 1.44353 -0.112587
(kJ/mol)
> *one single molecule in gas phase*
>>
>>
>> Energy Average Err.Est. RMSD Tot-Drift
>>
>> -------------------------------------------------------------------------------
>> LJ (SR) -2.24473 0.073 1.292 0.342696
>> (kJ/mol)
>> Coulomb (SR) 11.5723 0.55 2.17577 -2.33224
>> (kJ/mol)
>> Potential * 59.244 * 0.94 10.9756 6.35631
>> (kJ/mol)
>> Total Energy 106.647 1 15.4828 6.78792
>> (kJ/mol)
>>
>> *equivalent number of molecules as in liquid* ( large box 20 nm)
>>
>> Statistics over 1000001 steps [ 0.0000 through 2000.0000 ps ], 4 data sets
>> All statistics are over 100001 points
>>
>> Energy Average Err.Est. RMSD Tot-Drift
>>
>> -------------------------------------------------------------------------------
>> LJ (SR) -2.16367 0.053 0.171542 0.374027
>> (kJ/mol)
>> Coulomb (SR) 11.2894 0.23 0.49105 -1.44437
>> (kJ/mol)
>> Potential * 63.2369 * 1.1 2.47211 7.69756
>> (kJ/mol)
>> Total Energy 114.337 1.1 2.65547 7.72258
>> (kJ/mol)
>>
>>
>> Since pbc is set to NO molecules leave the box and I dont know if this
>> all right. I hope the difference is acceptable...!
>>
>>
> For "pbc = no" there is no box.
>
>
> 0- I am going to do the same calculation but for some polymers solvated in
>> the alkane. For binary system do I need to look at nonboded terms? and then
>> run a simulation for a single polymer in vacuum?
>>
>> Can you please provide me with a recipe for Delta Hvap of the solute in a
>> solvent?
>>
>>
> The method for calculating heat of vaporization is not dependent upon the
> contents of the system; it is a fundamental thermodynamic definition. Heat
> of vaporization is not something that can be calculated from a solute in a
> solvent. You can calculate DHvap for a particular system, but not some
> subset of that system.
>
> Thanks Justin. I am interested in the energy required to vaporize the
> solute in a particular solvent not the whole DHvap of the mixture. do you
> think this can be achieved by calculating nonbonded energies between solute
> and solvent? ( defining energy groups ..)
>
>
>> 1- If I want to look at nonboded interactions only, do I have to add
>> Coul. recip. to [ LJ (SR) + Coulomb (SR) ] ?
>>
>>
> The PME-related terms contain both solute-solvent, solvent-solvent, and
> potentially solute-solute terms (depending on the size and nature of the
> solute), so trying to interpret this term in some pairwise fashion is an
> exercise in futility.
>
> What you mean is when one uses PME interaction energies between components
> can not be decomposed? So the energy groups I defined to extract nonbonded
> energies are not giving correct values? Sofar I have been defining energy
> groups to calculate nonbonded terms between components _A-A A_B... I hope I
> have not been doing thing wrongly!
>
Please help me out!
Thanks,
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