Re: [gmx-users] Heat of vap

2011-04-04 Thread David van der Spoel

On 2011-04-04 01.32, Justin A. Lemkul wrote:



Elisabeth wrote:





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


What is not correct is comparing the potential energy of a liquid system
of many molecules with a gas phase of a single molecule. Whether or
not that was something you did still is not entirely clear, but to be
very clear, that's what I was saying is incorrect to do. DHvap is based
on conversion of equivalent systems between liquid and gas.


treated and even where there are many particles in gas phase to get


This is incorrect. Cutoffs of zero mean that all nonbonded interactions
are calculated, they are not truncated.


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).



You shouldn't need -nmol for any of this. Simply take the potential
energy of the two systems (with equivalent numbers of molecules) and
apply the formula I gave you several emails ago.

NOO


1 molecule in the gas phase  - Epot(g) in your case 59.2 kJ/mol
N molecules in the liquid phase - Epot(l) (since this is per mole you 
DO need the -nmol option) in you case 34.7 kJ/mol
DHvap = Epot(g) + kBT - Epot(l) = 59.2+2.5-34.7 = 27 kJ/mol which is 
quite close to hexane (28.9 kJ/mol).




-Justin


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 101 steps [ 0. through 2000. ps ], 4
data sets
All statistics are over 11 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 

Re: [gmx-users] Heat of vap

2011-04-03 Thread David van der Spoel

On 2011-04-03 02.15, 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:

*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   0.552.17577   -2.33224
(kJ/mol)
Potential *  59.244 *  0.9410.97566.35631  (kJ/mol)
Total Energy106.647  115.48286.78792
(kJ/mol)

*equivalent number of molecules as in liquid* ( large box 20 nm)
This is not correct. You need to simulate the liquid in the liquid 
state. Now you have a dilute gas instead, hence the energy difference is 
very small and due to dimers and trimers in the gas phase. Just extract 
Epot from your previous liquid phase calculations.





Statistics over 101 steps [ 0. through 2000. ps ], 4 data sets
All statistics are over 11 points

Energy  Average   Err.Est.   RMSD  Tot-Drift
---
LJ (SR)-2.16367  0.053   0.171542   0.374027
(kJ/mol)
Coulomb (SR)11.2894   0.230.49105   -1.44437
(kJ/mol)
Potential *  63.2369 *1.12.472117.69756  (kJ/mol)
Total Energy114.3371.12.655477.72258
(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...!

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?


1- If I want to look at nonboded interactions only, do I have to add
Coul. recip.  to [ LJ (SR)  + Coulomb (SR) ] ?


coulombtype =  PME
vdw-type=  Shift
rcoulomb-switch =  0
rvdw-switch =  0.9
rlist   =  1.2
rcoulomb=  1.2
rvdw=  1.0


ff: OPLSAA


Appreciate your help,
Best,




--
David van der Spoel, Ph.D., Professor of Biology
Dept. of Cell  Molec. Biol., Uppsala University.
Box 596, 75124 Uppsala, Sweden. Phone:  +46184714205.
sp...@xray.bmc.uu.sehttp://folding.bmc.uu.se
--
gmx-users mailing listgmx-users@gromacs.org
http://lists.gromacs.org/mailman/listinfo/gmx-users
Please search the archive at 
http://www.gromacs.org/Support/Mailing_Lists/Search before posting!
Please don't post (un)subscribe requests to the list. Use the 
www interface or send it to gmx-users-requ...@gromacs.org.

Can't post? Read http://www.gromacs.org/Support/Mailing_Lists


Re: [gmx-users] Heat of vap

2011-04-03 Thread Elisabeth

 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  *0.0251.03468   -0.11177
(kJ/mol)
Total Energy86.4044  0.0261.44353  -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   0.552.17577   -2.33224
  (kJ/mol)
 Potential  *  59.244 *  0.9410.97566.35631
  (kJ/mol)
 Total Energy106.647  115.48286.78792
  (kJ/mol)

 *equivalent number of molecules as in liquid* ( large box 20 nm)

 Statistics over 101 steps [ 0. through 2000. ps ], 4 data sets
 All statistics are over 11 points

 Energy  Average   Err.Est.   RMSD  Tot-Drift

 ---
 LJ (SR)-2.16367  0.053   0.171542   0.374027
  (kJ/mol)
 Coulomb (SR)11.2894   0.230.49105   -1.44437
  (kJ/mol)
 Potential *  63.2369*1.12.472117.69756
  (kJ/mol)
 Total Energy114.3371.12.655477.72258
  (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,
-- 
gmx-users mailing listgmx-users@gromacs.org
http://lists.gromacs.org/mailman/listinfo/gmx-users
Please search the archive at 
http://www.gromacs.org/Support/Mailing_Lists/Search before posting!
Please don't post (un)subscribe requests to the list. Use the 
www interface or send it to gmx-users-requ...@gromacs.org.
Can't post? Read 

Re: [gmx-users] Heat of vap

2011-04-03 Thread Justin A. Lemkul



Elisabeth wrote:





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 


What is not correct is comparing the potential energy of a liquid system of many 
molecules with a gas phase of a single molecule.  Whether or not that was 
something you did still is not entirely clear, but to be very clear, that's what 
I was saying is incorrect to do.  DHvap is based on conversion of equivalent 
systems between liquid and gas.


treated and even where there are many particles in gas phase to get 


This is incorrect.  Cutoffs of zero mean that all nonbonded interactions are 
calculated, they are not truncated.


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).




You shouldn't need -nmol for any of this.  Simply take the potential energy of 
the two systems (with equivalent numbers of molecules) and apply the formula I 
gave you several emails ago.


-Justin


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  *0.0251.03468   -0.11177  
(kJ/mol)
Total Energy86.4044  0.0261.44353  -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   0.552.17577  
-2.33224  (kJ/mol)
Potential  *  59.244 *  0.9410.9756  
 6.35631  (kJ/mol)
Total Energy106.647  115.4828  
 6.78792  (kJ/mol)


*equivalent number of molecules as in liquid* ( large box 20 nm)

Statistics over 101 steps [ 0. through 2000. ps ], 4
data sets
All statistics are over 11 points

Energy  Average   Err.Est.   RMSD  Tot-Drift

---
LJ (SR)-2.16367  0.053   0.171542  
0.374027  (kJ/mol)
Coulomb (SR)11.2894   0.230.49105  
-1.44437  (kJ/mol)
Potential *  63.2369*1.12.47211  
 7.69756  (kJ/mol)
Total Energy114.3371.12.65547  
 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, 

Re: [gmx-users] Heat of vap

2011-04-02 Thread Justin A. Lemkul



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.



*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   0.552.17577   -2.33224  
(kJ/mol)
Potential  *  59.244 *  0.9410.97566.35631  
(kJ/mol)
Total Energy106.647  115.48286.78792  
(kJ/mol)


*equivalent number of molecules as in liquid* ( large box 20 nm)

Statistics over 101 steps [ 0. through 2000. ps ], 4 data sets
All statistics are over 11 points

Energy  Average   Err.Est.   RMSD  Tot-Drift
---
LJ (SR)-2.16367  0.053   0.171542   0.374027  
(kJ/mol)
Coulomb (SR)11.2894   0.230.49105   -1.44437  
(kJ/mol)
Potential *  63.2369*1.12.472117.69756  
(kJ/mol)
Total Energy114.3371.12.655477.72258  
(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.




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.


-Justin

coulombtype =  PME  
vdw-type=  Shift   
rcoulomb-switch =  0  
rvdw-switch =  0.9
rlist   =  1.2   
rcoulomb=  1.2
rvdw=  1.0   



ff: OPLSAA


Appreciate your help,
Best,



--


Justin A. Lemkul
Ph.D. Candidate
ICTAS Doctoral Scholar
MILES-IGERT Trainee
Department of Biochemistry
Virginia Tech
Blacksburg, VA
jalemkul[at]vt.edu | (540) 231-9080
http://www.bevanlab.biochem.vt.edu/Pages/Personal/justin


--
gmx-users mailing listgmx-users@gromacs.org
http://lists.gromacs.org/mailman/listinfo/gmx-users
Please search the archive at 
http://www.gromacs.org/Support/Mailing_Lists/Search before posting!
Please don't post (un)subscribe requests to the list. Use the 
www interface or send it to gmx-users-requ...@gromacs.org.

Can't post? Read http://www.gromacs.org/Support/Mailing_Lists


Re: [gmx-users] Heat of vap

2011-03-31 Thread Elisabeth
in your mail:

On 30 March 2011 15:30, Justin A. Lemkul jalem...@vt.edu wrote:



 Elisabeth wrote:

 Dear all,

 I intend to obtain vaporization heat per volume for a /pure alkane
 system/.  Here is the steps I am taking. Please correct me.

 1- Obtain total energy of system (kinetic+potential) and divide by number
 of molecules to obtain energy per mol of molecules. g_energy -f *.edr -nmol
 XXX
 2- Obtain total energy of a single molecule (use pbc).
 3- Subtract step 2 from step 1.
 4- Divide by simulation box volume.

 My questions is:

 in step 2 : what should be the box size? The same size as in 1 or it does
 not matter? (step 1 is done for the actual denstiy)


 More troubling, how does one define the energy of a molecule?  If you use
 any sort of long-range algorithms (especially PME, but also dispersion
 correction), you can't simply decompose the system like this.

 Thanks Justin and David.

I have been trying to find the article in which this has been presented. If
you have time Please see page 5937, right column, equation 11. I think I
made a mistake and I dont have to include kinetic energy, Only nonboded
energies!?

http://pubs.acs.org/doi/pdfplus/10.1021/jp0707539



 In the derivation of recent Gromos96 parameter sets, the heat of
 vaporization is quite simple:

 DHvap = Ugas - Uliq + RT


1- So  Uliq is the total energy or only potential (no kinetic)
2- How can I compute Ugas? I have liquid now...


  Thank you,
 Regards,


 --
 

 Justin A. Lemkul
 Ph.D. Candidate
 ICTAS Doctoral Scholar
 MILES-IGERT Trainee
 Department of Biochemistry
 Virginia Tech
 Blacksburg, VA
 jalemkul[at]vt.edu | (540) 231-9080
 http://www.bevanlab.biochem.vt.edu/Pages/Personal/justin

 

 --
 gmx-users mailing listgmx-users@gromacs.org
 http://lists.gromacs.org/mailman/listinfo/gmx-users
 Please search the archive at
 http://www.gromacs.org/Support/Mailing_Lists/Search before posting!
 Please don't post (un)subscribe requests to the list. Use the www interface
 or send it to gmx-users-requ...@gromacs.org.
 Can't post? Read http://www.gromacs.org/Support/Mailing_Lists

-- 
gmx-users mailing listgmx-users@gromacs.org
http://lists.gromacs.org/mailman/listinfo/gmx-users
Please search the archive at 
http://www.gromacs.org/Support/Mailing_Lists/Search before posting!
Please don't post (un)subscribe requests to the list. Use the 
www interface or send it to gmx-users-requ...@gromacs.org.
Can't post? Read http://www.gromacs.org/Support/Mailing_Lists

Re: [gmx-users] Heat of vap

2011-03-31 Thread Justin A. Lemkul



Elisabeth wrote:



in your mail:

On 30 March 2011 15:30, Justin A. Lemkul jalem...@vt.edu 
mailto:jalem...@vt.edu wrote:




Elisabeth wrote:

Dear all,

I intend to obtain vaporization heat per volume for a /pure
alkane system/.  Here is the steps I am taking. Please correct me.

1- Obtain total energy of system (kinetic+potential) and divide
by number of molecules to obtain energy per mol of molecules.
g_energy -f *.edr -nmol XXX
2- Obtain total energy of a single molecule (use pbc).
3- Subtract step 2 from step 1.
4- Divide by simulation box volume.

My questions is:

in step 2 : what should be the box size? The same size as in 1
or it does not matter? (step 1 is done for the actual denstiy)


More troubling, how does one define the energy of a molecule?  If
you use any sort of long-range algorithms (especially PME, but also
dispersion correction), you can't simply decompose the system like this.

Thanks Justin and David.

I have been trying to find the article in which this has been presented. 
If you have time Please see page 5937, right column, equation 11. I 
think I made a mistake and I dont have to include kinetic energy, Only 
nonboded energies!?


http://pubs.acs.org/doi/pdfplus/10.1021/jp0707539



What is cohesive energy and how does it relate to the quantity you're trying to 
calculate?


 


In the derivation of recent Gromos96 parameter sets, the heat of
vaporization is quite simple:

DHvap = Ugas - Uliq + RT


1- So  Uliq is the total energy or only potential (no kinetic)


Potential.


2- How can I compute Ugas? I have liquid now...



Run a simulation in the gas phase.

-Justin



Thank you,
Regards,


-- 



Justin A. Lemkul
Ph.D. Candidate
ICTAS Doctoral Scholar
MILES-IGERT Trainee
Department of Biochemistry
Virginia Tech
Blacksburg, VA
jalemkul[at]vt.edu http://vt.edu | (540) 231-9080
http://www.bevanlab.biochem.vt.edu/Pages/Personal/justin



-- 
gmx-users mailing listgmx-users@gromacs.org

mailto:gmx-users@gromacs.org
http://lists.gromacs.org/mailman/listinfo/gmx-users
Please search the archive at
http://www.gromacs.org/Support/Mailing_Lists/Search before posting!
Please don't post (un)subscribe requests to the list. Use the www
interface or send it to gmx-users-requ...@gromacs.org
mailto:gmx-users-requ...@gromacs.org.
Can't post? Read http://www.gromacs.org/Support/Mailing_Lists




--


Justin A. Lemkul
Ph.D. Candidate
ICTAS Doctoral Scholar
MILES-IGERT Trainee
Department of Biochemistry
Virginia Tech
Blacksburg, VA
jalemkul[at]vt.edu | (540) 231-9080
http://www.bevanlab.biochem.vt.edu/Pages/Personal/justin


--
gmx-users mailing listgmx-users@gromacs.org
http://lists.gromacs.org/mailman/listinfo/gmx-users
Please search the archive at 
http://www.gromacs.org/Support/Mailing_Lists/Search before posting!
Please don't post (un)subscribe requests to the list. Use the 
www interface or send it to gmx-users-requ...@gromacs.org.

Can't post? Read http://www.gromacs.org/Support/Mailing_Lists


Re: [gmx-users] Heat of vap

2011-03-31 Thread David van der Spoel

On 2011-03-31 18.52, Elisabeth wrote:



in your mail:

On 30 March 2011 15:30, Justin A. Lemkul jalem...@vt.edu
mailto:jalem...@vt.edu wrote:



Elisabeth wrote:

Dear all,

I intend to obtain vaporization heat per volume for a /pure
alkane system/.  Here is the steps I am taking. Please correct me.

1- Obtain total energy of system (kinetic+potential) and divide
by number of molecules to obtain energy per mol of molecules.
g_energy -f *.edr -nmol XXX
2- Obtain total energy of a single molecule (use pbc).
3- Subtract step 2 from step 1.
4- Divide by simulation box volume.

My questions is:

in step 2 : what should be the box size? The same size as in 1
or it does not matter? (step 1 is done for the actual denstiy)


More troubling, how does one define the energy of a molecule?  If
you use any sort of long-range algorithms (especially PME, but also
dispersion correction), you can't simply decompose the system like this.

Thanks Justin and David.

I have been trying to find the article in which this has been presented.
If you have time Please see page 5937, right column, equation 11. I
think I made a mistake and I dont have to include kinetic energy, Only
nonboded energies!?
Either Epot or Etot. It does not matter if you simulate at the same 
Temp. You could also consider using the enthalphy (gmx 4.5 and higher).


http://pubs.acs.org/doi/pdfplus/10.1021/jp0707539

In the derivation of recent Gromos96 parameter sets, the heat of
vaporization is quite simple:

DHvap = Ugas - Uliq + RT


1- So Uliq is the total energy or only potential (no kinetic)
2- How can I compute Ugas? I have liquid now...


Thank you,
Regards,


--


Justin A. Lemkul
Ph.D. Candidate
ICTAS Doctoral Scholar
MILES-IGERT Trainee
Department of Biochemistry
Virginia Tech
Blacksburg, VA
jalemkul[at]vt.edu http://vt.edu | (540) 231-9080
http://www.bevanlab.biochem.vt.edu/Pages/Personal/justin



--
gmx-users mailing list gmx-users@gromacs.org
mailto:gmx-users@gromacs.org
http://lists.gromacs.org/mailman/listinfo/gmx-users
Please search the archive at
http://www.gromacs.org/Support/Mailing_Lists/Search before posting!
Please don't post (un)subscribe requests to the list. Use the www
interface or send it to gmx-users-requ...@gromacs.org
mailto:gmx-users-requ...@gromacs.org.
Can't post? Read http://www.gromacs.org/Support/Mailing_Lists





--
David van der Spoel, Ph.D., Professor of Biology
Dept. of Cell  Molec. Biol., Uppsala University.
Box 596, 75124 Uppsala, Sweden. Phone:  +46184714205.
sp...@xray.bmc.uu.sehttp://folding.bmc.uu.se
--
gmx-users mailing listgmx-users@gromacs.org
http://lists.gromacs.org/mailman/listinfo/gmx-users
Please search the archive at 
http://www.gromacs.org/Support/Mailing_Lists/Search before posting!
Please don't post (un)subscribe requests to the list. Use the 
www interface or send it to gmx-users-requ...@gromacs.org.

Can't post? Read http://www.gromacs.org/Support/Mailing_Lists


Re: [gmx-users] Heat of vap

2011-03-31 Thread Elisabeth
On 31 March 2011 12:58, Justin A. Lemkul jalem...@vt.edu wrote:



 Elisabeth wrote:



 in your mail:


 On 30 March 2011 15:30, Justin A. Lemkul jalem...@vt.edu mailto:
 jalem...@vt.edu wrote:



Elisabeth wrote:

Dear all,

I intend to obtain vaporization heat per volume for a /pure
alkane system/.  Here is the steps I am taking. Please correct me.

1- Obtain total energy of system (kinetic+potential) and divide
by number of molecules to obtain energy per mol of molecules.
g_energy -f *.edr -nmol XXX
2- Obtain total energy of a single molecule (use pbc).
3- Subtract step 2 from step 1.
4- Divide by simulation box volume.

My questions is:

in step 2 : what should be the box size? The same size as in 1
or it does not matter? (step 1 is done for the actual denstiy)


More troubling, how does one define the energy of a molecule?  If
you use any sort of long-range algorithms (especially PME, but also
dispersion correction), you can't simply decompose the system like
 this.

 Thanks Justin and David.

 I have been trying to find the article in which this has been presented.
 If you have time Please see page 5937, right column, equation 11. I think I
 made a mistake and I dont have to include kinetic energy, Only nonboded
 energies!?

 http://pubs.acs.org/doi/pdfplus/10.1021/jp0707539


 What is cohesive energy and how does it relate to the quantity you're
 trying to calculate?

 It is delta Hvap/volume. It is directly related to Hvap. What is happening
 is that they are calculating nonbonded energy of some chains, divide by
 number of chains and substract from nonbonded energy of a single chain in
 vacuum. These are the steps I wrote in my first post but I think I should
 not have included kinetic and should just look at LJ-SR and Coulomb-SR.


I am using PME..If I remember correctly LR is included in Coulomb-SR and can
not get decomposed? But I dont think this doesnt matter since if I am to
take nonbonded energies this should not hurt,,,

Please comment ...




In the derivation of recent Gromos96 parameter sets, the heat of
vaporization is quite simple:

DHvap = Ugas - Uliq + RT


 1- So  Uliq is the total energy or only potential (no kinetic)


 Potential.


  2- How can I compute Ugas? I have liquid now...


 Run a simulation in the gas phase.


Sorry, but how can I do this? :( I have box of molecules with density of
actual liquid..How can I shift to gas phase ..I mean how many molecules I
need to keep in the box..

Many thanks...


 -Justin


Thank you,
Regards,


-- 

Justin A. Lemkul
Ph.D. Candidate
ICTAS Doctoral Scholar
MILES-IGERT Trainee
Department of Biochemistry
Virginia Tech
Blacksburg, VA
jalemkul[at]vt.edu http://vt.edu | (540) 231-9080

http://www.bevanlab.biochem.vt.edu/Pages/Personal/justin



-- gmx-users mailing listgmx-users@gromacs.org
mailto:gmx-users@gromacs.org

http://lists.gromacs.org/mailman/listinfo/gmx-users
Please search the archive at
http://www.gromacs.org/Support/Mailing_Lists/Search before posting!
Please don't post (un)subscribe requests to the list. Use the www
interface or send it to gmx-users-requ...@gromacs.org
mailto:gmx-users-requ...@gromacs.org.

Can't post? Read http://www.gromacs.org/Support/Mailing_Lists



 --
 

 Justin A. Lemkul
 Ph.D. Candidate
 ICTAS Doctoral Scholar
 MILES-IGERT Trainee
 Department of Biochemistry
 Virginia Tech
 Blacksburg, VA
 jalemkul[at]vt.edu | (540) 231-9080
 http://www.bevanlab.biochem.vt.edu/Pages/Personal/justin

 
 --
 gmx-users mailing listgmx-users@gromacs.org
 http://lists.gromacs.org/mailman/listinfo/gmx-users
 Please search the archive at
 http://www.gromacs.org/Support/Mailing_Lists/Search before posting!
 Please don't post (un)subscribe requests to the list. Use the www interface
 or send it to gmx-users-requ...@gromacs.org.
 Can't post? Read http://www.gromacs.org/Support/Mailing_Lists

-- 
gmx-users mailing listgmx-users@gromacs.org
http://lists.gromacs.org/mailman/listinfo/gmx-users
Please search the archive at 
http://www.gromacs.org/Support/Mailing_Lists/Search before posting!
Please don't post (un)subscribe requests to the list. Use the 
www interface or send it to gmx-users-requ...@gromacs.org.
Can't post? Read http://www.gromacs.org/Support/Mailing_Lists

Re: [gmx-users] Heat of vap

2011-03-31 Thread Justin A. Lemkul



Elisabeth wrote:



On 31 March 2011 12:58, Justin A. Lemkul jalem...@vt.edu 
mailto:jalem...@vt.edu wrote:




Elisabeth wrote:



in your mail:


On 30 March 2011 15:30, Justin A. Lemkul jalem...@vt.edu
mailto:jalem...@vt.edu mailto:jalem...@vt.edu
mailto:jalem...@vt.edu wrote:



   Elisabeth wrote:

   Dear all,

   I intend to obtain vaporization heat per volume for a /pure
   alkane system/.  Here is the steps I am taking. Please
correct me.

   1- Obtain total energy of system (kinetic+potential) and
divide
   by number of molecules to obtain energy per mol of molecules.
   g_energy -f *.edr -nmol XXX
   2- Obtain total energy of a single molecule (use pbc).
   3- Subtract step 2 from step 1.
   4- Divide by simulation box volume.

   My questions is:

   in step 2 : what should be the box size? The same size as
in 1
   or it does not matter? (step 1 is done for the actual
denstiy)


   More troubling, how does one define the energy of a molecule?  If
   you use any sort of long-range algorithms (especially PME,
but also
   dispersion correction), you can't simply decompose the system
like this.

Thanks Justin and David.

I have been trying to find the article in which this has been
presented. If you have time Please see page 5937, right column,
equation 11. I think I made a mistake and I dont have to include
kinetic energy, Only nonboded energies!?

http://pubs.acs.org/doi/pdfplus/10.1021/jp0707539


What is cohesive energy and how does it relate to the quantity
you're trying to calculate?

It is delta Hvap/volume. It is directly related to Hvap. What is
happening is that they are calculating nonbonded energy of some
chains, divide by number of chains and substract from nonbonded
energy of a single chain in vacuum. These are the steps I wrote in
my first post but I think I should not have included kinetic and
should just look at LJ-SR and Coulomb-SR.


I am using PME..If I remember correctly LR is included in Coulomb-SR and 
can not get decomposed? But I dont think this doesnt matter since if I 
am to take nonbonded energies this should not hurt,,,


Please comment ...



PME energies are from nonbonded interactions.  The mesh energy is written to the 
Coul-recip term in the .edr file.  If there is some other Coul (LR) term, it 
is because you're using a twin-range cutoff such that rcoulomb  rlist, which I 
do not believe is correct when using PME.


 

 
   In the derivation of recent Gromos96 parameter sets, the heat of

   vaporization is quite simple:

   DHvap = Ugas - Uliq + RT


1- So  Uliq is the total energy or only potential (no kinetic)


Potential.


2- How can I compute Ugas? I have liquid now...


Run a simulation in the gas phase.


Sorry, but how can I do this? :( I have box of molecules with density of 
actual liquid..How can I shift to gas phase ..I mean how many molecules 
I need to keep in the box..




Make a box with an equivalent number of molecules separated by some large amount 
of space (i.e. 50 nm or so).  Set pbc=no and all cutoffs to zero.  I'm basing 
this on Gromos96 parameterization, but I don't know what your target force field is.


-Justin


Many thanks...


-Justin


   Thank you,
   Regards,


   -- 

   Justin A. Lemkul
   Ph.D. Candidate
   ICTAS Doctoral Scholar
   MILES-IGERT Trainee
   Department of Biochemistry
   Virginia Tech
   Blacksburg, VA
   jalemkul[at]vt.edu http://vt.edu http://vt.edu | (540)
231-9080

   http://www.bevanlab.biochem.vt.edu/Pages/Personal/justin

   

   -- gmx-users mailing listgmx-users@gromacs.org
mailto:gmx-users@gromacs.org
   mailto:gmx-users@gromacs.org mailto:gmx-users@gromacs.org

   http://lists.gromacs.org/mailman/listinfo/gmx-users
   Please search the archive at
   http://www.gromacs.org/Support/Mailing_Lists/Search before
posting!
   Please don't post (un)subscribe requests to the list. Use the www
   interface or send it to gmx-users-requ...@gromacs.org
mailto:gmx-users-requ...@gromacs.org
   mailto:gmx-users-requ...@gromacs.org
mailto:gmx-users-requ...@gromacs.org.

   Can't post? Read http://www.gromacs.org/Support/Mailing_Lists



-- 



Justin A. Lemkul
Ph.D. Candidate
ICTAS Doctoral Scholar
MILES-IGERT Trainee
Department of Biochemistry
  

Re: [gmx-users] Heat of vap

2011-03-31 Thread David van der Spoel

On 2011-03-31 19.11, Elisabeth wrote:



On 31 March 2011 12:58, Justin A. Lemkul jalem...@vt.edu
mailto:jalem...@vt.edu wrote:



Elisabeth wrote:



in your mail:


On 30 March 2011 15:30, Justin A. Lemkul jalem...@vt.edu
mailto:jalem...@vt.edu mailto:jalem...@vt.edu
mailto:jalem...@vt.edu wrote:



Elisabeth wrote:

Dear all,

I intend to obtain vaporization heat per volume for a /pure
alkane system/.  Here is the steps I am taking. Please
correct me.

1- Obtain total energy of system (kinetic+potential) and
divide
by number of molecules to obtain energy per mol of
molecules.
g_energy -f *.edr -nmol XXX
2- Obtain total energy of a single molecule (use pbc).
3- Subtract step 2 from step 1.
4- Divide by simulation box volume.

My questions is:

in step 2 : what should be the box size? The same size
as in 1
or it does not matter? (step 1 is done for the actual
denstiy)


More troubling, how does one define the energy of a
molecule?  If
you use any sort of long-range algorithms (especially PME,
but also
dispersion correction), you can't simply decompose the
system like this.

Thanks Justin and David.

I have been trying to find the article in which this has been
presented. If you have time Please see page 5937, right column,
equation 11. I think I made a mistake and I dont have to include
kinetic energy, Only nonboded energies!?

http://pubs.acs.org/doi/pdfplus/10.1021/jp0707539


What is cohesive energy and how does it relate to the quantity
you're trying to calculate?

It is delta Hvap/volume. It is directly related to Hvap. What is
happening is that they are calculating nonbonded energy of some
chains, divide by number of chains and substract from nonbonded
energy of a single chain in vacuum. These are the steps I wrote in
my first post but I think I should not have included kinetic and
should just look at LJ-SR and Coulomb-SR.


I am using PME..If I remember correctly LR is included in Coulomb-SR and
can not get decomposed? But I dont think this doesnt matter since if I
am to take nonbonded energies this should not hurt,,,

Please comment ...

It is simple.
Compute Epot with all normal liquid options (PME, Dispcorr etc.).
Compute Epot for a gas phase molecule without any cutoffs
Apply equation below.
For OPLS/AA we obtain close to 98% correlation between experiment and 
simulation (paper submitted).



In the derivation of recent Gromos96 parameter sets, the heat of
vaporization is quite simple:

DHvap = Ugas - Uliq + RT


1- So Uliq is the total energy or only potential (no kinetic)


Potential.


2- How can I compute Ugas? I have liquid now...


Run a simulation in the gas phase.


Sorry, but how can I do this? :( I have box of molecules with density of
actual liquid..How can I shift to gas phase ..I mean how many molecules
I need to keep in the box..

Many thanks...


-Justin


Thank you,
Regards,


-- 

Justin A. Lemkul
Ph.D. Candidate
ICTAS Doctoral Scholar
MILES-IGERT Trainee
Department of Biochemistry
Virginia Tech
Blacksburg, VA
jalemkul[at]vt.edu http://vt.edu http://vt.edu | (540)
231-9080

http://www.bevanlab.biochem.vt.edu/Pages/Personal/justin



-- gmx-users mailing list gmx-users@gromacs.org
mailto:gmx-users@gromacs.org
mailto:gmx-users@gromacs.org mailto:gmx-users@gromacs.org

http://lists.gromacs.org/mailman/listinfo/gmx-users
Please search the archive at
http://www.gromacs.org/Support/Mailing_Lists/Search before posting!
Please don't post (un)subscribe requests to the list. Use
the www
interface or send it to gmx-users-requ...@gromacs.org
mailto:gmx-users-requ...@gromacs.org
mailto:gmx-users-requ...@gromacs.org
mailto:gmx-users-requ...@gromacs.org.

Can't post? Read http://www.gromacs.org/Support/Mailing_Lists



--


Justin A. Lemkul
Ph.D. Candidate
ICTAS Doctoral Scholar
MILES-IGERT Trainee
Department of Biochemistry
Virginia Tech
Blacksburg, VA
jalemkul[at]vt.edu http://vt.edu | (540) 231-9080
http://www.bevanlab.biochem.vt.edu/Pages/Personal/justin


--
gmx-users mailing list gmx-users@gromacs.org
  

Re: [gmx-users] Heat of vap

2011-03-30 Thread David van der Spoel

On 2011-03-30 21.22, Elisabeth wrote:

Dear all,

I intend to obtain vaporization heat per volume for a /pure alkane
system/.  Here is the steps I am taking. Please correct me.

1- Obtain total energy of system (kinetic+potential) and divide by
number of molecules to obtain energy per mol of molecules. g_energy -f
*.edr -nmol XXX
2- Obtain total energy of a single molecule (use pbc).
3- Subtract step 2 from step 1.
4- Divide by simulation box volume.

My questions is:

in step 2 : what should be the box size? The same size as in 1 or it
does not matter? (step 1 is done for the actual denstiy)

do turn off all pbc and cutoff for that one.


Thanking you all,
Regards,




--
David van der Spoel, Ph.D., Professor of Biology
Dept. of Cell  Molec. Biol., Uppsala University.
Box 596, 75124 Uppsala, Sweden. Phone:  +46184714205.
sp...@xray.bmc.uu.sehttp://folding.bmc.uu.se
--
gmx-users mailing listgmx-users@gromacs.org
http://lists.gromacs.org/mailman/listinfo/gmx-users
Please search the archive at 
http://www.gromacs.org/Support/Mailing_Lists/Search before posting!
Please don't post (un)subscribe requests to the list. Use the 
www interface or send it to gmx-users-requ...@gromacs.org.

Can't post? Read http://www.gromacs.org/Support/Mailing_Lists


Re: [gmx-users] Heat of vap

2011-03-30 Thread Justin A. Lemkul



Elisabeth wrote:

Dear all,

I intend to obtain vaporization heat per volume for a /pure alkane 
system/.  Here is the steps I am taking. Please correct me.


1- Obtain total energy of system (kinetic+potential) and divide by 
number of molecules to obtain energy per mol of molecules. g_energy -f 
*.edr -nmol XXX

2- Obtain total energy of a single molecule (use pbc).
3- Subtract step 2 from step 1.
4- Divide by simulation box volume.

My questions is:

in step 2 : what should be the box size? The same size as in 1 or it 
does not matter? (step 1 is done for the actual denstiy)




More troubling, how does one define the energy of a molecule?  If you use any 
sort of long-range algorithms (especially PME, but also dispersion correction), 
you can't simply decompose the system like this.


In the derivation of recent Gromos96 parameter sets, the heat of vaporization is 
quite simple:


DHvap = Ugas - Uliq + RT

I have seen this equation used in a number of other studies, as well.

-Justin


Thanking you all,
Regards,



--


Justin A. Lemkul
Ph.D. Candidate
ICTAS Doctoral Scholar
MILES-IGERT Trainee
Department of Biochemistry
Virginia Tech
Blacksburg, VA
jalemkul[at]vt.edu | (540) 231-9080
http://www.bevanlab.biochem.vt.edu/Pages/Personal/justin


--
gmx-users mailing listgmx-users@gromacs.org
http://lists.gromacs.org/mailman/listinfo/gmx-users
Please search the archive at 
http://www.gromacs.org/Support/Mailing_Lists/Search before posting!
Please don't post (un)subscribe requests to the list. Use the 
www interface or send it to gmx-users-requ...@gromacs.org.

Can't post? Read http://www.gromacs.org/Support/Mailing_Lists