22
10/24/2007 Thermodynamic Simulations for Thermodynamic Simulations for Phosphorus-Containing Systems Using Phosphorus-Containing Systems Using OLI Software Together with a First- OLI Software Together with a First- Principle Calculation Principle Calculation Katsuhiko TSUNASHIMA, Yasuo YAMAZAKI Nippon Chemical Industrial Co., Ltd. (NC I) JAPAN www.nippon-chem.com e-mail: [email protected] katsuhiko.tsunashima@nippon-che m.co.jp Oct. 24, 2007 OLI Simulation Conference

10/24/2007 Thermodynamic Simulations for Phosphorus- Containing Systems Using OLI Software Together with a First-Principle Calculation Katsuhiko TSUNASHIMA,

Embed Size (px)

Citation preview

10/24/2007

Thermodynamic Simulations for Phosphorus-Thermodynamic Simulations for Phosphorus-Containing Systems Using OLI Software Together Containing Systems Using OLI Software Together

with a First-Principle Calculationwith a First-Principle Calculation

Katsuhiko TSUNASHIMA, Yasuo YAMAZAKI

Nippon Chemical Industrial Co., Ltd. (NCI)

JAPAN

www.nippon-chem.com

e-mail: [email protected]

[email protected]

Oct. 24, 2007

OLI Simulation Conference

10/24/2007

Outline of the talk

1) Introductory remarks on OLI simulations in NCI

2) Thermodynamic model based on MSE model together with a first-principle calculation

Phosphorus-containing species

COSMOTherm

Evaluation of calculation accuracy

3) Applications in NCI

An example of calculation using the new model

4) Summary and future work

10/24/2007

Nippon Chemical Industrial Co., Ltd. (NCI)

--- A manufacturer of phosphorus compounds ---

Head OfficeR&D Center

NishiyodogawaFukushima No.1Fukushima No.2AichiTokuyama

The products include:

• Red phosphorus• Phosphorus chlorides• Orthophosphoric acid• Orthophosphates• Hypophosphites• Phosphine• Alkylphosphines• Phosphonium salts• etc.

10/24/2007

NCI phosphorus compounds (Inorganic)

Elementaryphosphorus

P2O5

Phosphoruspentoxide

PCl3Phosphorustrichloride

PCl5Phosphorus

pentachloride

POCl3Phosphorusoxychloride

MPH2O2

Phosphinates M2PHO3

Phosphonates

M3PO4

Ortho-phosphates

M4P2O7   PyrophosphatesM5P3O10   Tripolyphosphates(MPO3)n   Metaphosphates

Ca5(OH)(PO4)3   Hydroxyapatite

PH3

Phosphine

M = H, Ba, Na, K, Li, NH4, Ca, Mg, Zn, Ni, Cu, Fe

(O)

Cl2

Cl2

O2

H2O

(O)

(O)

No solvents

- H2O

No solvents*

No solvents*

No solvents*

(P2O5

)

KOH

Organophosphorus compounds

10/24/2007

NCI phosphorus compounds (Organic)

www.nippon-chem.com/organic.htm

P+

R1

R2

R3

R4PH3Haloalkanes

P

Phosphine

1-Olefines

Radicaladdition

Trialkylphosphines

Nucleophilic addition

R3

R1

R2

Quaternary phosphoniumsalts

X-

P C4H9

C4H9

C4H9

Tributylphosphine

P C8H17

C8H17

C8H17

Trioctylphosphine

P+

C4H9

C4H9

C4H9

C4H9 Cl-

Tetrabutylphosphoniumchloride

P+

C4H9

C4H9

C4H9

C4H9 Br-

Tetrabutylphosphoniumbromide

10/24/2007

Nippon Chemical Industrial Co., Ltd. (NCI)--- An active user of OLI software ---

NCI has been an active user of OLI software (OLI Systems) and calcAQ (created and developed by Dr. Turner, Turner Technology). Both software packages have been installed into ALL client PCs in NCI.

www.olisystems.com www.turnertechnology.com

10/24/2007

P-Project

More than 90 “inorganic” phosphorus species were surveyedand registered into the private databank.

The species include: elementary phosphorus (white P, red P) phosphine (PH3), phosphinates (PH2O2

-), phosphonates (PHO32-),

orthophosphates (PO43-),

pyrophosphates (P2O74-), tripolyphosphates (P3O10

5-), phosphorus pentoxide (P2O5), phosphorus chlorides (PCl3, PCl5, POCl3).

The construction of a private databank for simulations of phosphorus-containing systems using OLI software

10/24/2007

0.81

1.21.41.61.8

22.22.42.62.8

0 25 50 75 100

Concentration of H3PO4 / wt%

De

nsi

ty /

g c

m-3

Calculated data

Literature Data

P-Project: An application

The Excel interface was kindly created by

Dr. H. Turner, Turner Technology, LLC.

Prediction of concentration from measured density in aqueous H3PO4 systems

Fig. Comparison between literature and

calculated data for concentration vs. density

of orthophosphoric acid at 25 oC.

Fig. An Excel interface actually used in a

plant in NCI.

10/24/2007

Thermodynamic data of organic phosphorus species

Organic phosphorus compounds are not always common, compared to inorganic phosphorus compounds. Therefore, no or little literature data for organic phosphorus species are available.

Some organic phosphorus compounds, such as organic phosphines, are unstable (highly oxidized) in air, which makes it difficult to carry out experimental studies to measure their thermodynamic data.

P C4H9

C4H9

C4H9

Tributylphosphine

P C8H17

C8H17

C8H17

Trioctylphosphine

P+

C4H9

C4H9

C4H9

C4H9 Cl-

Tetrabutylphosphoniumchloride

P+

C4H9

C4H9

C4H9

C4H9 Br-

Tetrabutylphosphoniumbromide

However, thermodynamic data of organic phosphorus species were not able to be included into P-project databank, because:

10/24/2007

When no experimental data are available, how do we calculate ?

OLI software with the data is expected to enable the thermodynamic calculation, even in the case of

no experimental data

Thermodynamic data for phosphorus species

First-principle calculation based on quantum mechanics for obtaining the data of phosphorus species

“OLI software”, “calcAQ”

“COSMOTherm” (COSMOLogic)

10/24/2007

Approach

• OLI Systems’ Mixed-Solvent Electrolyte (MSE) model Reproducing available experimental data Excess Gibbs energy model for solution nonideality Calculating phase equilibria in liquid-solid-vapor systems an

d chemical equilibria (acid-base, complexation, redox)

• COSMOLogic’s COSMOTherm software First-principle quantum mechanics of isolated molecules yie

lds charge densities. Using dielectric continuum solvation techniques, local intera

ctions between molecules yield the chemical potential. Predicting liquid-phase nonideality when no experimental d

ata are available. Solid-liquid transitions cannot be directly calculated unless

properties of the solid phase are known from experimental sources

10/24/2007

Thermodynamics of orthophosphoric acid(MSE)

• The model accurately reproduces solid-liquid equilibria in the phosphoric acid system up to the fused salt limit.

• In this case, there is no need to estimate properties using COSMOTherm.

0

10

20

30

40

50

60

70

80

90

100

-90 -80 -70 -60 -50 -40 -30 -20 -10 0 10 20 30 40 50

Temperature, C

H3P

O4,

wei

ght

%

H2O(s)

H3PO4.0.5H2O

H3PO4(s)

(s)

SLE

This data was kindly provided by Dr. A. Anderko, OLI Systems.

10/24/2007

Hierarchy of parameter determination

If sufficient experimental data are available, only experimental data are used.

If experimental data for VLE and/or LLE are fragmentary, the MSE model is constrained to match the available data and COSMOTherm predictions are used to fill the gaps in the data.

If experimental data are limited to solid solubility and no VLE or LLE data are available, COSMOTherm predictions are used to constrain the activity coefficients. Then, the available solubility data are used to calculate the thermochemical properties of the solid phase as described above.

If no solubility data or thermochemical properties of solid phases are available, the MSE model is unable to predict SLE. Then, MSE can predict only VLE and/or LLE using parameters obtained from either experimental data or COSMOTherm predictions.

10/24/2007

Triphenylphosphate (TPP) + water

• In order to evaluate the accuracy of the calc

ulation, triphenylphosphate is used, because a few literature data are available, although this compound is not phosphine compound.

• The experimental data are limited to the melting point and room-temperature solubility

• The LLE predictions from COSMOTherm are consistent with the fragmental experimental data

• COSMOTherm fills the gaps in experimental coverage; MSE enables SLE predictions

0

50

100

150

200

250

300

1E-05 1E-04 0.001 0.01 0.1 1 10 100

%w TPP

t/C

Saeger, Hicks et al. 1979

Merck

NIST

COSMOtherm

COSMOtherm 2nd phase

MSE LLE

MSE LLE 2nd phase

MSE SLE

0

50

100

150

200

250

300

0.001 0.01 0.1 1 10 100

%w H2O

t/C

Saeger, Hicks et al. 1979

Merck

NIST

COSMOtherm

COSMOtherm 2nd phase

MSE LLE

MSE LLE 2nd phase

MSE SLE

LLE

LLE

SLE

SLEThis data was kindly provided by Dr. A. Anderko,

OLI Systems.

10/24/2007

Summary

• A comprehensive model has been established for calculating the thermodynamic properties of aqueous systems containing phosphorus compounds.

• The framework is based on the OLI MSE model.

• The model parameters are determined from a combination of experimental data and predictions from COSMOTherm, a computational chemistry software.

• The model has been implemented in process simulation software.

10/24/2007

In our plants, OLI software equipped with the databank containing the data of P-species are actually available for the:

• Reaction processes• Mixing processes• Crystallization processes• Distillation processes• Waste water treatments• etc.

Industrial applications

Fukushima plant, NCI

10/24/2007

Private databank containing P-speciesbased on MSE model

Added organic phosphorus speciesinclude:

tributylphosphate (BuO)3P=O

triphenylphosphate (PhO)3P=O

tributylphosphine Bu3P

trioctylphosphine Oc3P

triphenylphosphine Ph3P

tetrabutylphosphonium chloride

Bu4P-Cl

tetrabutylphosphonium bromide

Bu4P-Br

tributylmethylphosphonium iodide

Bu3MeP-I

10/24/2007

An example: PH3 + Bu3P in water

• It is very important for us to be able to calculate this system from the viewpoint of process control.

10/24/2007

Low pressure conditions

Bu3P, 2nd liq.

Bu3P, Vap.

Ambientpressure

• A vapor-liquid equilibria of Bu3P was calculated.

• The calculation under low pressures is important for controlling

the evaporation and distillation processes of Bu3P.

10/24/2007

High pressure conditions

Ambientpressure

PH3, 2nd liq.

PH3, Aq.

PH3, Vap.

• A vapor-liquid equilibria of PH3 was calculated. The contents of PH3 in aqueous and 2nd liquid phases are increased with increasing the pressure.

• Bu3P is often produced from PH3 under high pressure conditions, so that this calculation is very important for controlling the production process.

10/24/2007

The future target

Organic phase(hexane, toluene, etc.)

Aqueous phase

Ionic liquid phase

The tri-phasic system containing an “ionic liquid” phaseas the third liquid phase

“Ionic liquids” are organic molten salts with low melting point:

P+

R1

R2

R3

R4N+

R1

R2

R3

R4N+NR1 R2

N+

R

BF4-, PF6

-, -SO3CF3,

-N(SO2CF3)2etc.

10/24/2007

Acknowledgements

We would like to acknowledge and thank:

Dr. Andrzej Anderko, OLI Systems, Inc.

Dr. Malgorzata M. Lencka, OLI Systems, Inc.

Mr. Jerzy J. Kosinski, OLI Systems, Inc.

Mr. Ronald D. Springer, OLI Systems, Inc.

Dr. Andreas Klamt, COSMOlogic GmbH & Co. KG

Dr. Hamp Turner, Turner Technology, LLC.

Thank you for your kind attention.