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Physical & Chemical properties

Vapour pressure

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Reference
Endpoint:
vapour pressure
Type of information:
calculation (if not (Q)SAR)
Remarks:
Migrated phrase: estimated by calculation
Adequacy of study:
key study
Study period:
17 Oct 2011
Reliability:
2 (reliable with restrictions)
Rationale for reliability incl. deficiencies:
other: Acceptable, well-documented study report which meets basic scientific principles.
Principles of method if other than guideline:
Calculated limit value according to column 2 in Annex VII of Regulation (EC) No 1907/2006 (melting point - here: decomposition temperature -between 200°C and 300°C, see section 4.2).
Type of method:
other: estimate
Temp.:
25 °C
Vapour pressure:
< 0 Pa

Vapour pressure estimation of component 1

Software output:

------------------------ SUMMARY MPBPWIN v1.43 --------------------

Boiling Point: 745.09 deg C (Adapted Stein and Brown Method)

Melting Point: 349.84 deg C (Adapted Joback Method)

Melting Point: 321.39 deg C (Gold and Ogle Method)

Mean Melt Pt : 335.62 deg C (Joback; Gold,Ogle Methods)

Selected MP: 327.08 deg C (Weighted Value)

Vapor Pressure Estimations (25 deg C):

(Using BP: 745.09 deg C (estimated))

(Using MP: 327.08 deg C (estimated))

VP: 1.35E-029 mm Hg (Antoine Method)

     : 1.79E-027 Pa (Antoine Method)

VP: 1.45E-019 mm Hg (Modified Grain Method)

     : 1.93E-017 Pa (Modified Grain Method)

VP: 2.1E-017 mm Hg (Mackay Method)

     : 2.8E-015 Pa (Mackay Method)

Selected VP: 1.45E-019 mm Hg (Modified Grain Method)

            : 1.93E-017 Pa (Modified Grain Method)

Subcooled liquid VP: 3.77E-016 mm Hg (25 deg C, Mod-Grain method)

                    : 5.02E-014 Pa (25 deg C, Mod-Grain method)

Interpretation: On the basis of the vapour pressure of 1.93 x 10-17Pa selected in the software output, a limit value of <0.000001 Pa is chosen.

Vapour pressure estimation of component 2

Software output:

------------------------ SUMMARY MPBPWIN v1.43 --------------------

Boiling Point: 733.48 deg C (Adapted Stein and Brown Method)

Melting Point: 349.84 deg C (Adapted Joback Method)

Melting Point: 314.62 deg C (Gold and Ogle Method)

Mean Melt Pt : 332.23 deg C (Joback; Gold,Ogle Methods)

Selected MP: 321.66 deg C (Weighted Value)

Vapor Pressure Estimations (25 deg C):

(Using BP: 733.48 deg C (estimated))

(Using MP: 321.66 deg C (estimated))

VP: 1.47E-028 mm Hg (Antoine Method)

            : 1.97E-026 Pa (Antoine Method)

VP: 3.72E-019 mm Hg (Modified Grain Method)

           : 4.96E-017 Pa (Modified Grain Method)

VP: 4.91E-017 mm Hg (Mackay Method)

            : 6.55E-015 Pa (Mackay Method)

Selected VP: 3.72E-019 mm Hg (Modified Grain Method)

            : 4.96E-017 Pa (Modified Grain Method)

Subcooled liquid VP: 8.25E-016 mm Hg (25 deg C, Mod-Grain method)

                    : 1.1E-013 Pa (25 deg C, Mod-Grain method)

Interpretation: On the basis of the vapour pressure of 4.96 x 10-17Pa selected in the software output, a limit value of <0.000001 Pa is chosen.

 

Vapour pressure estimation of the submission substance

As the calculated vapour pressure of its components is far below the chosen limit value of 0.000001 Pa, the vapour pressure of the submission substance is also estimated to be far below 0.000001 Pa.

Conclusions:
The vapour pressure of the submission substance is estimated to be far below 0.000001 Pa.
Executive summary:

The vapour pressure of the submission substance was estimated by calculation in accordance with column 2 in Annex VII of Regulation (EC) No 1907/2006 by a calculation method recommended by the Guidance on Information Requirements and Chemical Safety Assessment (chapter R.7.1.5.3), MPBPVP of the EPI Suite (TM) software by the US Environmental Protection Agency (EPA, 2011).

The submission substance is an about half-and-half mixture of two components. Calculation of the vapour pressure of a mixture is not applicable in MPBPVP, therefore vapour pressure values for the components were estimated by calculation.

The calculated vapour pressureof the components at 25°C is far below the chosen limit value of 0.000001 Pa, therefore the vapour pressure of the submission substance is also estimated to be far below 0.000001 Pa.

Description of key information

The vapour pressure of the submission substance was estimated by calculation in accordance with column 2 in Annex VII of Regulation (EC) No 1907/2006 by a calculation method recommended by the Guidance on Information Requirements and Chemical Safety Assessment (chapter R.7.1.5.3), MPBPVP of the EPI Suite (TM) software by the US Environmental Protection Agency (EPA, 2011).


The submission substance is an about half-and-half mixture of two components. Calculation of the vapour pressure of a mixture is not applicable in MPBPVP, therefore vapour pressure values for the components were estimated by calculation.


The calculated vapour pressureof the components at 25°C is far below the chosen limit value of 0.000001 Pa, therefore the vapour pressure of the submission substance is also estimated to be far below 0.000001 Pa.

Key value for chemical safety assessment

Vapour pressure:
0 Pa
at the temperature of:
25 °C

Additional information