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Process Design Course 2016-17 Using the NIST, DIPPR and DDBSP databases for Finding Physical, Chemical and Thermodynamic Properties Process Design Course.

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Presentation on theme: "Process Design Course 2016-17 Using the NIST, DIPPR and DDBSP databases for Finding Physical, Chemical and Thermodynamic Properties Process Design Course."— Presentation transcript:

1 Process Design Course 2016-17
Using the NIST, DIPPR and DDBSP databases for Finding Physical, Chemical and Thermodynamic Properties Process Design Course by Mordechai Shacham NIST – Open Access DIPPR – Limited Access user: byudippr password: di2003ppr DDBSP – Installed in Room 238 Building 59 NIST – Open Access DIPPR – Limited Access user: byudippr password: di2003ppr DDBSP – Installed in Room 238 Building 59 NIST – Open Access DIPPR – Limited Access user: byudippr password: di2003ppr DDBSP – Installed in Room 238 Building 59

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3 Properties of gases and liquid are measured, calculated from basic models or estimated from correlations Pure component constants: critical constants, boiling and freezing points, acentric factor Thermodynamic properties of ideal gases: enthalpy and Gibbs energy of formation and heat capacity PVT relationships: temperature, pressure, volume Thermodynamic properties: heat capacity, fugacity and departure functions Vapor pressure and enthalpy of vaporization Fluid phase equilibria Transport properties: viscosity, thermal conductivity and diffusivity

4 Search for Compounds in NIST

5 Specifying the Type of Data to be Displayed

6 Basic Information Concerning the Compound
2-D and 3-D structure representation

7 Solid Properties and Phase Change Data
Temp. dependent property given in an equation Note that several values may be available for the same property

8 Basic Information Concerning a Different Compound

9 Solid Properties and Phase Change Data for Styrene
Vapor pressure represented by Antoine equation. Note difference in the parameters. NIST very reliable source. Relies only on experimental data.

10 Constant Properties from DIPPR
Change Units

11 DIPPR – Definition of the Properties

12 DIPPR – Additional Information Regarding the Data
Data Type Source Type Reliability None: Data have been predicted by project staff but no reliability was assigned

13 DIPPR – Additional Information Regarding Data
DIPPR attempts to provide full sets of data for all the compounds included by predicting properties whenever possible

14 DIPPR – Selection of the “Accepted” Property Value
Rejected Acceptable

15 DIPPR – Coefficients for Temperature Dependent Property Correlations
Range of validity Original Data Equation No. + Property Calculator

16 DIPPR – Calculator for Temperature Dependent Property (Viscosity)
Property name and units Validity Range

17 DIPPR – Equations Used for Various Properties

18 DIPPR – Equations Used for Various Properties

19 DIPPR – Original Data for Temperature Dependent Properties

20 DIPPR – Changing Display Units of Properties

21 DDBSP – Selecting the Compounds to be Included
Click to add the compound

22 DDBSP – Pure Compound Properties
Click for details For calculation of activity coeffs.

23 DDBSP – Detailed Pure Compound Properties

24 DDBSP – Prediction of Properties
Draw the 2-D structure

25 DDBSP – Prediction of Properties
Continue Tools for drawing the 2-D structure

26 DDBSP – Prediction of Properties
Prediction of critical properties by the Gani/Constantinous method

27 DDBSP – Mixture Property Prediction
Equilibrium type Prediction Methods Display

28 DDBSP – Molecular Structure Editor - Cyclohexylamine

29 DDBSP – Prediction of Properties by Group Contribution Methods

30 DDBSP – Phase Equilibrium Results
Ideal Toluene Azeotrope

31 The main source for correlations to estimate properties (including analysis based on experimental data), prediction methods for mixture properties Poling, B.E., Prausnitz, J.M. and O’Connell, J.P., “The Properties of Gases and Liquids”, McGraw-Hill, Fifth Ed. 2001


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