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Published byMuriel Bradford Modified over 6 years ago
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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 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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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
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Search for Compounds in NIST
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Specifying the Type of Data to be Displayed
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Basic Information Concerning the Compound
2-D and 3-D structure representation
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Solid Properties and Phase Change Data
Temp. dependent property given in an equation Note that several values may be available for the same property
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Basic Information Concerning a Different Compound
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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.
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Constant Properties from DIPPR
Change Units
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DIPPR – Definition of the Properties
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DIPPR – Additional Information Regarding the Data
Data Type Source Type Reliability None: Data have been predicted by project staff but no reliability was assigned
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DIPPR – Additional Information Regarding Data
DIPPR attempts to provide full sets of data for all the compounds included by predicting properties whenever possible
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DIPPR – Selection of the “Accepted” Property Value
Rejected Acceptable
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DIPPR – Coefficients for Temperature Dependent Property Correlations
Range of validity Original Data Equation No. + Property Calculator
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DIPPR – Calculator for Temperature Dependent Property (Viscosity)
Property name and units Validity Range
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DIPPR – Equations Used for Various Properties
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DIPPR – Equations Used for Various Properties
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DIPPR – Original Data for Temperature Dependent Properties
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DIPPR – Changing Display Units of Properties
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DDBSP – Selecting the Compounds to be Included
Click to add the compound
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DDBSP – Pure Compound Properties
Click for details For calculation of activity coeffs.
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DDBSP – Detailed Pure Compound Properties
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DDBSP – Prediction of Properties
Draw the 2-D structure
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DDBSP – Prediction of Properties
Continue Tools for drawing the 2-D structure
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DDBSP – Prediction of Properties
Prediction of critical properties by the Gani/Constantinous method
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DDBSP – Mixture Property Prediction
Equilibrium type Prediction Methods Display
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DDBSP – Molecular Structure Editor - Cyclohexylamine
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DDBSP – Prediction of Properties by Group Contribution Methods
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DDBSP – Phase Equilibrium Results
Ideal Toluene Azeotrope
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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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