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1 By Ertanto Vetra EVALUATING PROPERTIES FOR A PURE SUBSTANCES
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Page 1: EVALUATING PROPERTIES FOR A PURE …tmg3201.weebly.com/.../11832443/03-evaluating_properties.pdfEVALUATING PROPERTIES FOR A PURE SUBSTANCES Outlines - TV, PV, PT, PVT Diagram - Property

1 By Ertanto Vetra

EVALUATING PROPERTIES FOR A PURE SUBSTANCES

Page 2: EVALUATING PROPERTIES FOR A PURE …tmg3201.weebly.com/.../11832443/03-evaluating_properties.pdfEVALUATING PROPERTIES FOR A PURE SUBSTANCES Outlines - TV, PV, PT, PVT Diagram - Property

Outlines

- TV, PV, PT, PVT Diagram - Property Tables - Introduction to Enthalpy - Reference State & Reference Values - Ideal Gas Equation of State - Compressibility Factor - Other Equation of State

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Phase, Pure Substances

• PHASE refers to a quantity of matter that is homogeneous throughout in both chemical composition and physical structure

• PURE SUBSTANCE is one that is uniform and invariable in chemical composition

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Pure Substances

• A pure substance does not have to be of a single chemical element or compound

• A mixture of various chemical elements or compounds also qualifies as a pure substance as long as the mixture is homogeneous, example : Air

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Pure Substance on Different Phases

• A mixture of two or more phases of a pure substance is still a pure substance as long as the chemical composition of all phases is the same. For example: – A mixture of ice and liquid water, is a pure substance – A mixture of liquid air and gaseous air, however, is not

a pure substance

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Sub-cooled, Saturated, Superheated

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PVT diagram

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T-V Diagram

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P-V diagram

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Superheated vs Saturated vs. Subcooled

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Property Tables, Evaluating P, V, T Vapor & Liquid Tables

• Moran, Table A-4 Superheated Water Vapor

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Property Tables, Evaluating P, V, T Vapor & Liquid Tables

• Moran, Table A-5 Sub-cooled Liquid Water

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Exercise

• Find the following: – Saturation Temperature of Water at 10 MPa – Specific Volume of Water Vap. at 10 MPa, 600 °C – Specific Volume of Liq. Water at 10 MPa, 100 °C – Specific Volume of Water Vap. at 10 Bar, 215 °C

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Linear Interpolation

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Enthalpy

• Energy Balance : U = Q + W • At constant Pressure :

U = Q – PdV Q = U + PdV • At constant Volume :

U = Q - PdV Q = U • For convenience, we define a new variable: Enthalpy (H) = U + PV (in Energy Unit) Per unit mass: h = u + Pv easier to tabulate

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Property Tables, Evaluating P, V, T Saturation Tables

• Moran, Table A-2 Temperature Table

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Property Tables, Evaluating P, V, T Saturation Tables

• Moran, Table A-3 Pressure Table

18 Table A.3-A.5 is also known as Steam Tables

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Example

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Mixture of Vapor & Liquid

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Quality / Vapor Fraction:

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Example

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Reference state & reference values

• u , h , and s ≠ direct measurement • u , h , and s = calculated from experiment • When applying the energy balance, it is

differences in internal, kinetic, and potential energy between two states that are important, and not the values of these energy quantities at each of the two states.

• Remember to check what is the reference state & reference values used by the data tables

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Energy Balance using Property Tables

• Water contained in a piston–cylinder assembly undergoes two processes in series from an initial state where the pressure is 10 bar and the temperature is 400°C. – Process 1–2 : The water is cooled as it is compressed at a

constant pressure of 10 bar to the saturated vapor state. – Process 2–3: The water is cooled at constant volume to

150°C. a) Sketch both processes on T–v and p–v diagrams. b) For the overall process determine the work, in kJ/kg. c) For the overall process determine the heat transfer, in

kJ/kg.

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Specific Heat (Cv & Cp)

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Constant Volume

Constant Pressure

Units: kJ/kg K or kJ/kmol K

Specific Heat Ratio (dimensionless)

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Incompressible Substance Model

• Incompressible : applicable for liquids, solids

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differentiating Eq. above with respect to temperature while holding pressure fixed obtains:

Negligible

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Ideal Gas Model

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Ideal Gas Equation of State (EOS)

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Compressibility Factor

• A measure of deviation from Ideal Gas behavior

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General Compressibility data, Z-chart

28 In this lecture, only single component is considered. Multi-component Z-value will not be covered

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Other Equation of State

29 And still many more….

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∆U, ∆H, Cp, Cv Relations

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For ideal gas:

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Using Specific Heat Function

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In some cases, constant Cp or Cv may be assumed

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Energy Balance using Ideal Gas Tables

• Table for Ideal Gas can be found in Table A.22 and A.23

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Note that this table is different from Table A.2-A-18, since this table is only applicable for Ideal Gas

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Exercise

• A rigid tank contains 50 kg of saturated liquid water at 90°C. Determine the pressure in the tank and the volume of the tank.

• A piston–cylinder device contains 2 ft3 of saturated water vapor at 50-psia pressure. Determine the temperature and the mass of the vapor inside the cylinder

• A mass of 200 g of saturated liquid water is completely vaporized at a constant pressure of 100 kPa. Determine; a. the volume change b. the amount of energy transferred to the water

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Exercise

• determine the specific enthalpy of Refrigerant-22 when its temperature is 12°C and its specific internal energy is 144.58 kJ/kg.

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Homework #4 due on Tuesday, March 13th

• Create a summary of Key Learning Points from Chapter 1-3, in one page of Plain Duplex A4, It can contain: – Equations – Important Conversion Factors – Theory, Concepts, Definition – Sketches/Diagram – Problem example with solution – Other important Key Learning Points

• Must be Hand written, using non-black pen (Blue/Red/etc) • Fit as many information as possible, small writing is encouraged (as

long as you can read it), utilize every space available • This summary will be a part of your notes for Mid-Exam (you’ll be

allowed to bring 2 pages of this summary)

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