Vector or Cross Product r The area A due to a vector product
b. Vector or Cross Product r The area A due to a vector product
A =× xy , (82) can be written in the form
A = | || | sinθ kxy , (83) r
rr where k denotes the unit vector in a plane normal to that containing the vectors x and y , and
θ the angle between these two vectors. The vector product yields an area vector in a direction normal to the plane containing the two vectors.
Consider the circular motion of an object around an origin in a plane. The force due to that object in the plane r r
F = iF x + jF y = iF cos θ + jF sin θ , (84) where r θ denotes the angle between the force and an arbitrary x–wise coordinate at any instant, r
and i and j denote unit vectors in the x– and y– directions, respectively. The torque exerted about the center
B =×= F r ( iF cos θ + jF sin ) ( θ × ix + jy ) = kyF ( cos θ + xF sin ) θ , (85) r r
where i × i = 0, i ×= j k , and j ×= i − k . When a screw is loosened from a flat surface by rotating it in the counter clockwise direction, it emerges outward normal to the surface, say, in the z–direction. To place the screw back into the surface, it must be rotated in the clockwise direction, i.e., it may be visualized as moving towards the origin of the z–direction. The rotation is caused by an applied torque that is a vector. If the term (F cos θ y – Fsinθ x) = 0 in Eq.(87), then there is no rotation around the
z–axis. In general, a force has three spatial components, i.e., r r
F = iF x + jF y + kF z , (86) and the torque is described by the relation
B =×= F r iFzFy ( y + z ) + jFxFz ( z + x ) + kFyFx ( x + y ) , i.e.,
(87) r
r there are rotational components in the x– and y– directions also. If r r r F and r are parallel to
r each other, e.g., F = iF x and r = ix , then r r r
B =×=0 F r .
c. Gradient of a Scalar Consider a one–dimensional heat transfer problem in which the temperature T is only
a function of one spatial coordinate, say, y, i.e., T = T(y). In this case T(y) is a point or scalar function of y, since its value is fixed once y is specified. In general, the gradient of T is defined as a function of one spatial coordinate, say, y, i.e., T = T(y). In this case T(y) is a point or scalar function of y, since its value is fixed once y is specified. In general, the gradient of T is defined as
∇ T = ( i ∂∂ / x + j ∂∂ / yk + ∂∂ / zT ) , (88) which for the one–dimensional problem assumes the form
rr ∇= T jT ∂ / ∂ y ,
The x–z plane contains isotherms, since T ≠T(x,z), and ∇ T is a vector along normal to the isotherms in the y–direction.
Consider, now, the temperature profile in an infinite cylindrical rod. Assume that the temperature is constant along the axial direction z, once a cross–sectional location (x,y) is specified, i.e., T=T(x,y), and T ≠T(z). Assume an axisymmetric problem for which the iso-
therms are circular in the x–y plane and form cylindrical surfaces. In this case, r ∇
(90) r
dT = ( r ∂T/∂x)dx + (∂T/∂y)dy = ∇ T·
ds ,
rr where , ∇ T = iT ∂ / ∂ x + jT ∂ / ∂ y . Therefore, r
(91) the gradient dT/ds varies, depending upon the direction of the gradient between any two iso- r
dT/ds = r ∇ T·
ds /ds, i.e.,
r therms. Along any circular isotherm r ∇ T· ds = 0 according to Eq. (93), since ∇ T and ds are
normal to each other. In general, if T=T(x,y,z) then isotherms form surfaces that lie in all three (x,y,z) coor- r dinates, and, at any location, ∇ T represents a vector that lies normal to a scalar surface on which T is constant.
Parts
» COMPUTATIONAL MECHANICS and APPLIED ANALYSIS
» Explicit and Implicit Functions and Total Differentiation
» Exact (Perfect) and Inexact (Imperfect) Differentials
» Intermolecular Forces and Potential Energy
» Internal Energy, Temperature, Collision Number and Mean Free Path
» Vector or Cross Product r The area A due to a vector product
» First Law for a Closed System
» First Law For an Open System
» STATEMENTS OF THE SECOND LAW
» Cyclical Integral for a Reversible Heat Engine
» Irreversibility and Entropy of an Isolated System
» Degradation and Quality of Energy
» SINGLE–COMPONENT INCOMPRESSIBLE FLUIDS
» Evaluation of Entropy for a Control Volume
» Internally Reversible Work for an Open System
» MAXIMUM ENTROPY AND MINIMUM ENERGY
» Generalized Derivation for a Single Phase
» LaGrange Multiplier Method for Equilibrium
» Absolute and Relative Availability Under Interactions with Ambient
» Irreversibility or Lost Work
» Applications of the Availability Balance Equation
» Closed System (Non–Flow Systems)
» Heat Pumps and Refrigerators
» Work Producing and Consumption Devices
» Graphical Illustration of Lost, Isentropic, and Optimum Work
» Flow Processes or Heat Exchangers
» CLASSICAL RATIONALE FOR POSTULATORY APPROACH
» Generalized Legendre Transform
» Van der Waals (VW) Equation of State
» Other Two–Parameter Equations of State
» Compressibility Charts (Principle of Corresponding States)
» Boyle Temperature and Boyle Curves
» Three Parameter Equations of State
» Empirical Equations Of State
» State Equations for Liquids/Solids
» Internal Energy (du) Relation
» EXPERIMENTS TO MEASURE (u O – u)
» Vapor Pressure and the Clapeyron Equation
» Saturation Relations with Surface Tension Effects
» Temperature Change During Throttling
» Throttling in Closed Systems
» Procedure for Determining Thermodynamic Properties
» Euler and Gibbs–Duhem Equations
» Relationship Between Molal and Pure Properties
» Relations between Partial Molal and Pure Properties
» Mixing Rules for Equations of State
» Partial Molal Properties Using Mixture State Equations
» Ideal Solution and Raoult’s Law
» Completely Miscible Mixtures
» DEVIATIONS FROM RAOULT’S LAW
» Mathematical Criterion for Stability
» APPLICATION TO BOILING AND CONDENSATION
» Physical Processes and Stability
» Constant Temperature and Volume
» Equivalence Ratio, Stoichiometric Ratio
» Entropy, Gibbs Function, and Gibbs Function of Formation
» Entropy Generated During an Adiabatic Chemical Reaction
» MASS CONSERVATION AND MOLE BALANCE EQUATIONS
» Evaluation of Properties During an Irreversible Chemical Reaction
» Criteria in Terms of Chemical Force Potential
» Generalized Relation for the Chemical Potential
» Nonideal Mixtures and Solutions
» Gas, Liquid and Solid Mixtures
» Availability Balance Equation
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