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Control Volumes Thermodynamics Professor Lee Carkner Lecture 9

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Control Volumes. Thermodynamics Professor Lee Carkner Lecture 9. PAL # 8 Specific Heat. Piston of N 2 compressed polytropically Can find work from polytropic eqn. W = mR(T 2 -T 1 )/(n-1) Final pressure: P 1 V n 1 =P 2 V n 2 P 2 = (V 1 /V 2 ) 1.3 (P 1 ) = (2 1.3 )(100) = - PowerPoint PPT Presentation

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Page 1: Control Volumes

Control Volumes

Thermodynamics

Professor Lee Carkner

Lecture 9

Page 2: Control Volumes

PAL # 8 Specific Heat Piston of N2 compressed polytropically

Can find work from polytropic eqn.

W = mR(T2-T1)/(n-1) Final pressure:

P1Vn1=P2Vn

2

P2 = (V1/V2)1.3 (P1) = (21.3)(100) = Final temperature

P1V1/T1 = P2V2/T2

T2 = (P2/P1)(V2/V1)T1 = (246.2/100)(0.5)(300) =

Page 3: Control Volumes

PAL # 8 Specific Heat Work is:

W = (0.8)(0.2968)(369.3-300) / (1-1.3) =

Can get E from cv

Average T = (369+300)/2 = 335 K

U = mu = mcvT U = (0.8)(0.744)(369.3-300) =

Q = 54.8 – 41.2 =

Page 4: Control Volumes

Control Volume

For a control volume, mass can flow in and out Mass flow rate depends on:

Velocity normal to Ac: Vn

Note that:

V = velocity V =volume

Page 5: Control Volumes

Flow

Mass flowing through a pipe

Not easy to solve

Velocity is not

Vavg = V = (1/Ac) ∫ Vn dAc

We can now write:

Page 6: Control Volumes

Volume

The volume flow rate is just:

Related to the mass flow rate just by the

density:

In m3/s

Page 7: Control Volumes

Conservation of Mass

We examine: Mass streams flowing out = mout

So then: m’in – m’out = dmcv/dt

Page 8: Control Volumes

Common Cases For the steady flow case:

m’in = m’out

For systems with just a single stream:

1V1A1 = 2V2A2

For incompressible fluids, 1 = 2

V’1 = V’2

Page 9: Control Volumes

Flow Work

The amount of energy needed to push fluid into a control volume is the flow work:

Can think of it as a property of the fluid itself

Page 10: Control Volumes

Energy

Our previous result for fluid energy was:

We can add the flow work, but note:

We designate the total fluid energy per unit

mass by :

= h + V2/2 + gz Now we don’t have to worry about the flow work

Page 11: Control Volumes

Energy and Mass Flow

The total is:

E’mass = m’ = m’(h + V2/2 +gz)

If V and z are small:

True for most systems

Page 12: Control Volumes

Steady-Flow Systems

Once they are up and running the

properties of the fluid at a given point don’t change with time

q – w = = h + V2/2 + gz Energy balance for a steady flow system per

unit mass

Page 13: Control Volumes

Steady Flow Heat and Work

Heat This is the net heat Q’in-Q’out

Work Boundary work = 0, flow work part of enthalpy Remaining work:

Page 14: Control Volumes

Steady Flow Energies

Enthalpy h is difference between inlet and exit

Kinetic energy

Often very small

Potential energy

10’s or 100’s of meters

Page 15: Control Volumes

Automotive Cooling System

Page 16: Control Volumes

Example: Radiator

Assume cooling fluid is water

Flow velocity about 1 m/s

Maximum height differential about 1 meter gz = (9.8)(1) /(1000) = 0.0098 kJ/kg

Page 17: Control Volumes

Next Time

Read: 5.4-5.5 Homework: Ch 5, P: 17, 21, 36, 75