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Control Volumes

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Can find work from polytropic eqn. W = mR(T2-T1)/(n-1) Final pressure: P1Vn1=P2Vn2. P2 = (V1/V2)1.3 (P1) = (21.3)(100) = Final temperature. P1V1/T1 = P2V2/T2 ... – PowerPoint PPT presentation

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Title: Control Volumes


1
Control Volumes
  • Thermodynamics
  • Professor Lee Carkner
  • Lecture 9

2
PAL 8 Specific Heat
  • Piston of N2 compressed polytropically
  • Can find work from polytropic eqn.
  • W mR(T2-T1)/(n-1)
  • Final pressure
  • P1Vn1P2Vn2
  • 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)

3
PAL 8 Specific Heat
  • Work is
  • W (0.8)(0.2968)(369.3-300) / (1-1.3)
  • Can get DE from cv
  • Average T (369300)/2 335 K
  • DU mDu mcvDT
  • DU (0.8)(0.744)(369.3-300)
  • Q 54.8 41.2

4
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

5
Flow
  • Mass flowing through a pipe
  • Not easy to solve
  • Velocity is not
  • Vavg V (1/Ac) ? Vn dAc
  • We can now write

6
Volume
  • The volume flow rate is just
  • Related to the mass flow rate just by the
    density
  • In m3/s

7
Conservation of Mass
  • We examine
  • Mass streams flowing out mout
  • So then
  • min mout dmcv/dt

8
Common Cases
  • For the steady flow case
  • S min S mout
  • For systems with just a single stream
  • r1V1A1 r2V2A2
  • For incompressible fluids, r1 r2
  • V1 V2

9
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

10
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 q
  • q h V2/2 gz
  • Now we dont have to worry about the flow work

11
Energy and Mass Flow
  • The total is
  • Emass mq m(h V2/2 gz)
  • If V and z are small
  • True for most systems

12
Steady-Flow Systems
  • Once they are up and running the properties of
    the fluid at a given point dont change with time
  • q w Dq Dh DV2/2 gDz
  • Energy balance for a steady flow system per unit
    mass

13
Steady Flow Heat and Work
  • Heat
  • This is the net heat Qin-Qout
  • Work
  • Boundary work 0, flow work part of enthalpy
  • Remaining work

14
Steady Flow Energies
  • Enthalpy
  • Dh is difference between inlet and exit
  • Kinetic energy
  • Often very small
  • Potential energy
  • 10s or 100s of meters

15
Automotive Cooling System
16
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

17
Next Time
  • Read 5.4-5.5
  • Homework Ch 5, P 17, 21, 36, 75
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