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Thermodynamics

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234 | <strong>Thermodynamics</strong>EXAMPLE 5–4Deceleration of Air in a Diffuser>>Nozzle V 1Air at 10°C and 80 kPa enters the diffuser of a jet engine steadily with avelocity of 200 m/s. The inlet area of the diffuser is 0.4 m 2 . The air leavesthe diffuser with a velocity that is very small compared with the inlet velocity.Determine (a) the mass flow rate of the air and (b) the temperature ofthe air leaving the diffuser.V 1V 2V 2V 1V 1DiffuserFIGURE 5–25Nozzles and diffusers are shaped sothat they cause large changes in fluidvelocities and thus kinetic energies.P 1 = 80 kPaT 1 = 10°CAIRV 1 = 200 m/s m = ?A 1 = 0.4 m 2FIGURE 5–26Schematic for Example 5–4.>>T 2 = ?Solution Air enters the diffuser of a jet engine steadily at a specified velocity.The mass flow rate of air and the temperature at the diffuser exit are tobe determined.Assumptions 1 This is a steady-flow process since there is no change withtime at any point and thus m CV 0 and E CV 0. 2 Air is an ideal gassince it is at a high temperature and low pressure relative to its critical-pointvalues. 3 The potential energy change is zero, pe 0. 4 Heat transfer isnegligible. 5 Kinetic energy at the diffuser exit is negligible. 6 There are nowork interactions.Analysis We take the diffuser as the system (Fig. 5–26). This is a controlvolume since mass crosses the system boundary during the process. Weobserve that there is only one inlet and one exit and thus ṁ 1 ṁ 2 ṁ.(a) To determine the mass flow rate, we need to find the specific volumeof the air first. This is determined from the ideal-gas relation at the inletconditions:Then,v 1 RT 1P 1Since the flow is steady, the mass flow rate through the entire diffuser remainsconstant at this value.(b) Under stated assumptions and observations, the energy balance for thissteady-flow system can be expressed in the rate form asE # in E # out dE system >dt 0Rate of net energy transferby heat, work, and massm # 1 v 1V 1 A 1 ⎫⎪⎪⎪⎬⎪⎪⎪⎭⎫⎪⎪⎬⎪⎪⎭ 0.287 kPa # m 3 /kg # K21283 K280 kPa11.015 m 3 /kg 1200 m/s2 10.4 m2 2 78.8 kg/s¡ 0 (steady)Rate of change in internal, kinetic,potential, etc., energies 1.015 m 3 /kgm # a h 1 V 1 2E # in E # out2 b m# a h 2 V 2 2h 2 h 1 V 2 2 V 1222 b1since Q# 0, W # 0, and ¢pe 02The exit velocity of a diffuser is usually small compared with the inletvelocity (V 2 V 1 ); thus, the kinetic energy at the exit can be neglected.The enthalpy of air at the diffuser inlet is determined from the air table(Table A–17) to beh 1 h @ 283 K 283.14 kJ/kg

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