Chapter 7 Application of Thermodynamics to Flow Processes Review For a steady-state flow process M+答+g=0+形 名-2a8-2增a (∑B)n=(∑B)+D 7.1 Duct Flow of Compressible Fluid 7.2 Turbines(expanders) 7.3 Compression Processes 7.1 Duct Flow of Compressible Fluid 2+84=Q+m H145 H3u,2, △H=0orH2=H hrottling Processoccurs at constant enthalpy Thinking(7-1) (1)throttlingprocess for idealgas T1 T2? (2)throttling process for wet steam Cause the liquid to evaporateand the vaporto become superheated
Chapter 7 Application of Thermodynamics to Flow Processes Review For a steady-state flow process 2 2 s u H g z Q W + + = + , j j j i i G j i j j Q m S m S S T − − = ( ) ( ) B B D in out = + 7.1 Duct Flow of Compressible Fluid 7.2 Turbines (expanders) 7.3 Compression Processes 7.1 Duct Flow of Compressible Fluid 2 2 u H g z Q W + + = + hrottling Process occurs at constant enthalpy Thinking(7-1) (1) throttling process for ideal gas T1、T2? (2) throttling process for wet steam Cause the liquid to evaporate and the vapor to become superheated 2 1 = = H or H H 0 1 1 1 1 1 P T H u z 2 2 2 2 2 P T H u z
(3)throttlingprocess for saturatedliquid Some ofliquid vaporizes or flashes 7.1.1 Throttling Process Joule-Thomsoncoefficient - 微分节流效应系数,有时用山,表示 节流过程中压力变化所引起的温度变化: A=T,-I=∫udP Joule-Thomson coefficient ())()- (》=c ,- 别 部-().(〔) ,-r- V=ZRT/P
(3) throttling process for saturated liquid Some of liquid vaporizes or flashes 7.1.1 Throttling Process Joule-Thomson coefficient H s T P = 微分节流效应系数,有时用 J 表示 节流过程中压力变化所引起的温度变化: 2 1 2 1 d P H P = − = T T T P Joule-Thomson coefficient 1 y x F F x y x y F = − P P H C T = T P H V V T P T = − H T P = H P T T T H P H P = − 1 P T H H T P − = − T P H V V T P T = − V ZRT P = /
),-( “=部) u For ideal gas 21-0 For real gas 某种气体的节流效应可以通过实验确定在某一高压状态P1,T1, 向不同P2进行节流膨胀,同时可测得此时的2,描点画图,可得出 一系列等焓线。等焓线上任一点的斜率值即为μ值。 H0 Constant enthalpy curve <0 <0 T -Inversion point 4>0 Joule-Thomson inversion curve P Inversion curves for reduced coordinates Thinking(7-2) Application ofthermodynamics to other flow processes
2 T P H Z RT P P T = − 1 P T H C P = − 2 P P RT Z C P T = For ideal gas 2 1 0 P P RT Z Z C P T = = = For real gas 某种气体的节流效应可以通过实验确定.在某一高压状态 P1,T1, 向不同 P2 进行节流膨胀,同时可测得此时的 T2,描点画图,可得出 一系列等焓线。等焓线上任一点的斜率值即为 μ 值。 Thinking(7-2) Application of thermodynamics to other flow processes = 0 Joule-Thomson inversion curve 0 0 P T Constant enthalpy curve Inversion point Inversion curves for reduced coordinates Pr Tr 0 0
4H+4n +g△=Q+W 2 (2)Nozzle and Diffuser Diffu Nozzle 喷嘴与扩压管的结构特点是进出口截面积变化很大。流体通过 时,使压力沿着流动方向降低,而使流速加快的部件称为喷嘴。反之, 使流体流速减缓,压力升高的部件称为扩压管。 Thinking(7-2) :+g=Q+ AH+-0 2 A,-H=-蓝 流体通过焓值的改变来换取动能的调整 2 7.2 Turbines(expanders) 7.2.1 Reversible Adiabatic Expansion(可逆绝热膨胀) 容-号- d
2 2 s u H g z Q W + + = + = H Q (2) Nozzle and Diffuser 喷嘴与扩压管的结构特点是进出口截面积变化很大。流体通过 时,使压力沿着流动方向降低,而使流速加快的部件称为喷嘴。反之, 使流体流速减缓,压力升高的部件称为扩压管。 Thinking(7-2) 2 2 s u H g z Q W + + = + 2 0 2 u H + = 2 2 1 2 2 1 2 u u H H − − = 流体通过焓值的改变来换取动能的调整 7.2 Turbines (expanders) 7.2.1 Reversible Adiabatic Expansion(可逆绝热膨胀) , ( ) ( ) CV j fs G j j d mS Q mS S dt T + − = Nozzle Diffuser
△(mS)6=0 Because of△(mS)s=∑m,S,-∑m,S S0∑ms=∑m5,orAS=0 Isentropicprocess 微分等熵效应系数 4-( %) 4>0 制冷效应 任何气体在任何条件下,进行等熵膨胀,气体温度必定降低 节流过程中压力变化所引起的温度变化: △T=T2-T=∫4dP 7.2.2 Principle of Turbines(expanders) A turbines (expanders)consists of alternate sets of nozzles and T,P rotating blades 2 T2,P2
( ) 0 = mS fs Because of ( )fs j j i i j i = − mS m S m S So i i j j i j m S m S = or = S 0 Isentropic process 微分等熵效应系数 S S T P = S P P T V C T = 0 S 制冷效应 任何气体在任何条件下,进行等熵膨胀,气体温度必定降低 节流过程中压力变化所引起的温度变化: 2 1 2 1 d P S S P = − = T T T P 7.2.2 Principle of Turbines (expanders) A turbines (expanders) consists of alternate sets of nozzles and rotating blades 1 2 T2, P2 T1, P1 Ws