Elements Of Electromagnetics
7th Edition
ISBN: 9780190698614
Author: Sadiku, Matthew N. O.
Publisher: Oxford University Press
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hi, where did u get this R value from. these are the values i have
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hi, where did u get this R value from. these are the values i have
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- Superheated steam from boiler expands in turbine from initial pressure p₁ = 230 bar and initial temperature T₁ = 577 °C to pressure p₂ = 1 MPa. Isentropic efficiency of turbine ns is 0.8. Steam mass flow rate am,h is 146 kg/s. Read from h,s-chart Enthalpy of superheated steam h Enthalpy after isentropic expansion h₂,s Calculate: Enthalpy at the turbine outlet h₂ Power of turbine P MWarrow_forwardHelium is compressed through a compressor steadily. At the inlet the pressure is and the temperature is . At the exit the pressure is and the temperature is . The power input is and the heat loss rate is during this process. Neglect the kinetic and potential energy changes. Assume helium is ideal gas with a constant specific heat and its specific heat ratio , which means that enthalpy can be calculated using . Select the simplified the energy balance equation for this process_________ A. B. C. D.arrow_forwardA gas flows steadily through a rotary compressor at a temperature of 16 ⁰C, a pressure of 100kPa, and an enthalpy of 392.2 kJkg-1. The gas leaves the compressor at a temperature of 245⁰C, a pressure of 0.6 MPa and an enthalpy of 534.5 kJkg-1. There is no heat transfer to or fromthe gas as it flows through the compressor. Using the steady flow equation appropriate toeach case, evaluate the external work done per unit mass of gas: a) when the inlet and exit velocities of the gas are negligible b) when the inlet velocity of the gas is 80 ms-1 and the exit velocity of the gas is 160 ms-1.arrow_forwardRefrigerant R-134a to the compressor of a refrigeration machine It enters at 140 kPa pressure and -10 °C, and exits at 1 MPa pressure. Volumetric flow of the refrigerant entering the compressor It is 0.23 m³/minute. The refrigerant enters the throttling valve at a pressure of 0.95 MPa and at 30 °C, and exits the evaporator as saturated steam at -18 °C. Adiabatic efficiency of the compressor It is 78%. Show the cycle in the T-s diagram. And; a) Calculate the power required to run the compressor. b) Calculate the heat absorbed per unit time from the cooled medium. ( COPSM=? ) c) Calculate, between the evaporator and the compressor, how much the pressure of the refrigerant drops and how much the heat gain.arrow_forwardHelium is compressed through a compressor steadily. At the inlet the pressure is and the temperature is . At the exit the pressure is and the temperature is . The power input is and the heat loss rate is during this process. Neglect the kinetic and potential energy changes. Assume helium is ideal gas with a constant specific heat and its specific heat ratio , which means that enthalpy can be calculated using . Calculate the work per unit mass _________arrow_forwardSteam at a rate of 200 kg/min enters a turbine at 350°C and 40 bar through a 7.5-cm internal diameter pipe. The turbine operation is adiabatic, and the effluent leaves as saturated water at 5 bar through a 5-cm diameter pipe. 1. Calculate the work produced by the turbine in kW. 2. What is the enthalpyand phase of the effluent stream? 21 If it leaves the turbine at 75C and 5 bar 22 If it leaves the turbine at 30C and 5 bar 7.5arrow_forwardNo Handwriting pleasearrow_forwardAn insulated tank A of 0.6 m3 volume is connected to an insulated tank B of 0.3m3 volume. Initially, tank A contains steam at 0.2 MPa and 200 °C, and tank B contains wet steam at 0.5 MPa and 85% quality. The valve is opened and flow occurs until equilibrium (both mechanical and thermal) is attained. Estimate the final pressure.arrow_forwardA rigid tank of volume 10 m³ initially contains saturated water vapor at a temperature of 120 °C. Steam at a pressure 1.2 MPa and a temperature of 400 °C enters the tank through a valve in steam line that is connected to the tank until the final pressure in the tank is 800 kPa, at which time the temperature is 200 °C. All kinetic and potential energy effects can be neglected. A schematic of the problem and properties at all state points except state 1 are shown in the figure below. All of the properties at state 2 and the inlet state i are provided on the figure. Initial State in Tank T₁-120 °C, Sat. vapor u₁=? kJ/kg V₁=? m³/kg Pi=1.2 MPa, Ti-400 °C hi-3261.3 kJ/kg V=10 m³ Final State in Tank T: 200 °C, P₂-800 kPa u₂= 2631.1 kJ/kg v₂=0.26088 m³/kg Qout For Question 6: The initial specific internal energy, u1, of the saturated vapor in the tank in kJ/kg isarrow_forwardarrow_back_iosarrow_forward_ios
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