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VB . Net is a simple, modern, object-oriented computer programming language developed ... VB . Net programming is very much based on BASIC and Visual Basic ... 722 Isobutane expands adiabatically in a turbine from 5000 kPa and 52315 K (250 C) to 500 kPa at the rate of 07 kmol s-' If the turbine efficiency is 080, what is the power output of the turbine and what is the temperature of the isobutane leaving the turbine 723 The steam rate to a turbine for variable output is controlled by a throttle valve in the inlet line Steam is supplied to the throttle valve at 1700 kPa and 49815 K (225 C) During a test run, the pressure at the turbine inlet is 1000 kPa, the exhaust steam at 10 kPa has a quality of 095, the steam flow rate is 05 kg s-', and the power output of thc turbine is 180 kW (a) What are the heat losses from the turbine (6) What would be the power output if the steam supplied to the throttle valve were expanded isentropically to the final pressure 724 Carbon dioxide gas enters an adiabatic expander at 8 bar and 67315 K (400 C) and discharges at 1 bar If the turbine efficiency is 075, what is the discharge temperature and what is the work output per mole of C02 Assume COz to be an ideal gas at these conditions 725 Tests on an adiabatic gas turbine (expander) yield values for inlet conditions (TI, PI) and outlet conditions (Tz, P2) Assuming ideal gases with constant heat capacities, determine the turbine efficiency for one of the following: (a) TI = 500 K, P1 = 6 bar, Tz = 371 K, P2 = 12 bar, Cp/R = 712 (b) TI = 450 K, Pl = 5 bar, T2 = 376 K, P2 = 2 bar, Cp/R = 4 (c) Tl = 525 K, PI = 10 bar, T2 = 458 K, P2 = 3 bar, Cp/R = 11/2 (d) Tl = 475 K, Pl = 7 bar, T2 = 372 K, P2 = 15 bar, Cp/R = 912 (e) Tl = 550 K, PI = 4 bar, T2 = 403 K, P2 = 12 bar, Cp/R = 512 726 The efficiency of a particular series of adiabatic gas turbines (expanders) correlates with power output according to the empirical expression:. ","00","00001","0000000000000000047000000000000","OZ","000"," 30"," "," "," "," "," "," ","0000000000000000043410000000000","0000 000000000000060310000000000","6/15/05", "6/1/05","6/15/05","6/15/05","0/0/00","0/0/00","0/0/00","0/0/00","0/0/0 0"," "," "," "," "," "," ", " "," "," "," "," "," "," "," "," ","00000000000000000000000000000000"," "," "," "," ","00000000000000000000000000000000","000000000000000000000000000000 00"," "," "," "," "," "," ","0000000000000000000000000900000","00000000000000000000000000000000 "," ","KG","M3"," "," "," "," "," ","N"," "," "," "," ","00000000000000000000000000000000","F","FRF","000000000000000000 0001751000000 "," ","0000000000000000000000005139920","DEMODATA "," "," ","0/0/00","00000000000000000000000000000000","0000000000000000000000 0000000000"," "," ","DEMO ","ER43500 ","TN06DN12 ","5/7/97","0000000000000001610340000000000" "D","0000000000000000000010000000000","00001","0000000000000001000000 000000000", "PO","0000000000000000000010000000000","850 "," ","0/0/00","S","00000000000000000000000000000000"," ","9000 "," ","00001","0000000000000000047000000000000","OZ","000","000000000000 00000000100 00000000"," 30","00001"," "," "," ","0000000000000 0000000000000000000"," "," "," ","00000000000000000000000000000000"," ","00000000000000000000000000000000","00000000000000000434100000000 00","0000000000000000060310000000000","7/15/05","6/1/05","7/15/05","7/ 15/05","0/0/00","0/0/00","0/0/ 00","0/0/00","0/0/00","0/0/00","6/1/05","000000000000000000000000000000 00"," "," ","0000000000000000600620000000000","2001 ","2001 "," "," "," "," "," ","00000000000000000000000000000000","000000000000000000000000000000 00","Cro-Moly Frame, Red "," "," Here, I w 1 is the absolute value of the actual power output in kW Nitrogen gas is to be expanded from inlet conditions of 550 K and 6 bar to an outlet pressure of 12 bar For a molar flowrate of 175 mol s-I, what is the delivered power in kW What is the efficiency of the turbine What is the rate of entropy generation & Assume nitrogen to be an ideal gas with Cp = (7/2)R vb.net code to convert pdf to text How to Convert PDF to PDF /A in C#, VB . NET - E-iceblue
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