using steam table we get the following data
we have calculated the above table data
I.e hf=424.26 BTU/lb
hg=1205.3 BTU/lb
so using h=hf +x(hg-hf)
or 600=424.26+x(1205.3-424.26)
calculating we get x=0.225 ans
what is the quality of steam at 400 psia if the enthalpy of the steam is...
questioni 211 point) Javea What is the enthalpy of steam at 1200 psia and 900°F? 567.26 BTU/ID 1184.2 BTU/Ib 1621.8 BTU/Ib 1440.9 BTU/ID Question 3 (1 point) Saturated steam at 220 psia is heated to 700°F at constant pressure. What is the change in enthalpy? 172.9 BTU/Ib 835.91 BTU/Ib 1200.1 BTU/Ib 1373.0 BTU/ID
A steam plant generates saturated steam at 600 psia. The condensate exits the condenser at 5 psia and 158 ºF. The feed pump and main turbine are isentropic. Find: a. Is the condensate sub-cooled? If so, how much condensate depression is there (ºF) b. Is the generated steam superheated? If so, how much superheat is there (ºF)? c. Determine all four state point enthalpy (h) values (BTU/lbm).
Determine the following properties of superheated steam at 400 psia and 7950F. (a) Specific volume (b) Enthalpy (10)
punlp. Problem #10)(10 points) Determine the specific volume and enthalpy of steam at 10 psia and 90% quality. Also determine the percent by volume of saturated vapor in the mixture.
Problem A: 15 Ibm of saturated vapor steam at 10 psia is contained in a frictionless piston-cylinder arrangement. The steam is heated at constant pressure to 400° F. a. Calculate the work done by the steam on the piston, in BTUS. b. Calculate the amount of heat delivered to the steam for this process, in BTUS. c. Determine the change in internal energy of the steam, in BTUs.
Problem 4 A steam turbine is used to generate power. The turbine expansion process is "adiabatic," this means that there is no heat transfer during this process. The inlet and exit conditions are listed below T1 = 600-degF P2 10-psia T2 1932-degF x2 0.9 P1 500-psia BTU lb Adiabatio Steam Turbine h1:= 1299.1·ww s1 1.5652. BTU b-R Qloss 0 BTU lb At 10 psia, BTU h,-1143.3- BTU BTU lb s,-1.788-en lb-R hr:= 161.2- S(30-2836. A. Determine the work of the...
Air is compressed isothermally from 13 psia and 55°F to 74 psia in a reversible steadyflow device. Calculate the work required. In Btu/bm, for this compression. The gas constant of air is R=0.06855 Btu/ibm-R. The work required for this compression is Btu/ibm
10. (25 Points) Steam enters an insulated nozzle at 140 psia, 600 F with a velocity of 100 ft/s. It leaves the nozzle at 20 psia, 360°F. The mass flow rate is 10 lbm/s. Find: Ans a) b) Ans. The actual kinetic energy of the steam at the exit, in Btu The exit velocity in ft/s for part a) The exit cross sectional area of the nozzle, in in The nozzle isentropic efficiency (%) Show the actual and the ideal...
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PROBLEM #2 (68 pts.) Steam at 200 psia, 600°F (State 1) enters an adiabatic turbine cperating at steady state with a mass flow rate of 16.5 lbm/min and exits at 15 psia, 240°F (State 2), Neglecting the changes in kinetic and potential energies and assuming the surroundings to be at T.- 537 R. Determine: a) the actual power output, in Btu/min. b) the reversible (or maximum) power output, in Btu/min. c) the rate of exergy destruction, in Btu/min....
A ship's steam turbine receives 7200 lbm/min of steam at pressure of 900psia and a velocity of 100ft/s. The steam leaves the turbine at 450 psia with a velocity of 800 ft/s. Specific enthalpy at the inlet and exit, respectively, are 1508.9 Btu/lbm and 1238.5 Btu/lbm. As the steam passes through turbine 12 Btu/lbm of heat is lost to the environment. a) Using the Steady Flow Energy Equation, determine the specific work generated by this turbine. (Btu/lbm) b) Determine the...