A turbine discharges 216.3 kg/h saturated steam at 10.0 bar. It is desired to generate steam at 250°C and 10.0 bar by mixing the turbine discharge with a second stream of superheated steam of 300°C and 10.0 bar. For 393.2 kg/h of the product stream to be generated , how much heat must be added to the mixer in kW? Report positive umber.
A turbine discharges 216.3 kg/h saturated steam at 10.0 bar. It is desired to generate steam...
1. a) Superheated steam at T1 (°C) and corresponding specific enthalpy H^1 and 10.0 bar pressure is combined with saturated steam at T2 (°C) and 7.0 bar pressure in a ratio 1.96kg of steam at 10.0 bar / 1.0 kg steam at 7.0 bar. The product stream is at 250°C and 7.0 bar. The process operates at steady state. What is the specific enthalpy H^1 associated with stream 1 assuming that the blender operates adiabatically? b) You have calculated the...
Saturated steam at a pressure of 5.0 bar, abs with a flowrate of 220 kg/h is mixed with superheated steam at the same pressure with a temperature of 500 degrees Celsius and a flowrate of 480 kg/h. If the mixing is both adiabatic and isobaric what is the temperaure of the steam produced in degrees Celsius?
In a cogeneration plant, 10% kg/h of steam at 80 bar, 480 °C expands in the h.p. turbine to 10 bar. From the exhaust 4 x 10 kgh of steam is extracted for process heating. The remaining steam expands in the l.p. turbine to 0.08 bar. Saturated liquid at 0.08 bar leaving the condenser is pumped to 9.5 bar where it mixes with the condensate from the process heater leaving at 9.5 bar, 120°C. The entire flow is then pumped...
In a cogeneration plant, 10^6 kg/h of steam at 80 bar, 480 °C expands in the h.p. turbine to 10 bar. From the exhaust 4 x 10 kgh of steam is extracted for process heating. The remaining steam expands in the l.p. turbine to 0.08 bar. Saturated liquid at 0.08 bar leaving the condenser is pumped to 9.5 bar where it mixes with the condensate from the process heater leaving at 9.5 bar, 120°C. The entire flow is then pumped...
Steam enters a turbine with mass flow rate of 62.0 kg/s. The inlet pressure is 80.0 bar and temperature 350°C. The outlet contains saturated steam at 5.0 bar. At steaady state calculate the power generated by the turbine in kW.(you need to report positive number). Assume negligible heat loss.
In a cogeneration plant, 10^6 kg/h of steam at 80 bar, 480 °C expands in the h.p. turbine to 10 bar. From the exhaust 4 x 10 kgh of steam is extracted for process heating. The remaining steam expands in the l.p. turbine to 0.08 bar. Saturated liquid at 0.08 bar leaving the condenser is pumped to 9.5 bar where it mixes with the condensate from the process heater leaving at 9.5 bar, 120°C. The entire flow is then pumped...
Question 38 (2 points) A steam turbine receives 10 kg/s of superheated steam at 120 bar and 600°C. The steam expands adiabatically through the turbine and exits at a pressure of 0.2 bar and a quality of 90%. The steam inlet velocity is 200 m/s and the exit velocity is 50 m/s. Determine the power output of the turbine. 12.531 kW e) 12,344 kW (0) 12,719 kW None of the above
Problem 7.47 Adiabatic Steam Blender Superheated steam at Ti(°C) and 20.0 bar is combined with saturated steam at T2 (°C) and 12.0 bar in a ratio (1.45 kg of steam at 20.0 bar)/(1.0 kg of steam at 12.0 bar) The product stream is at 250°C and 12.0 bar. The process operates at steady state. Physical Property Tables ▼ Temperature of Saturated Steam Estimate the temperature of the saturated steam at 12.0 bar the tolerance is +/-5% Click if you would...
Chemical Engineering Question 100 KW of energy from a stream of superheated steam@ 200kg/sec, 10 bar and 2100 C is used in a heat exchanger to preheat a reactor feed. Determine the (a) enthalpy, (b) temperature and the phase of the resulting stream. 100 Kg/hr. of a saturated steam at 1 bar is mixed with superheated steam available at 4000C and 1 bar to produce superheated steam at 3000C and 1 bar. Calculate amount of superheated steam produced at 3000C...
Steam enters the first-stage turbine shown in Fig. P4.50 at 40 bar and 500℃ with a volumetric flow rate of 90 m3/min. Steam exits the turbine at 20 bar and 400℃. The steam is then reheated at constant pressure to 500℃ before entering the second-stage turbine. Steam leaves the second stage as saturated vapor at 0.6 bar. For operation at steady state, and ignoring stray heat transfer and kinetic and potential energy effects, determine the(a) mass flow rate of the...