Question

A gas mixture at 685.0°C and 135 kPa absolute enters a heat exchanger at a rate of 73.0 m/hr. The gas leaves the heat exchang

0 0
Add a comment Improve this question Transcribed image text
Answer #1

We have the ideal gas equation,

PV = nRT

Where, P is the pressure of the gas, V is the volume, n is the number of moles, R is the gas constant and T is the temperature in Kelvin

By substituting the values, the number of moles can be calculated as,

n = PV/RT = [(135 x 103 Pa)(73 /3600 m3/s)]/ (8.314 m3Pa/Kmol)( 958 K) = 0.343 mol/s

Here, the change in enthalpy = -5.60 kJ/mol

We have,

Heat = q = H x n = -5.60 kJ/mol x 0.343 mol/s = -1.92 kW

Heat required = -1.92 kW

Add a comment
Know the answer?
Add Answer to:
A gas mixture at 685.0°C and 135 kPa absolute enters a heat exchanger at a rate...
Your Answer:

Post as a guest

Your Name:

What's your source?

Earn Coins

Coins can be redeemed for fabulous gifts.

Not the answer you're looking for? Ask your own homework help question. Our experts will answer your question WITHIN MINUTES for Free.
Similar Homework Help Questions
  • A gas mixture at 445.0°C and 105 kPa absolute enters a heat exchanger at a rate...

    A gas mixture at 445.0°C and 105 kPa absolute enters a heat exchanger at a rate of 74.0 m/hr. The gas leaves the heat exchanger at 165.0°C. The change in enthalpy of the gas during the cooling process is -6.10 kJ/mol. What is the heat required in kW? Assume the gas behaves ideally and that the changes in kinetic and potential energy are negligible. Number

  • A gas mixture at 560.0°C and 129 kPa absolute enters a heat exchanger at a rate of 70.0 m/hr. The qas leaves the heat e...

    A gas mixture at 560.0°C and 129 kPa absolute enters a heat exchanger at a rate of 70.0 m/hr. The qas leaves the heat exchanger at 205.0°C. The change in enthalpy of the gas during the cooling process is -4.50 kJ/mol. What is the heat required in kW? Assume the gas behaves ideally and that the changes in kinetic and potential energy are negligible. Number kW

  • Q4/ Toluene gas (CH3) enters a continuous adiabatic heat exchanger at (35°C) and (300 KPa) and...

    Q4/ Toluene gas (CH3) enters a continuous adiabatic heat exchanger at (35°C) and (300 KPa) and exits at (260°C). Superheated steam at (400°C) and (5 bar) enters to exchanger flowing counter currently to a Toluene and exits as a saturated liquid at the same pressure. 1- If (150 mol) of Toluene is fed, draw and label a process flow chart. 2- Calculate the values of inlet-outlet enthalpies. 3- Calculate the volumetric feed ratio of the two streams (m' steam fed/mºtoluene...

  • Propane gas enters a continuous adiabatic heat exchanger 240°C. Superheated steam at 300 C and 5 bar enters the exchang...

    Propane gas enters a continuous adiabatic heat exchanger 240°C. Superheated steam at 300 C and 5 bar enters the exchanger flowing countercurrently to the propane and exits as a saturated liquid at the same pressure at 40 C and 250 kPa and exits at Taking flow chart. Include both mass and volumes on your inlet and outlet streams. b. Calculate the specific enthalpy values for the inlet and outlet streams. c. Use an energy balance to calculate the required mass...

  • Steam enters a counterflow heat exchanger operating at steady state at 0.07 MPa with a quality...

    Steam enters a counterflow heat exchanger operating at steady state at 0.07 MPa with a quality of 0.9 and exits at the same pressure as saturated liquid. The steam mass flow rate is 1.3 kg/min. A separate stream of air with a mass flow rate of 100 kg/min enters at 30oC and exits at 60oC. The ideal gas model with cp = 1.005 kJ/kg·K can be assumed for air. Kinetic and potential energy effects are negligible. Determine the temperature of...

  • Problem 3 Steam enters a heat exchanger at 0.1 bar with a quality of 0.95 and...

    Problem 3 Steam enters a heat exchanger at 0.1 bar with a quality of 0.95 and condensate exits at 0.1 bar and 45'C. Cooling water enters the heat exchanger in a separate stream as a liquid at 20'C and exits as a liquid at 35 C with no changes in pressure. Heat transfer from the outside of the heat exchanger and changes in the kinetic and potential energies of the flowing streams can be ignored. For steady state operation, (a)...

  • pls Q4/ Toluene gas (C,Hg) enters a continuous adiabatic heat exchanger at (35°C) and (300 KPa)...

    pls Q4/ Toluene gas (C,Hg) enters a continuous adiabatic heat exchanger at (35°C) and (300 KPa) and exits at (260°C). Superheated steam at (400°C) and (5 bar) enters to exchanger flowing counter currently to a Toluene and exits as a saturated liquid at the same pressure. 1- If (150 mol) of Toluene is fed, draw and label a process flow chart. 2- Calculate the values of inlet-outlet enthalpies. 3- Calculate the volumetric feed ratio of the two streams (m' steam...

  • please Q4/ Toluene gas (C,Hg) enters a continuous adiabatic heat exchanger at (35°C) and (300 KPa)...

    please Q4/ Toluene gas (C,Hg) enters a continuous adiabatic heat exchanger at (35°C) and (300 KPa) and exits at (260°C). Superheated steam at (400°C) and (5 bar) enters to exchanger flowing counter currently to a Toluene and exits as a saturated liquid at the same pressure. 1- If (150 mol) of Toluene is fed, draw and label a process flow chart. 2- Calculate the values of inlet-outlet enthalpies. 3- Calculate the volumetric feed ratio of the two streams (m' steam...

  • Could someone help with the following problem??? Helium enters a constant flow heat exchanger at 100...

    Could someone help with the following problem??? Helium enters a constant flow heat exchanger at 100 kPa, 100 C, and 90 m / s, and receives heat in the amount of 120 kJ / kg as it flows through it. Helium leaves the heat exchanger at 80 kPa with a speed of 150 0 m / s. Determine the pressure and temperature of nitrogen stagnation in the input and output states. Helium enters a constant flow heat exchanger at 100...

  • A mixture containing 35 mole% n-butane and the balance isobutane at 10°C enters a heat exchanger...

    A mixture containing 35 mole% n-butane and the balance isobutane at 10°C enters a heat exchanger at a rate of 24.5 kmol/h and at 1.96 bar pressure. The exchanger has been designed to heat and vaporize the liquid and heat the vapor mixture to 180°C. The heating fluid is a high molecular weight liquid with a constant heat capacity (Cp=2.62 kJ/kg C).It enters the exchanger at 215°C and flows countercurrently to the hydrocarbon mixture. According to the heat exchanger design...

ADVERTISEMENT
Free Homework Help App
Download From Google Play
Scan Your Homework
to Get Instant Free Answers
Need Online Homework Help?
Ask a Question
Get Answers For Free
Most questions answered within 3 hours.
ADVERTISEMENT
ADVERTISEMENT
ADVERTISEMENT