Consider sterilization of the pharmaceutical product of Problem 8.27. To avoid any possibility of heating the product to an unacceptably high temperature, atmospheric steam is condensed on the exterior of the tube instead of using the resistance heater, providing a uniform surface temperature,
(a) For the conditions of Problem 8.27, determine the required length of straight tube,
(b) Consider replacing the straight tube with a coiled tube characterized by a coil diameter
(c) Calculate the pressure drop through the straight tube and through the coiled tube.
(d) Calculate the steam condensation rate.
Want to see the full answer?
Check out a sample textbook solutionChapter 8 Solutions
Fundamentals of Heat and Mass Transfer
Additional Engineering Textbook Solutions
Shigley's Mechanical Engineering Design (McGraw-Hill Series in Mechanical Engineering)
Thinking Like an Engineer: An Active Learning Approach (3rd Edition)
Heating Ventilating and Air Conditioning: Analysis and Design
Fox and McDonald's Introduction to Fluid Mechanics
Vector Mechanics for Engineers: Statics and Dynamics
HEAT+MASS TRANSFER:FUND.+APPL.
- Twelve liters per minute of hot water at 330 K flow through a 0.5 inch schedule 40 (0.622 in wall thickness) domestic hot water line. What is the heat transfer coefficient inside the pipe? The kinematic viscosity is 0.5 x 106. The Prandtl number is 3.2.arrow_forward8.25 Engine oil flows at a rate of 1 kg/s through a 5-mm-diameter straight tube. The oil has an inlet temperature of 45°C and it is desired to heat the oil to a mean temperature of 80°C at the exit of the tube. The surface of the tube is maintained at 150°C. Determine the required length of the tube. Hint: Calculate the Reynolds numbers at the entrance and exit of the tube before proceeding with your analysis.arrow_forward2. Engine oil (similar to oil C) flows at 1.2 ft/s through a 1-inch diameter tube. The bulk oil temperature is 190 F and the tube surface temperature is 210 F. Determine the unit convective coefficient for a tube length of 10 ft. If the tube length is doubled, what is the percentage increase (or decrease) in the film coefficient? Let k = 0.96 Btu-in/hr-ft2-F and c = 0.52 Btu/lb-F for the oil. *arrow_forward
- A thick-walled cylinder tubing of hard rubber having an inside radius of 20mm is being used as temporary cooling coil in a bath. Ice water is flowing rapidly through inside tube and the inside wall temperature is 274.9K. The outside surface temperature is 297.1K. A total of 14.65W must be removed from the bath by cooling coil. How many m of tubing are required?arrow_forwardProblem 2: A 5mm x 20 mm rectangle tube houses fully-developed flow of water. The surface temperature is 45°C, and the water enters at 25°C and exits at 35°C. What is the heat transfer.arrow_forwardCurrent Attempt in Progress Consider pressurized water, engine oil (unused), and Nak (22 %/78%) flowing in a 20-mm-diameter tube. (a) Determine the mean velocity, in m/s, the hydrodynamic entry length, in m, and the thermal entry length, in m, for each of the fluids when the fluid temperature is 366 K and the flow rate is 0.014 kg/s. (b) Determine the mass flow rate, in kg/s, the hydrodynamic entry length, in m, and the thermal entry length, in m, for water and engine oil at 300 and 400 K and a mean velocity of 0.018 m/s. Part A Your answer is incorrect. Determine the mean velocity, in m/s, the hydrodynamic entry length, in m, and the thermal entry length, in m, for each of the fluids when the fluid temperature is 366 K and the flow rate is 0.014 kg/s. Liquid water engine oil Nak (m/s) ! i XALA(M) xer (m) Attempts: unlimited Submit Answerarrow_forward
- Please help. I am not sure how to approach this problem. This problem involves heat transfer and internal flow within a pipe. Thank you.arrow_forwardA shell-and-tube heat exchanger is used to cool compressed liquid methanol from 176 °F to 104 °F. The methanol flows on the shell side of the exchanger. The coolant is water that rises in temperature from 50 °F to 86 °F and flows within the tubes at a rate of 68.9 kg s1. Finding the appropriate thermophysical data and applying the proper equations, you are required to do the following: (a) Calculate i) methanol mass flow rate in the exchanger, ii) methanol volumetric flowrate at the inlet of the exchanger. (b) i) For the counter-current flow of the fluids calculate the log temperature difference, ii) explain the purpose of calculating this difference, iii) explain, quantitatively, why is the counter-current flow in heat exchangers preferred to co-current flow. meanarrow_forwardanswer=correctarrow_forward
- Consider pressurized water, engine oil (unused), and Nak (22%/78%) flowing in a 20-mm-diameter tube. (a) Determine the mean velocity, in m/s, the hydrodynamic entry length, in m, and the thermal entry length, in m, for each of the fluids when the fluid temperature is 366 K and the flow rate is 0.01 kg/s. (b) Determine the mass flow rate, in kg/s, the hydrodynamic entry length, in m, and the thermal entry length, in m, for water and engine oil at 300 and 400 K and a mean velocity of 0.022 m/s. Part A Determine the mean velocity, in m/s, the hydrodynamic entry length, in m, and the thermal entry length, in m, for each of the fluids when the fluid temperature is 366K and the flow rate is 0.01 kg/s. Liquid Um (m/s) Xfdh (m) Xfd,t (m) water i engine oil i i i Nak iarrow_forwardA two effect system of evaporators with parallel forward feed flow of liquid and vapor is to be designed to concentrate continuously 10,000 Ib/h of a 10% by weight solution to 40%, the feed being at 150 °F. It is planned to use saturated steam condensing at 220 °F. Specific Heat of feed liquor is 0.9, while that leaving the first effect is equal to the average specific heat of feed and product. The overall heat transfer coefficients are 300 and 400 BTU/(f2-hr-°F) for the first and second effects respectively. The latent heat of vaporization for the vapor leaving the first effect is 1002.3 BTU/lb and 1020 BTU/lb for the second. Calculate for the steam economy and the heat transfer area in each effect. Given: (1) Required: andarrow_forwardEthylene glycol flows at 0.02 kg/s through a 4-mm diameter, thin-walled tube. The tube is coiled and submerged in a well-stirred water bath maintained at 35°C. If the fluid enters the tube at 93°C, what heat rate and tube length are required for the fluid to leave at 41°C? Neglect heat transfer enhancement associated with the coiling. Draw temperature profile. Net fluld The Colled tubing Well- stirred water bath WWarrow_forward
- Elements Of ElectromagneticsMechanical EngineeringISBN:9780190698614Author:Sadiku, Matthew N. O.Publisher:Oxford University PressMechanics of Materials (10th Edition)Mechanical EngineeringISBN:9780134319650Author:Russell C. HibbelerPublisher:PEARSONThermodynamics: An Engineering ApproachMechanical EngineeringISBN:9781259822674Author:Yunus A. Cengel Dr., Michael A. BolesPublisher:McGraw-Hill Education
- Control Systems EngineeringMechanical EngineeringISBN:9781118170519Author:Norman S. NisePublisher:WILEYMechanics of Materials (MindTap Course List)Mechanical EngineeringISBN:9781337093347Author:Barry J. Goodno, James M. GerePublisher:Cengage LearningEngineering Mechanics: StaticsMechanical EngineeringISBN:9781118807330Author:James L. Meriam, L. G. Kraige, J. N. BoltonPublisher:WILEY