By Jayde Kowallis and Jordan Rhoads. Introduction A copper pipe wrapped with heated tape is needed to direct blow-by gasses from the engine crank case.

Slides:



Advertisements
Similar presentations
Extended Surfaces Chapter Three Section 3.6 Lecture 6.
Advertisements

Heat Transfer to Solids in a Flowing Fluid
Quiz – An organic liquid enters a in. ID horizontal steel tube, 3.5 ft long, at a rate of 5000 lb/hr. You are given that the specific.
ME 340 Project: Fall 2010 Heat Transfer in a Rice Cooker Brad Glenn Mason Campbell.
First Law of Thermodynamics - Open Systems
Lecture# 9 MASS AND ENERGY ANALYSIS OF CONTROL VOLUMES
Me 340 Project Ben Richards, Michael Plooster. -In many applications it is desirable to insulate a pipe in order to protect those working near it. -It.
Chapter 3.2: Heat Exchanger Analysis Using -NTU method
Jacob Adams ME 340 Winter The Problem: Long complex boiling equations Numerous cases and different variations can be confusing Evaluation takes.
Chapter 2: Overall Heat Transfer Coefficient
Transient Conduction of a Turkey Cooked by: Benjamin Baird & Michael Jarvis 1.
Analysis of Simple Cases in Heat Transfer P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Gaining Experience !!!
1 Dept. of Energy Technology, Div. of Applied Thermodynamics and Refrigeration Tube diameter influence on heat exchanger performance and design. Single.
Jed Goodell Jesse Williams. Introduction Problem How much heat does a particular heat sink dissipate How many fins are needed to dissipate a specific.
Mass and Energy Analysis of Control Volumes. 2 Conservation of Energy for Control volumes The conservation of mass and the conservation of energy principles.
Internal Flow Calculator Melissa Armstrong Micah Christiansen.
Thermal Analysis of Helium- Cooled T-tube Divertor S. Shin, S. I. Abdel-Khalik, and M. Yoda ARIES Meeting, Madison (June 14-15, 2005) G. W. Woodruff School.
1 Lec 26: Frictionless flow with work, pipe flow.
CHE/ME 109 Heat Transfer in Electronics LECTURE 18 – FLOW IN TUBES.
Chapter 5 Mass and Energy Analysis of Control Volumes Study Guide in PowerPoint to accompany Thermodynamics: An Engineering Approach, 5th edition.
Furnace Efficiency Bryce Cox Dallin Bullock. Problem My gas bill is very expensive My furnace claims an efficiency of 78% but it appears to be less efficient.
Chapter 16: Temperature and Heat. Heat Thermal energy that flows from something of high temp. to something of low temp. Warm  Cold Metric unit  Joules.
Gas Dynamics ESA 341 Chapter 2
Real Life Fin Problem By Matthew Elverud and Roger Smith.
SPECIFIC HEAT CAPACITY OF
HEAT EXCHANGERS Day 2.
Cooling Hot Chocolate in an insulated container James Jackson and Jordan Peterson.
Core Ag Engineering Principles – Session 1
How Much Does a Cooling Pad Help Your Laptop?
Feasibility Analysis h T1 T2 T3 T4 T5 One Dimensional Transient Analysis One Dimensional Finite Difference Steady State Analysis T1 and T5 will be known.
Chapter 4.1: Design and Rating of Double Pipe Heat Exchangers.
1/22/05ME 2591 ME 259 Heat Transfer Lecture Slides IV Dr. Gregory A. Kallio Dept. of Mechanical Engineering, Mechatronic Engineering & Manufacturing Technology.
Introduction to Heat Transfer
Solar Energy Systems in the Eco-Village at the University of Manitoba
Fouling Factor: After a period of operation the heat transfer surfaces for a heat exchanger become coated with various deposits present in flow systems,
1 CAMS in the School of Computing, Engineering and Physical Sciences Introductory fluid dynamics by Dr J. Whitty.
Chapter 10 Heat and Temperature. Temperature Page 324 Temperature is proportional to the average kinetic energy of an object.
Heat Transfer Equations For “thin walled” tubes, A i = A o.
Things to grab for this session (in priority order)  Pencil  Henderson, Perry, and Young text (Principles of Process Engineering)  Calculator  Eraser.
E NERGY SAVINGS : Central AC vs. Convective River Cooling By Drew Anderson & Joshua Cluff.
Senior Design Team #18 Lacey Ednoff Brianna Beconovich Jarimy Passmore Jesse Poorman.
1 CHAPTER 6 HEAT TRANSFER IN CHANNEL FLOW 6.1 Introduction (1) Laminar vs. turbulent flow transition Reynolds number is where  D tube diameter  u mean.
Last Time Where did all these equations come from?
T W DAVIES1 CONSERVATION OF MECHANICAL ENERGY FRICTIONLESS FLOW ALONG A STREAMLINE MECHANICAL ENERGY BALANCE ON A UNIT MASS OF FLUID –POTENTIAL ENERGY.
CHAPTER 3 EXACT ONE-DIMENSIONAL SOLUTIONS 3.1 Introduction  Temperature solution depends on velocity  Velocity is governed by non-linear Navier-Stokes.
Convective heat exchange within a compact heat exchanger EGEE 520 Instructor: Dr. Derek Elsworth Student: Ana Nedeljkovic-Davidovic 2005.
THERMAL ANEMOMETER MEASUREMENT The Kurz thermal anemometers use two RTDs, one heated 50 to 100’C above the ambient. The other monitors the ambient. The.
Convection: Internal Flow ( )
Heat Transfer Equations. Fouling Layers of dirt, particles, biological growth, etc. effect resistance to heat transfer We cannot predict fouling factors.
One Minute Paper Statics; reply. Fluid dynamics  Fluids in motion Pumps Fans Compressors Turbines Heat exchangers.
INTRODUCTION TO CONVECTION
Time Calculation of the Temperature Rise in an Electric Iron.
Heat Transfer Su Yongkang School of Mechanical Engineering # 1 HEAT TRANSFER CHAPTER 11 Heat Exchangers.
Bernoulli Equation – Pitot tube  Horizontal  Velocity at stagnation point is 0  Incompressible fluid  Steady state  Velocity as function of pressure.
Solar Collector Plate Collector plate 1 m wide, W=1 m Water tubes x insulation Radiation heat transfer in T Question: what will be the temperature distribution.
Heat Transfer by Convection
Heat Transfer Su Yongkang School of Mechanical Engineering # 1 HEAT TRANSFER CHAPTER 8 Internal flow.
Dr. Owen Clarkin School of Mechanical & Manufacturing Engineering Summary of Energy Topics Chapter 1: Thermodynamics / Energy Introduction Chapter 2: Systems.
Dr. Owen Clarkin School of Mechanical & Manufacturing Engineering Summary of Energy Topics Chapter 1: Thermodynamics / Energy Introduction Chapter 2: Systems.
Estimation of Maximum Temperature for Argon Gas Exiting Ullage Space in Micro-Boone K. C. Wu 11/2/11 1.
Thermodynamics. Energy Heat Heat Transfer and Equation Q = m*C*∆T – Q = Heat – m = Mass – C = Specific Heat of material – ∆T = Change in Temperature.
Heat Transfer Su Yongkang School of Mechanical Engineering # 1 HEAT TRANSFER CHAPTER 8 Internal flow.
Energy and Heat. What is Energy? When something is able to change its environment or itself, it has energy Energy is the ability to change Energy has.
First Law of Thermodynamics applied to Flow processes
MAE 5310: COMBUSTION FUNDAMENTALS
Analysis of the Simplest Flow
Conservation of Energy/Bernoulli’s Equation
Heat Transfer In Channels Flow
What are Fins ? Fins are extended surfaces used to increase the rate of heat transfer. It is made of highly conductive materials such as aluminum.
Natural Circulation and Convection
Presentation transcript:

By Jayde Kowallis and Jordan Rhoads

Introduction A copper pipe wrapped with heated tape is needed to direct blow-by gasses from the engine crank case to a centrifuge pump. Our Tube Objective: To find the length needed (L) to heat gas from 25°C to 130°C and from 190°F to 230°F.

Problem Setup: assumptions Assumptions: Heat tape creates a constant heat flux (q s ”) Tube is perfectly insulated with a fiberglass coating. (no heat is lost)

Problem Setup Conservation of energy (with perfect insulation) Using and you get Solving for L:

Solution and Procedure Known Values Properties of Air at K ρ = kg/m 3 c p = x 10 3 J/kg*K Other known values q s ” = 2055 W/m 2 mdot varies from to kg/s Inside Diameter = 1 in Case 1: T o,air = 25°C, T f,air =130°C Case 2: T o,air = 190°F, T f,air = 230°F Use the following equation to find the length of pipe for each mass flow rate using the temperatures in Case 1 and in Case 2.

Results Case 1: (T o,air = 25°C, T f,air = 130°C) For mdot = kg/s: L = 0.545m For mdot = kg/s: L = 3.079m Case 2: (T o,air = 190°F, T f,air = 230°F) For mdot = kg/s: L = 0.115m For mdot = kg/s: L = 0.545m

Conclusion and Recommendations Using this analysis and given assumptions, heating a fluid, flowing at these velocities, using a typical heat tape is a plausible solution for this application. For the majority of constant flow conditions, a recommended length of minimum m is needed to eliminate condensation.

Appendix Sources: Dr. Soloviev’s assistance in setting up the problem Fundamentals of Heat and Mass Transfer (7 th edition)