Group 3: Seong Won Byun Jakob Combs Zachary Lightner Bart Sudhoff Devin Templeton.

Slides:



Advertisements
Similar presentations
Heat Loss Calculator for a Stainless Steel Complex Pipe System By: Thomas Morris & Jacob Hannon.
Advertisements

ME 414 Design Project Heat Exchanger Design Created and Designed by:
Hydraulic.
Objectives Heat transfer Convection Radiation Fluid dynamics Review Bernoulli equation flow in pipes, ducts, pitot tube.
Heat Exchanger Design Thermal / Fluid System Design Final Project Department of Mechanical Engineering Fall 2005 December 13, 2005 Team Members: Andrew.
ME 414- FLUID SYSTEMS DESIGN PROFESSOR: JOHN TOKSOY SPRING 2009 TEAM Tyler Laughlin Denis Shkurapet Ethan Sneed Matt Tolentino Tyler Turk Heat Exchanger.
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.
Conduction & Convection Quiz 9 – TIME IS UP!!! A flat furnace wall is constructed with a 4.5-inch layer of refractory brick (k = Btu/ft·h·
Convection in Flat Plate Turbulent Boundary Layers P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi An Extra Effect For.
Estimation of Convective Heat Transfer Coefficient
Lesson 14 Jet Bit Nozzle Size Selection
Chapter 4.2: Flow Across a Tube Bundle Heat Exchanger (Tube Bank)
Heat Exchange Design and Optimization Project Presented: May 6 th, 2010 Professor: Mr. Toksoy Group Members: Nathan Dart Andrew Kinney Paul Thompson Joe.
Pipeline Hydraulics.
Experiment : 5/03/2012 Presentation : 12/03/2012 Group B1/B Vartak Shankul Shisheer 10D Abhishek Mathur 10D Kunal Bhoyar 10D
Types of Heat Exchangers
Internal Convection: Fully Developed Flow
Internal Flow: Heat Transfer Correlations
First Wall Thermal Hydraulics Analysis El-Sayed Mogahed Fusion Technology Institute The University of Wisconsin With input from S. Malang, M. Sawan, I.
Kern Method of SHELL-AND-TUBE HEAT EXCHANGER Analysis
Heat Exchangers with Cross Flow past Cylinders P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Another Common Industrial Application!!!
LINEAR SECOND ORDER ORDINARY DIFFERENTIAL EQUATIONS
Kern Method of SHELL-AND-TUBE HEAT EXCHANGER Analysis
Basic Hydraulics Irrigation.
Rotary Sprinklers – uniform application over entire area – lawns.
THERMAL ANALYSIS OF SHELL AND TUBE HEAT EXCHANGER
I RRIGATION S YSTEM ME 414: Team 4 Chris Cook Matt Griffey Jason Colgan Breanne Walters Jeremy Johnson.
Specifying and Sizing Control Valves A design equation used for sizing control valves relates valve lift to the actual flow rate q by means of the valve.
Supervised by : Dr. mohammad fahim Eng. Yousef ali Yaqoub bader ali.
Exergy Analysis of STHE P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Formalization of Thermo-economics…..
FEASIBILITY OF COMPONENTS CLARA ECHAVARRIA & JONATHON LOCKE.
ME 414 – TEAM #1 JENNIFER HACKER JESSE KENDALL CHRISTOPHER ROGERS BRANDON RODRIGUEZ ALEK VANLUCHENE Heat Exchanger Design.
Group 17 Oceanic Thermal Energy Conversion Model - Lockheed Martin 1 Oceanic Thermal Energy Conversions Group Members: Brooks Collins Kirby Little Chris.
ME 414 : Project 1 Heating System for NASA North Pole Project Team Members Alan Benedict Jeffrey Jones Laura O’Hair Aaron Randall May 5, 2006.
1 Calorimeter Thermal Analysis with Increased Heat Loads September 28, 2009.
SHELL AND TUBE HEAT EXCHANGER
Senior Design Team #18 Lacey Ednoff Brianna Beconovich Jarimy Passmore Jesse Poorman.
Irrigation Design and Heat Exchanger Design
ME414 Spring 2006 Design Project 2 Heat Exchanger Ugo Anyoarah Osinanna Okonkwo Vinay Prisad Daniel Reed.
Design Project 1 Equalized Velocity for Automobile Climate Control Rodger Stowe Amber Russell Kevin Feeley Kreischer Davis Tom Filipucci.
Condensation and Boiling Heat Transfer Source: Vishwas V. Wadekar, HTFS, Aspen Technology J.P. Holman boiling, condensation : high heat transfer rates.
ME 414 Thermal / Fluid System Design Heat Exchanger Project Professor: John Toksoy 12/13/05 Team Members: Chester Bennett Wilton Green Scott Guttman Nick.
NRCS -IWM II 1 IWM I APPLICATION VOLUME CALCULATIONS.
ME T HERMAL F LUID S YSTEM D ESIGNS Heat Exchanger Final Project.
ME 414 Project 2 Heat Exchanger Design Date: - May 6, 2009 Instructor: - John Toksoy Member: - Rahul Patel Hesam Nouri Atoosa Solhkonan Juan Tapia.
Jim Hahn Kelly McCormick Jeff Snyder Andrew Taylor Nathan Wagers ME 414: Thermal/Fluid Systems.
Available Water Flow Meter Size Typical flow depending on size
Project 2: Heat Exchanger Design Group Members: Brian Schludecker Phillip Palmer Adam Spindler Mike Hay Joe McGuire Presented 12/12/2006 to Dr. Toksoy.
ME 414 Thermal&Fluid Systems Design Heat Exchanger Design ME 414 Thermal / Fluid System Design William Donelson Josh Fosso Laurie Klank Jonathan Moore.
Design of an Automobile Cabin Ventilation System Krista Cowan John Fearncombe Nathaniel Greene Brad Holtsclaw Katie Iaizzo ME 414: Thermal Fluid System.
Internal Flow: Heat Transfer Correlations. Fully Developed Flow Laminar Flow in a Circular Tube: The local Nusselt number is a constant throughout the.
Step One The first step to designing a sprinkler system is to create a diagram of the area you wish to irrigate.
Friction Loss Tutorial Used in conjunction with the Friction Loss Check Sheet and any Irrigation Plan.
Step One The first step to designing a sprinkler system is to create a diagram of the area you wish to irrigate.
Exercises for Q1. Insulated copper tube A thin walled 10 mm copper tube is used to transport a low-temperature refrigerant with a temperature that is.
Lesson 19: Process Characteristics- 1 st Order Lag & Dead-Time Processes ET 438a Automatic Control Systems Technology lesson19et438a.pptx 1.
Internal Flow: Heat Transfer Correlations Chapter 8 Sections 8.4 through 8.8.
Internal Flow: Heat Transfer Correlations
DESIGN OF SHELL AND TUBE HEAT EXCHANGER
Purdue School of Engineering and Technology
SAMPLE PROBLEM MATRA Input Preparation
By: Brittany Watton & Jeff Philippart
Purdue School of Engineering and Technology
Heat Transfer Coefficients
Heat Exchanger Design Optimization
2018 SHADE Conference “Fundamentals (Keys) of Basic Irrigation Design”
Fundamentals of Convection
Natural Convection New terms Volumetric thermal expansion coefficient
Heat-transfer Equipment
Internal Flow: Heat Transfer Correlations Chapter 8 Sections 8.4 through 8.8.
Presentation transcript:

Group 3: Seong Won Byun Jakob Combs Zachary Lightner Bart Sudhoff Devin Templeton

Objective  Provide 1 inch of water to an area of 13,460ft 2 in the shortest time  Least amount of water falling outside the property  Minimize cost of materials  Minimize electric utility costs

Layout

 Large area used 30- foot radius sprinkler heads  Smaller areas used combination of 18 and 17-foot radius sprinkler heads

Layout  Sprinkler head locations  Circles are 30-foot radius  Outside corners are 270° rotors  Corners and boundary edges are 90° and 180° rotors  All others are 360° rotors

Pipe Layout & AFT Model Pipe Layout for Zone 1Pipe Layout for Zone 2Pipe Layout for Zone 3Sprinkler GPM for Zone 1Sprinkler GPM for Zone 2Sprinkler GPM for Zone 3

Sprinkler Parameters  Pressure difference across the component is [Equation 1]  The k-loss value is [Equation 2]

Table 2: Required Flow Rate and Time to Water for Each Zone Zone Area to be Covered (ft2) Water Needed for 1” depth (gal) Volumetric Flow Rate (gal/min) Time to Water (mins) TOTAL Project Results

Cost Analysis

 Largest cost in the project is the rotor sprinkler heads.  Another major factor for cost is the diameter of pipe.

Summary Project Outcomes:  56 Sprinkler Heads  Total Material Cost: $1154  192 Minutes to Water

References [1] Toksoy, John M., “Sprinkler Project Description”, Microsoft PowerPoint Presentation. Fall [2] Smajstrla, A.G., Zazueta, F.S. and Haman, D.Z., “Lawn Sprinkler Selection”, Accessed on November 2, [3] Hunter Industries, “I10/I20 Ultra Rotary Sprinklers”, Accessed on November 12, [4] Stryker, Jess. “Irrigation Tutorials”. Accessed on November 12, [5] Sprinkler Warehouse. Accessed on November 12, [6] US Plastics. Accessed on November 12, [7] McMaster-Carr. Accessed on November 12,

Updates to MATLAB Program Removed calculations from HE_Design_Input Tube ID, Tube Pitch, Number of Tubes Number of tubes when running DOE file Added Nusselt correlations for both shell and tube side Added more materials Entire program can be run from HE_Design_Main

Fixed Parameters

First Design of Experiments

Main Effects for First DOE

Second Design of Experiments

Main Effects for Second DOE

Reduction of Variables Eliminate: Tube OD Shell ID Tube Thickness Lowest Weight Configuration Possible

Final Design of Experiments

PARETO Plots for Final DOE

Minitab Optimization Results

Manual Optimization Results FINAL RESULTS

Heat Transfer Coefficients * Toksoy, “Convection Heat Transfer” TFD-HE2, pg. 9 * Gnielinski for Turbulent Flow, 2300 < Re < 5x10 6 * JP Holman, “Heat Transfer” 2002, For Turbulent Flow: C=0.386, n=0.592

Tube Thickness Calculate maximum allowable pressure:

Shell Thickness

Final Input Parameters * Correlations added by design group

Questions?