Irrigation Design and Heat Exchanger Design

Slides:



Advertisements
Similar presentations
ME 414 Design Project Heat Exchanger Design Created and Designed by:
Advertisements

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.
Fluid Mechanics.
The Bernoulli Equation - Work and Energy
Shell and Tube Heat Exchanger October 7, 2003 Cycle 2 Group 1A Frank Fadenholz Jennifer Fadenholz Christian Woods Angel Taylor.
Convection in Flat Plate Turbulent Boundary Layers P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi An Extra Effect For.
ME421 Heat Exchanger and Steam Generator Design Lecture Notes 7 Part 1 Shell-and-Tube Heat Exchangers.
Kern’s Description of Shell Side Flow in SHELL-AND-TUBE HEAT EXCHANGER P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Another.
Heat Exchange Design and Optimization Project Presented: May 6 th, 2010 Professor: Mr. Toksoy Group Members: Nathan Dart Andrew Kinney Paul Thompson Joe.
Heating and Air Conditioning I
 A 'heat exchanger' may be defined as an equipment which transfers the energy from a hot fluid to a cold fluid. Here, the process of heating or cooling.
Kern Method of SHELL-AND-TUBE HEAT EXCHANGER Analysis
Closure of Kern’s Method
Kern’s Description of Shell Side Flow in SHELL-AND-TUBE HEAT EXCHANGER
SHELL-AND-TUBE HEAT EXCHANGERS
Actual Shell Side Pressure Drop : Bell-Delaware Method
Kern Method of SHELL-AND-TUBE HEAT EXCHANGER Analysis
Installing & Maintaining Irrigation Systems Ms. Gripshover Landscaping Unit 15.
Hydraulic Analysis of STHE Using Bell Delaware Method
Results of Kern Method Basic Kinematic Details Group No. Tube Side Velocity (m/s) Number of Tubes Shell Diameter length STHX (m) Ds/L
Basic Hydraulics Irrigation.
Thermo-economic Optimization of STHE P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Minimizing capital and operating costs of shell.
ME421 Heat Exchanger and Steam Generator Design
THERMAL ANALYSIS OF SHELL AND TUBE HEAT EXCHANGER
Shell and Tube Heat Exchangers
2006 Oct. 19 DES Project -- Vaidas Simaitis, University of Illinois1 DHE – Detector Head Electronics Monsoon 80mm Crate Heat Load.
I RRIGATION S YSTEM ME 414: Team 4 Chris Cook Matt Griffey Jason Colgan Breanne Walters Jeremy Johnson.
Group 3: Seong Won Byun Jakob Combs Zachary Lightner Bart Sudhoff Devin Templeton.
MER Design of Thermal Fluid Systems Pumps and Fans Professor Anderson Spring Term
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…..
Applied Max and Min Problems Objective: To use the methods of this chapter to solve applied optimization problems.
Water piping design.
FEASIBILITY OF COMPONENTS CLARA ECHAVARRIA & JONATHON LOCKE.
ME421 Heat Exchanger and Steam Generator Design Lecture Notes 6 Double-Pipe Heat Exchangers.
ME 414 – TEAM #1 JENNIFER HACKER JESSE KENDALL CHRISTOPHER ROGERS BRANDON RODRIGUEZ ALEK VANLUCHENE Heat Exchanger Design.
Applied Max and Min Problems
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.
Senior Design Team #18 Lacey Ednoff Brianna Beconovich Jarimy Passmore Jesse Poorman.
Design Formulae for Mingled Shell-side stream P M V Subbarao Professor Mechanical Engineering Department I I T Delhi A Confluence Model for A Circuitous.
ME414 Spring 2006 Design Project 2 Heat Exchanger Ugo Anyoarah Osinanna Okonkwo Vinay Prisad Daniel Reed.
The Family of Shell and Tube Heat Exchangers P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Family members with Simple Geometrical.
Design Project 1 Equalized Velocity for Automobile Climate Control Rodger Stowe Amber Russell Kevin Feeley Kreischer Davis Tom Filipucci.
ME 414 Thermal / Fluid System Design Heat Exchanger Project Professor: John Toksoy 12/13/05 Team Members: Chester Bennett Wilton Green Scott Guttman Nick.
ME T HERMAL F LUID S YSTEM D ESIGNS Heat Exchanger Final Project.
Lesson 23 HEAD LOSS DEFINE the terms head loss, frictional loss, and minor losses. DETERMINE friction factors for various flow situations using the Moody.
Sizing Variable Flow Piping – An Opportunity for Reducing Energy
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.
Equipment Design Designed by Eman A. Khajah. Outline Design of Heater. Design of Stripper.
Project 2: Heat Exchanger Design Group Members: Brian Schludecker Phillip Palmer Adam Spindler Mike Hay Joe McGuire Presented 12/12/2006 to Dr. Toksoy.
Design of Heat Exchangers
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.
Step One The first step to designing a sprinkler system is to create a diagram of the area you wish to irrigate.
Heat Exchanger Design Cooler E-100 Heater E-108.
Step One The first step to designing a sprinkler system is to create a diagram of the area you wish to irrigate.
IRRIGATION SYSTEMS. OBJECTIVES 1. Describe irrigation & its purpose 2. Explain preparation for irrigation systems 3. Calculate GPM 4. Identify & explain.
CHEMCAD Seminar Heat Transfer John Edwards, P&I Design Ltd
Purdue School of Engineering and Technology
HEAT EXCHANGER DESIGNPROJECT ME 414 Thermal Fluid System Design
By: Brittany Watton & Jeff Philippart
Purdue School of Engineering and Technology
Heat Exchanger Design Optimization
2018 SHADE Conference “Fundamentals (Keys) of Basic Irrigation Design”
Heat-transfer Equipment
Heat Exchangers Heat Exchangers.
SHELL-AND-TUBE HEAT EXCHANGERS
P M V Subbarao Professor Mechanical Engineering Department I I T Delhi
Presentation transcript:

Irrigation Design and Heat Exchanger Design Department of Mechanical Engineering, IUPUI Me 414 Thermal-Fluid Design Fall 2007 Irrigation Design and Heat Exchanger Design Neil Barnes Thomas Hylton Lalit Kumar Manan Langalia Matt Zwiesler

Objective Design an efficient irrigation system for a given yard Calculate and minimize utility and all other costs Minimize wasted water Calculate time to deliver one inch of water to the entire yard

Choosing a Sprinkler Head Chosen based on size, type of spray, and cost Need to spray in a generally uniformed and controlled area Spray, over-spray, and wasted water needs to be taken into account

Head Placement in Yard 35’ radius heads were impact/ratchet heads Poor design because low overlap and high cost sprinkler heads Based on the tutorial ratchet along with spray heads is not recommended

Head Placement in Yard Design using 24’, 18’, and rectangular heads Ruled out because of the pricing difference Price difference between this and chosen design: $450.00

Head Placement in Yard Chosen to reduce costs Only two different sprinkler heads (rectangular and 18’ head)

Square Head Decision Chosen as a result of less wasted water Square spray heads would spray with uniform coverage and would not need to overlap 8 heads spaced uniformly in rectangular strip of yard Toro 570 4x30’ Center Strip Nozzle

Piping Layout Reduce materials, bends, and joints Sprinkler heads in each row in series and each row is in parallel Parallel allows equal pressure loss in each branch of pipe with constant flow rate Series allows equal flow rates in each branch, but pressure changes in each branch Parallel allows for easy cleaning if blockages occur

Bill of Materials Part Individual Cost Quantity Total Cost 4" Sprayer - 1804P Rainbird (18') $2.50 52 $130.00 Rainbird Nozzle $1.20 $62.40 Toro 4x30 Nozzle (rectangular center strip) $1.10 8 $8.80 Toro Sprayer for 4x30 Nozzle $1.99 $15.92 Wilkins Backflow Preventer $61.80 1 Rainbird DV Series Valve $13.97 4 $55.88 ESP Indoor Controller $84.95 PVC (pressure pipe) $0.94/10 ft 1500 ft $141.00 PVC elbow $0.23 12 $2.76 PVC Tees 68 $15.64 Total $579.15 Comparison Rainbird Rotor Sprinkler (24') $18.35 35 $642.25

AFT 1st Iteration (No zones) High flow rates Not enough pressure

AFT 2nd Iteration (2 zones)

AFT 3rd Iteration (4 zones)

ZONE 1 of 4

Final Results

Project 2 Heat Exchanger Design

Design Requirements Remove 1.2 MW of heat from process water Inlet temperature 90 ◦C Exit temperature 40 ◦C City water Inlet temperature during summer is 25 C Minimize tube side and shell side pressure drops Minimize cost due to weight and material used Minimize the heat exchanger volume

Design Process DOE analysis with Matlab and Minitab Optimization Initial DOE Eliminate insignificant factors-down to 12 variables Learn effects of change in variables Final DOE Four most significant variables chosen based on effect seen in main effects plots Optimization Four variables analyzed Design goals met with optimal values

DOE process Run 2 sets of 6 initially All variables related to effects on output variables: Weight of HE Shell-Side DP Tube-Side DP Q, heat transfer List of final four variables: Tube OD Baffle Space Tube Length Shell ID

Main Effects Plots DP Tube Plot Q Calculated Plot

Main Effects Plots DP Shell Plot Weight Plot

Optimization Pareto charts of Q and Weight Minitab statistically equates effects of variables and interactions Used to confirm main effects plots

Optimization Plots Initial optimization with custom tube od required Final optimization with standard tube od

Results Critical Variables Value Baffle Space 0.50 m Shell Inner Diameter 0.3048 12” Tube Outer Diameter 0.0111 m 7/16” Tube Length 4.545 m Critical System Characteristics Value Heat Transfer Rate 1.2e6 W Overall System Weight 381.69 kg Tube-side Pressure Drop 438.955 Pa Shell-Side Pressure Drop 3623.99 Pa

Summary Success Met 1.2 MW requirement Weight minimized DP shell-side and tube-side minimized

Questions? ?