Task 5. Christopher Mack Zack Kaldy MET 330 Fluid Mechanics November 8, Purpose

Similar documents
Calculate the Costs of Piping System Elements

Fluid Mechanics. The Energy Equation [7] Dr. Mohammad N. Almasri

SEA Certified Piping Design Engineer

Hydraulics Laboratory Experiment Report

Session 2 Pump Selection. Mark Markham, P.E. Gresham, Smith and Partners September 14, 2017

Flow Test Data Book and Flow Handbook for 405 Compact Orifice Series and 1595 Conditioning Orifice Plate

VENTURI FLOW METER CALIBRATIONS SERIAL NUMBERS: , , , Prepared for. Imperial Flange and Fitting.

Piping layout for fire sprinkler system: An overview

Learning objectives. Upon successful completion of this lecture, the participants will be able to:

Stress analysis of reciprocating pump pipeline system in oil station

VENTURI FLOWMETERS. Your First Choice in Intelligent Flow Management...

SEMESTER LESSON PLANS (RPS)

SAWEA Workshop 2010 Innovative Water and Wastewater Networks Presented by Greg Welch, AECOM

Water supply components

The Integral Optimization Method of Oilfield Production System

Overview. We will not study pipe systems in detail as these are always solved with software. Wednesday, September 01, :21 PM.

Fire Protection Underground Piping. ASCE Meeting 12/17/14 Columbia, SC

GREEN THREAD Piping Systems

Section 5 - Planning Criteria. Section 5

Energetic Efficiency Analysis of Water Pumping Installations

Successfully dosing pipe networks. Kevin Sherman, Ph.D., P.E., D.WRE Vice President of Engineering Clearstream Wastewater Systems, Inc.

EXPERIMENTAL AERODYNAMICS FLOW TROUGH AN ORIFICE LAB SHEET

Screening, Definition: The unit involved is called a screen.

Pipe Stress Analysis Where Do I Start?

Pipelines. Oil & Gas Products for Transportation

DESIGN OF DUCTILE IRON PIPE ON SUPPORTS

Sag Pipe (depressed sewers, or Inverted siphons) Dr. Sataa A. Al-Bayati(10-11)

Water Utility Science Water Math and Hydraulics 050. Name: Date:

SECTION 4 - DESIGN STANDARDS FOR WATER DISTRIBUTION FACILITIES

Leachate Management Leachate Control and Collection

MICRO-HYDRO INSTALLATION SIZING Jacques Chaurette eng. January 17, 2008

David Baker Piping Technology & Products. NIA s 62nd Annual Convention Sheraton Grand at Wild Horse Pass March 29 April 1, 2017

APPENDIX G HYDRAULIC GRADE LINE

Storage Tank Piping (79720-PS-002) Stress Analysis

Variable Speed Waste Water Pumping

Where Intelligence Meets Infrastructure PA AWWA Conference

Basic Irrigation Design

HYDRAULIC DEMONSTRATION CHANNEL

Observations from Several Condition Assessments of Prestressed Concrete Cylinder Pipe used at Energy Generation Facilities

AR No. # Efficient Irrigation

Air Lift Pumps (Grit Pump) ST-027

Irrigation Rehabilitation Program Design and Construction Standards

NAU Hydraulic Testing System

AALSO Summary of Formulas needed for Levels I, II and III.

Flow Meter Calibration

The purpose of distribution system is to deliver water to consumer with appropriate quality, quantity and pressure. Distribution system is used to

Ivins City Standard Specifications for Design and Construction Part 2 Engineering and Design Standards

Gas Transmission and Distribution Piping Systems

Pumps, Turbines, and Pipe Networks. Ch 11 Young

Section 7 Hydraulic Model Development and Evaluation Criteria

CEMENT EVALUATION ITS NOT JUST ABOUT A BOND LOG GLEN BENGE SENIOR ADVISOR CEMENTING PRESSURE PUMPING

Assignment I Design of a Marine Outfall

ITEM 404 DRIVING STEEL PILING

Problems at the Cumene Production Facility, Unit 800

Bulletin No. A1300 November 1, Smith Fibercast GREEN THREAD Piping Systems

Bulletin No. A1380 September 15, Smith Fibercast CENTRICAST PLUS RB-2530 Piping Systems

NZQA registered unit standard version 4 Page 1 of 5

TRENCHLESS PIPELINE REMOVAL (TPR)

CHAPTER 12 TRICKLING FILTER PLANTS

Design and Development of Pico-hydro Generation System for Energy Storage Using Consuming Water Distributed to Houses

DIVISION 5 STORM DRAINAGE CRITERIA

Under-Tree Sprinkler Design in a Walnut/Cherry Orchard

A. This Section includes exterior piping for vertical, direct-buried, ground-loop, heat-pump systems that operate between 23 and 104 deg F.

Polyethylene Piping for Underground Fire Main Systems

RESULTS OF EXPERIMENTAL MEASUREMENTS AND CALCULATIONS OF PRESSURE LOSSES IN HD-PE PIPES. Pavel Mosler, Jan Melichar

Environmental Engineering-I

A new pipeline cleaning technology: Hydraulically Activated Power Pigging (HAPP TM )

Fluid Mechanics, Heat Transfer, Thermodynamics Design Project. Production of Ethylbenzene

GOVERNMENT POLYTECHNIC MUZAFFARPUR LAB MANUAL OF FLUID MECHANICS AND MACHINERY LAB SUBJECT CODE

Application for Underground Pipeline Crossing or Longitudinal of Railroad Property and or Track

Hydraulic Transient: Lift Irrigation Scheme

CONVEYANCE ANALYSIS OF THE MAINLINE TUNNEL USING ICAP

PIPING FLEXIBILITY & STRESS ANALYSIS COURSE DURATION: 5 DAYS

STUDY OF WATER DISTRIBUTION NETWORK USING EPANET

4A General Information A. Concept... 1 B. Conditions... 1

TYPICAL INSTALLATION INSTRUCTIONS

Index. Page numbers followed by f indicate figures.

A Guideline for Designing ASME B31 Pressure Piping Using Lokring Fittings with Elastic Strain Preload (ESP ) Technology

Fluid Mechanics, Heat Transfer, Fluid Mechanics Design Project. Production of Ethanol

Landon Carroll R. Weston Hudkins

Energy Savings through Pipe Selection A Case Study of Huntsville Utilities in Huntsville, Alabama. Rosemary Burbulis Smud 1, and Maury D.

ADDENDUM. Project: BYU-I Smith Building Chiller Replacement Project No.: Addendum No.: 1

Basic Pipe Stress Analysis Tutorial

Understanding. Hydraulics. palgrave macmillan. Les Hamill. University of Plymouth THIRD EDITION

GREEN THREAD Marine-Offshore Piping Systems. Bulletin No. C3800 May 1, 2007

COMPLETE REVISION April Process Industry Practices Piping. PIP PNC00004 Piping Stress Analysis Criteria for ASME B31.

For NGTL to file calculation of operating condition on pull back stress analysis.

AALSO Proficiency Program Level I, II & III

DESIGN OF WALL THICKNESS AND PREVENTION OF COLLAPSE OF SERVICEABLE LARGE DIAMETER PIPELINES. Lucksyn Avuwha Omidih and Godspower O.

Vortex Filters. Conservation Technology

Simulation of Pipes by Aspen Plus

CFD Analysis of Clarifier Performance With and Without Energy Dissipating Inlet

Bulletin No. A1200 May 15, Smith Fibercast RED THREAD II Piping Systems

Nodal Analysis Approach in Minimizing Pressure Losses to Improve Well Productivity

Copper Micro-channel Loop Thermosyphon. A thesis presented to. the faculty of. the Russ College of Engineering and Technology of Ohio University

BOSfluids. The Flow Simulation Tool of Choice. Services Introduction Input, Output, and Analysis Features Features and Example System and Training

Chilled Water Distribution Systems. APPA Institute for Facilities Management New Orleans, LA January 19, 2016

PART II: Metal Casting Processes and Equipment

FlowSet. Balancing Procedure

DESIGN OF SEWER SYSTEMS

Transcription:

Purpose Task 5 Christopher Mack Zack Kaldy MET 330 Fluid Mechanics November 8, 2015 For the fifth task of this project we are asked to specify the layout of the piping system, the material type and sizes of all pipes, and the lengths required each pipe. Drawings & Diagrams Sources Class Textbook Design Considerations The exit of the truck/entrance of the first pipe segment is located four feet above ground level. The first pipe segment is run four feet underground then hits a 90 elbow and continues until it reaches the clean storage holding tank. The exit for the last pipe segment into the truck is located about thirteen feet above ground level. Data & Variables Branch I flow rate = 0.3713 ft^3/s Branch II flow rate =. 0.0743 ft^3/s Branch III flow rate = 0.4827 ft^3/s Branch IV flow rate = 0.1485 ft^3/s Velocity Criterion = 9.48 ft/s Kinematic viscosity = 2.505*10^-5 ft^2/s Materials Commercial Steel Procedure Calculations..

Christopher Mack Zack Kaldy MET 330 Fluid Mechanics November 8, 2015 Summary Pipe material: Commercial Steel Pipe Lengths: Branch I: 578 ft. 10 in. Branch II: 60 ft. 1 in. Branch III: 440 ft. 7 in. Branch IV: 40 ft. Pipe Diameters: Branch I: 0.2058 ft. Branch II: 0.1150 ft. Branch III: 0.2557 ft. Branch IV: 0.1723 ft. Analysis If the exit nozzle on the train has a limited size, our flow rate then becomes limited as well which would inhibit the time it takes to fill Tank one. We created a spreadsheet that can calculate friction factors

Purpose Task 6 Christopher*Mack** Zack*Kaldy* MET*330*Fluid*Mechanics** November*8,*2015* The purpose of this task is to specify the number, types, material, and size of all valves, elbows, and fittings. Drawings & Diagrams Sources. Class Textbook Design Considerations The fluid is already held in the train tanker and will be released via a valve that is attached to the train. Gate valves were added before and after pumps for maintenance purposes. Data & Variables Gate valve resistance coefficient = 8*f_t 90 elbow resistance coefficient= 30*f_t Roughness of commercial steel = 1.5*10^-4 ft. Materials Commercial steel 90 elbows Gate valves Procedure Calculations Summary. We will be using 2 2½ in. NPS Gate valves (Branch II)

1 4 in. NPS Gate valve (Branch III) 2 3 in. NPS Gate valves (Branch IV) 2 8 in. NPS 90 elbows 1 2½ in. NPS 90 elbow 2 4 in. NPS 90 elbows 2 3 in. NPS 90 elbows Christopher*Mack** Zack*Kaldy* MET*330*Fluid*Mechanics** November*8,*2015* Analysis After applying Bernoulli's equation to our four series pipeline system, we were able to determine pipe sizes and pump head requirements. Using these pipe sizes we determined the size and amount of elbows, gate valves and fittings required. Since this was done with numerical analysis we will have to determine the best fitting pumps for our systems and depending on these pumps specifications our pipe sizes may change.

Purpose Task 7 Christopher Mack Zack Kaldy MET 330 Fluid Mechanics November 8, 2015 The purpose of task seven is to include the hydraulic analysis of all parts of the system, including energy losses due to friction and minor losses. Drawings & Diagrams Sources Class textbook Design Considerations We are considering energy losses due to pipe elbows, valves and friction. Data & Variables Materials Procedure Calculations Summary Specific Gravity of fluid = 0.94 Viscosity/Vapor pressure = 1.5x that of water Velocity Criterion= 9.84 ft/s Three pumps Four Gate valves Six 90 elbows. Pipe Flow Rates: Branch I flow rate = 0.3713 ft^3/s Branch II flow rate =. 0.0743 ft^3/s Branch III flow rate = 0.4827 ft^3/s

Branch IV flow rate = 0.1485 ft^3/s Christopher Mack Zack Kaldy MET 330 Fluid Mechanics November 8, 2015 Pipe Velocities: Branch I velocity = 11.16 ft/s Branch II velocity = 7.153 ft/s Branch III velocity = 2.029 ft/s Branch IV velocity = 6.369 ft/s Pipe Lengths: Branch I: 578 ft. 10 in. Branch II: 60 ft. 1 in. Branch III: 440 ft. 7 in. Branch IV: 40 ft. Pipe Diameters: Branch I: 0.2058 ft. Branch II: 0.1150 ft. Branch III: 0.2557 ft. Branch IV: 0.1723 ft. Pipe Friction Factors: Branch I: o F1 = 0.0244 o F_t = 0.014 Branch II: o F2 = 0.028 o F_t = 0.0182 Branch III: o F3 = 0.0209 o F_t = 0.0173 Branch IV: o F4 = 0.0243 o F_t = 0.019 Analysis After applying Bernoulli s to our four pipeline systems, we were able to determine the latter values based off of whether the system was pumped or gravity driven. If the flow rate of any one system changes the pipe diameter will either increase or decrease.

Purpose Task 8 Christopher Mack Zack Kaldy MET 330 Fluid Mechanics November 8, 2015 Specify pipe wall thickness (schedule). Drawings & Diagrams Sources Class textbook http://www.engineeringtoolbox.com/temperature-allowable-stresses-pipesd_1338.html Design Considerations Branch I has the highest pressure Data & Variables Design pressure = 8 psig Allowable stress = 15,000 psi Pipe outside diameter = 8.625 in. Longitudinal joint quality factor = 0.85 Correction factor based on material type and temperature = 0.4 Materials Procedure Calculations Summary Pipe material: Schedule 40 Commercial Steel Calculated thickness = 0.0027 in. Therefore the Schedule 40 pipe thickness of 0.322 in. will be more than enough.

Christopher Mack Zack Kaldy MET 330 Fluid Mechanics November 8, 2015 Analysis Because our highest pressure is seen in branch I we know Schedule 40 pipes will work throughout the plant.

Purpose: Task 9 Christopher Mack Zack Kaldy MET 330 Fluid Mechanics November 8, 2015 The purpose of task nine is to determine the requirements of each pump (i.e. pump head and flow rate), and determine how many pumps are needed. Drawings & Diagrams Sources Class textbook Design Considerations Two valves were placed on each pump in order to aid in the maintenance process. The pumps will be buried beside the tanks to avoid water hammer. Data & Variables Pipe material: Commercial Steel Pipe Lengths: Branch I: 578 ft. 10 in. Branch II: 60 ft. 1 in. Branch III: 440 ft. 7 in. Branch IV: 40 ft. Pipe Diameters: Branch I: 0.2058 ft. Branch II: 0.1150 ft. Branch III: 0.2557 ft. Branch IV: 0.1723 ft. Velocity Criterion = 9.84 ft/s Gate valve resistance coefficient = 8*f_t 90 elbow resistance coefficient= 30*f_t Roughness of commercial steel = 1.5*10^-4 ft. Materials Commercial steel 90 elbows

Gate valves Christopher Mack Zack Kaldy MET 330 Fluid Mechanics November 8, 2015 Procedure Calculations Summary Two pumps are needed. Pump I: 2 2½ in. NPS Gate valves (Branch II) Energy loss due to friction = 13.06 ft. h_a = 38.14 ft. Branch II flow rate =. 0.0743 ft^3/s Pump II: 2 3 in. NPS Gate valves (Branch IV) Energy loss due to friction = 5.4 ft h_a = 34.03 ft Branch IV flow rate = 0.1485 ft^3/s Analysis Since the pumps are buried next to the tanks at a distance of five feet, there may be water hammer issues. If these issues turn up we may have to change pipe lengths to compensate.