ABSTRACT The flow measuring apparatus is designed to study which the most preferable flow meter from different typical methods of measuring the discharge of an incompressible fluid. This can be identify by measuring the flow rate and the head loss with later to be compared to the different flow meter which is venture meter, orifice meter and rotameter. INTRODUCTION The objectives of this experiment are to demonstrate the characteristics of some various commonly used methods of measuring fluid flow
Table of Contents Abstract 1 1.0 Introduction 2 2.0 Experimental Design 3 2.1 Diagram of Experiment 3 2.2 Methods 4 2.3 Procedure 4 3.0 Results & Discussion 5 3.1 Table of Results 5 3.2 Discussion 6 4.0 Conclusion 8 References 9 ABSTRACT The purpose of this experiment is to investigate the flow rate/discharge and the head loss of 3 particular flow measuring apparatus which are the Venturi Meter, Orifice Meter and Rota Meter in accordance to Bernoulli’s Equation
Byline Report Section | Author Introduction & Theory | Author Apparatus and Operating Procedures | Author Results and Discussion | Author References and Appendix | Experiment I | Tricia Heitmann | Alex Long | William Kwendi | Khanh Ho | Experiment II | Alex Long | William Kwendi | Khanh Ho | Tricia Heitmann | Experiment V | William Kwendi | Khanh Ho | Tricia Heitmann | Alex Long | April 29, 2013 Dr. Nollert The University of Oklahoma Department of Chemical, Biological and Materials
and debris in pipes. 1. Introduction Because of safety circumstances, it is very important to control pressure loss through pipes in order to ensure a process plant to operate in a safe way. To design a safe plant operation, pressure loss across the process plant should be taken into account and it can be manageable by making changes in flowrate of the fluid. The aims of this experiment are to measure pressure drop across different pipes,fittings, venturi meter and orifice plate, to figure out momentum
Date of Experiment : 16th March 2006 Table of Contents Page Summary 2 Part I: Flow Measurement in Closed Conduit A. Introduction 3 B. Objectives 3 C. Theoretical Background 4 D. Experimental Procedures 9 E. Results and Calculations 12 F. Discussion 50 G. Error Analysis 58 H. Conclusion 61 Part II: Centrifugal Pump Characteristics I. Introduction 62 J. Objectives 63 K. Theoretical Background 63 L. Experimental Procedures 68 M. Safety Precautions 68 N. Results and Calculations
Group : Th1 Date of Experiment : 16th March 2006 Table of Contents Page Summary 2 Part I: Flow Measurement in Closed Conduit A. Introduction 3 B. Objectives 3 C. Theoretical Background 4 D. Experimental Procedures 9 E. Results and Calculations 12 F. Discussion 50 G. Error Analysis 58 H. Conclusion 61 Part II: Centrifugal Pump Characteristics I. Introduction 62 J. Objectives 63 K. Theoretical Background 63 L. Experimental Procedures 68 M. Safety Precautions 68 N. Results and Calculations 69
EXPERIMENTAL SETUP & PROCEDURE 5.1 INTRODUCTION The details of the experimental set up are presented in this chapter and the alternations made to the instrumentation are also described .The experimental setup is fabricated to fulfill the objective of the present work. The various components of the experimental set up including modification are presented in this chapter. 5.2 EXPERIMENTAL SET UP The experimental set up consists of engine, an alternator, and electrical load system, fuel tank, Fig5
both turbulent laminar for that day because of the accident that took place and because midway through our turbulent trials we realized that our calculations for the target orifice pressure drop were wrong. During the second lab period, we were able to finish all 15 of our turbulent flow trials with the adjusted target orifice pressure values, we were also able to finish the remaining 10 laminar flow trials, as well as record the density and viscosity values for both water and propylene glycol over
Ltd. INDEX 1. INTRODUCTION TO BARH STPP 2. KEY DATA 3. BRIEF SYSTEM DESCRIPTION AND GENERAL INFORMATION 4. 400/132 KV switchyard 5. Transformers 6. 11 & 3.3 KV SWITCHGEAR TO BE INSTALLED IN THE PLANT 7. TECHNICAL PARAMETERS & DETAILS OF SWITCHGEAR USED IN BARH STPP 8. 11KV MISCELLANEOUS SWITCHGEAR (UNDER TESTING) 9. COMMISIONING CHECKS/TESTS 10. MAJOR PROTECTIONS USED IN THE SWITCHGEAR 11. CONCLUSION INTRODUCTION Location :- The project site
SUBMISSION: 5/11/2011 MARK/20 (for demonstrator use): Introduction Aim: 1. Describe operation of various types of valves 2. Measure frictional losses due to flows through different valves 3. Identify sources of errors Background & theory: In this experiment, the relationship between volumetric flow rate and percentages of valve opening is determined by knowing that volumetric of flow rate of air through the flow meter is proportional to the square root of the differential head across