CHAPTER 2 EXPERIMENTAL SETUP AND PROCEDURE
|
|
- Rolf Briggs
- 5 years ago
- Views:
Transcription
1 22 CHAPTER 2 EXPERIMENTAL SETUP AND PROCEDURE 2.1 EXPERIMENTAL COLUMN All the experiments were carried out in an internal loop airlift fluidized bed and combined loop fluidized bed (an external down comer connected at the top and bottom of the column), made of perspex column with 0.15 m inner diameter, 1.63 m height, with a flat bottom and draft tube 1.54 m in height with m diameter. The external down comer was 0.98 m in height with 0.03 m in diameter. The diameter of the gas-liquid separator was 0.30 m. Figures 2.1 and 2.2 show the schematic diagram of internal loop airlift fluidized bed and combined loop airlift fluidized bed respectively. Figure 2.3 shows the photographic view of experimental setup used in the present study Internal loop airlift fluidized bed consisted of concentric tube and was comprised of different zones such as riser, gas - liquid separator and down comer. The air was sparged through the riser. From the riser gas went to the gas - liquid separator where part or whole gas bubbles were removed. The part of liquid from the separator moved to the internal down comer. The bulk density difference between the riser and down comer caused the liquid to flow, thus the liquid re-entered into the riser; the liquid phase circulates continuously around the loop. In combined loop configuration the liquid from the disengagement section went through the internal down comer as well as external down comer. The bottom clearance between draft tube and gas
2 23 distributor was 0.09 m and the top clearance between the free-gas liquid level and the draft tube was 0.12 m. Air was sparged through triangular pitch sparger which was 0.08 m in diameter with 180 holes of m diameter each located slightly below the perforated plate. Liquid from the storage tank was pumped into the column using a centrifugal pump and flow rate was measured by calibrated rotameters with an accuracy of 2%. Air was fed to the column through a pressure regulating valve by an oil free compressor. The flow rate of gas was measured and controlled by using gas rotameters with an accuracy of 2 %. Superficial gas and liquid velocities were calculated based on the column diameter. Ball valves were used for simultaneous opening and closing of both air and liquid lines. The densities of the liquids were measured with a specific gravity bottle and the rheological properties of non-newtonian liquids were measured by using Brookfiled Rheometer (Model LVDV-II+). Superficial liquid velocities were varied from m s -1 to 0.12 m s -1. Superficial gas velocities were varied from x 10-3 m s -1 to x 10-3 m s -1.
3 d c Degassing zone 2. Riser 3. Downcomer 4. Perforated plate 5. Sparger 6. Pressure taps 7. Manometer 8. Gas rotameter 9. Compressor 10. Liquid rotameter 11. Liquid pump 12. Liquid storage tank Figure 2.1 Schematic diagram of internal loop airlift fluidized bed
4 d c Degassing zone 2. Riser 3. Downcomer 4. Perforated plate 5. Sparger 6. Pressure taps 7. Manometer 8. Gas rotameter 9. Compressor 10. Liquid rotameter 11. Liquid pump 12. Liquid storage tank 13. External downcomer Figure 2.2 Schematic diagram of combined loop airlift fluidized bed
5 26 Figure 2.3 Photograph of the experimental setup 2.2 COLUMN OPERATION Initially the column was filled with liquid and then the selected solid particles were dropped into the column one by one. After the column was filled to desired height, air and liquid were introduced into the column. The experiments were carried out by increasing the liquid flow rate in the column by keeping the gas at a constant flow rate. After attaining a steady state, the pressure drop was measured and then the air and liquid flow rates were suddenly stopped by closing the valves simultaneously and the column was disconnected from the air and liquid feed lines and the gas holdup and liquid holdup were measured. After covering the desired range in liquid flow rates, the air flow rate was changed to the next higher value and the experiments were repeated. This procedure was continued to cover a wide range of the liquid and gas flow rates. Volume displacement method was used to measure the gas holdup (Nacef et al 1992 and Miura et al 2001). The liquid
6 27 holdup was measured by calculating the volume of the liquid available in the column to the total volume of the column and minimum fluidization velocity was determined by visual measurement (Koide et al 1983 and Zhang et al 1995) and compared with pressure drop method (Koide et al 1983). 2.3 SYSTEMS USED In the present work, water, 5% n-butanol and various concentrations of commercial grade glycerol (60% and 80%) were used as Newtonian fluids (and different concentrations of carboxy methyl cellulose (0.25%, 0.6% and 1.0%) were used as non-newtonian liquids. Different diameters of spheres, Bearl saddles and Raschig rings were used as solid phases. All the experiments were carried out in an atmospheric temperature with oil free compressed air as gas phase. After attaining the steady state, readings were taken and the error was found to be less than ± 3%. A minimum of 3-5 readings were taken and the average value was used for calculations. The properties of solid particles and liquids used in the present study are given in Tables 2.1 and 2.2. Table 2.1 Properties of solid particles used in the present study Sl.No Particle description Size, dp, m Density, kg m -3 p Sphericity 1 Spheres Spheres Spheres Spheres Spheres Spheres Spheres Bearl saddle Bearl saddle Raschig ring Raschig ring
7 28 Table 2.2 Properties of liquids used in the present study Density of Surface Viscosity Type of liquids liquids,( L ) kg m -3 tension L ) N m -1 K kg m -1 s n-2 n Water % n-butanol (Commercial grade) 80% Glycerol (Commercial grade) 60% Glycerol (Commercial grade) % CMC % CMC % CMC MEASUREMENT OF LIQUID PROPERTIES The properties of the liquids were measured at room temperature. The densities of the liquids were measured with a specific gravity bottle and the viscous properties of Newtonian and non-newtonian liquids were measured by using Brookfield Rheometer (Model LVDV-II+). The surface tension was measured by the drop weight method. Three to five experiments were conducted for the determination of liquid properties like density, surface tension, viscosity and the average value from the experiments was used for the calculations. Same static bed height was maintained for all experiments. 2.5 MEASUREMENT OF LIQUID HOLDUP The air and liquid flow rates were allowed to attain a steady state condition and both these flow rates were suddenly stopped by closing the
8 29 valves simultaneously. Then the liquid holdup was measured by using the following equation. l Volumeof theliquid Total volumeof thecolumn (2.1) 2.6 MEASUREMENT OF GAS HOLDUP Gas holdup was measured by volume displacement method (Nacef et al 1992 and Miura et al 2001).The air and liquid flow rates were allowed to attain a steady state condition and both these flow rates were suddenly stopped by closing the valves simultaneously and then the column was filled with liquid. After simultaneously closing the valves the height of the liquid in the column gets decreased. This decreased volume can be measured by filling liquid. The ratio of difference between the total volume of the column and volume of liquid used to fill the column to the total volume of the column gave the gas holdup. 2.7 MEASUREMENT OF MINIMUM FLUIDIZATION VELOCITY In visual observation method, the velocity at which the first particle move upwards is taken as minimum fluidization velocity. Minimum fluidization velocity was determined by visual observation method (Koide et al 1984, Zhang et al 1995). The minimum fluidization velocity results obtained by visual observation were compared with the results obtained from pressure drop method (Koide et al 1984). The deviation was found to be less than ± 5%.
Liquid -Vapor. Contacting columns
Liquid -Vapor * Contacting columns Distillation Column Design The design of a distillation column can be divided into the following steps: 1. Specify the degree of separation required: set product specifications.
More informationChapter 3 EXPERIMENTAL: EQUIPMENT, SET-UP, AND PROCEDURE
Chapter 3 EXPERIMENTAL: EQUIPMENT, SET-UP, AND PROCEDURE 72 3.0 Introduction The experimental work was carried out in three stages. First stage: a laboratory scale single nozzle horizontal jet ejector
More informationCFD SIMULATIONS IN AN INTERNAL CIRCULATION AIRLIFT OPERATING UNDER HOMOGENEOUS REGIME
CFD SIMULATIONS IN AN INTERNAL CIRCULATION AIRLIFT OPERATING UNDER HOMOGENEOUS REGIME P. A. S. Monteiro 1, P. Seleghim Jr. 1 1 University of São Paulo, Engineering School of São Carlos, Mechanical Engineering
More informationThe water supply for a hydroelectric plant is a reservoir with a large surface area. An outlet pipe takes the water to a turbine.
Fluids 1a. [1 mark] The water supply for a hydroelectric plant is a reservoir with a large surface area. An outlet pipe takes the water to a turbine. State the difference in terms of the velocity of the
More informationChapter 13 Fluids. Copyright 2009 Pearson Education, Inc.
Chapter 13 Fluids Phases of Matter Density and Specific Gravity Pressure in Fluids Atmospheric Pressure and Gauge Pressure Pascal s Principle Units of Chapter 13 Measurement of Pressure; Gauges and the
More informationPHYS 101 Previous Exam Problems
PHYS 101 Previous Exam Problems CHAPTER 14 Fluids Fluids at rest pressure vs. depth Pascal s principle Archimedes s principle Buoynat forces Fluids in motion: Continuity & Bernoulli equations 1. How deep
More informationOld-Exam.Questions-Ch-14 T072 T071
Old-Exam.Questions-Ch-14 T072 Q23. Water is pumped out of a swimming pool at a speed of 5.0 m/s through a uniform hose of radius 1.0 cm. Find the mass of water pumped out of the pool in one minute. (Density
More information. In an elevator accelerating upward (A) both the elevator accelerating upward (B) the first is equations are valid
IIT JEE Achiever 2014 Ist Year Physics-2: Worksheet-1 Date: 2014-06-26 Hydrostatics 1. A liquid can easily change its shape but a solid cannot because (A) the density of a liquid is smaller than that of
More informationFlow behavior of wakes in a three-phase slurry bubble column with viscous liquid medium
Korean J. Chem. Eng., 28(3), 974-979 (2011) DOI: 10.1007/s11814-010-0403-4 INVITED REVIEW PAPER Flow behavior of wakes in a three-phase slurry bubble column with viscous liquid medium Dae Ho Lim*, Ji Hwa
More informationHydrodynamic and Mass Transfer Characteristics of External-Loop Airlift Reactors without an Extension Tube above the Downcomer
Korean J. Chem. Eng., 18(2), 240-246 (2001) Hydrodynamic and Mass Transfer Characteristics of External-Loop Airlift Reactors without an Extension Tube above the Downcomer Keun Ho Choi Department of Chemical
More informationBioreactor System ERT 314. Sidang /2011
Bioreactor System ERT 314 Sidang 1 2010/2011 Chapter 2:Types of Bioreactors Week 4 Flow Patterns in Agitated Tanks The flow pattern in an agitated tank depends on the impeller design, the properties of
More informationLecture Outline Chapter 15. Physics, 4 th Edition James S. Walker. Copyright 2010 Pearson Education, Inc.
Lecture Outline Chapter 15 Physics, 4 th Edition James S. Walker Chapter 15 Fluids Density Units of Chapter 15 Pressure Static Equilibrium in Fluids: Pressure and Depth Archimedes Principle and Buoyancy
More informationExperimental Study of an Air Lift Pump
Engineering, Technology & Applied Science Research Vol. 7, No. 3, 217, 1676-168 1676 Experimental Study of an Air Lift Pump Fawzy Sh. Abou Taleb Mechanical Engineering Department Engineering College Northern
More informationEVALUATION OF FLUID DYNAMICS IN A HOT AND A COLD SYSTEM OF INTERCONNECTING FLUIDISED BEDS
Refereed Proceedings The 13th International Conference on Fluidization - New Paradigm in Fluidization Engineering Engineering Conferences International Year 2010 EVALUATION OF FLUID DYNAMICS IN A HOT AND
More information1. All fluids are: A. gases B. liquids C. gases or liquids D. non-metallic E. transparent ans: C
Chapter 14: FLUIDS 1 All fluids are: A gases B liquids C gases or liquids D non-metallic E transparent 2 Gases may be distinguished from other forms of matter by their: A lack of color B small atomic weights
More informationMultiple effects of operating variables on the bubble properties in three-phase slurry bubble columns
Korean J. Chem. Eng., 26(2), 587-591 (2009) SHORT COMMUNICATION Multiple effects of operating variables on the bubble properties in three-phase slurry bubble columns Ik Sang Shin*, Sung Mo Son*, Uk Yeong
More informationWorld Academy of Science, Engineering and Technology International Journal of Chemical and Molecular Engineering Vol:7, No:12, 2013
Study of the Particle Size Effect on Bubble Rise Velocities in a Three-Phase Bubble Column Weiling Li, Wenqi Zhong, Baosheng Jin, Rui Xiao, Yong Lu, Tingting He Abstract Experiments were performed in a
More informationLesson 12: Fluid statics, Continuity equation (Sections ) Chapter 9 Fluids
Lesson : luid statics, Continuity equation (Sections 9.-9.7) Chapter 9 luids States of Matter - Solid, liquid, gas. luids (liquids and gases) do not hold their shapes. In many cases we can think of liquids
More informationStructure of Mechanically Agitated Gas-Liquid Contactors
Structure of Mechanically Agitated Gas-Liquid Contactors 5 2 Structure of Mechanically Agitated Gas-Liquid Contactors 2.1 The vessel geometry The most commonly adopted geometry of a stirred gas-liquid
More informationCHEM 355 EXPERIMENT 7. Viscosity of gases: Estimation of molecular diameter
CHEM 355 EXPERIMENT 7 Viscosity of gases: Estimation of molecular diameter Expressed most simply, the viscosity of a fluid (liquid or gas) relates to its resistance to flow. The viscosity of a gas is determined
More informationSimulation of Gas Holdup in a Bubble Column with a Draft Tube for Gas Dispersion into an Annulus
Simulation of Gas Holdup in a Bubble Column with a Draft Tube for Gas Dispersion into an Annulus Fukuji Yamashita Dept. of Applied Bioscience, Kanagawa Institute of Technology, Atsugi 243-292, Japan, yamasita@bio.kanagawa-it.ac.jp
More informationAP Physics B Ch 10 Fluids. MULTIPLE CHOICE. Choose the one alternative that best completes the statement or answers the question.
Name: Period: Date: AP Physics B Ch 10 Fluids 1) The three common phases of matter are A) solid, liquid, and vapor. B) solid, plasma, and gas. C) condensate, plasma, and gas. D) solid, liquid, and gas.
More informationExperiment 8: Minor Losses
Experiment 8: Minor Losses Purpose: To determine the loss factors for flow through a range of pipe fittings including bends, a contraction, an enlargement and a gate-valve. Introduction: Energy losses
More informationof air-lift reactors based on bubble dynamics
Indian Journal of Chemical Technology Vol. 5, July 1998, pp. 187-191 Modelling of air-lift reactors based on bubble dynamics Saikat Chakraborty+, Kajari Kargupta & Avijit Bhowal* Department of Chemical
More informationChapter 13 Fluids. Copyright 2009 Pearson Education, Inc.
Chapter 13 Fluids Phases of Matter Density and Specific Gravity Pressure in Fluids Atmospheric Pressure and Gauge Pressure Pascal s Principle Units of Chapter 13 Measurement of Pressure; Gauges and the
More informationDigester Processes. 1. Raw Sludge Pumping System
Digester Processes 1. Raw Sludge Pumping System Removes accumulated sludge from the primary clarifiers, pumped through 1 of 2 pipes either 150 or 200mm in diameter (Fig. 1.1). Fig 1.1 Pipes feeding Digesters
More informationMS.RAJA ELGADY/PRESSURE PAPER 3
1- (a) A water tank has a rectangular base of dimensions 1.5m by 1.2m and contains 1440 kg of water. Calculate (i) the weight of the water, weight =...... [1] (ii) the pressure exerted by the water on
More informationChapter 9 Solids and Fluids
2/17/16 Chapter 9 Solids and Fluids Units of Chapter 9 Solids and Elastic Moduli Fluids: Pressure and Pascal s Buoyancy and Archimedes Fluid Dynamics and Bernoulli s Surface Tension, Viscosity, and Poiseuille
More informationQuestions. theonlinephysicstutor.com. facebook.com/theonlinephysicstutor. Name: Edexcel Drag Viscosity. Questions. Date: Time: Total marks available:
Name: Edexcel Drag Viscosity Questions Date: Time: Total marks available: Total marks achieved: Questions Q1. A small helium balloon is released into the air. The balloon initially accelerates upwards.
More informationCalculations of hydraulic resistance of simple pipelines for liquid viscous and non-newtonian products.
VISIMIX PL. PIPELINE FOR DISCHARGING OF A SHAMPOO Calculations of hydraulic resistance of simple pipelines for liquid viscous and non-newtonian products. The task: to build a temporary pipeline in order
More informationChapter 10 Fluids. Which has a greater density? Ch 10: Problem 5. Ch 10: Problem Phases of Matter Density and Specific Gravity
Chapter 10 Fluids 10-1 Phases of Matter The three common phases of matter are solid, liquid, and gas. A solid has a definite shape and size. A liquid has a fixed volume but can be any shape. A gas can
More informationMEMORANDUM. Investigation of Variability of Bourdon Gauge Sets in the Chemical Engineering Transport Laboratory
1 MEMORANDUM TO: FROM: Prof. Davis Hubbard Prof. Faith A. Morrison DATE: 22 April 2014 RE: Investigation of Variability of Bourdon Gauge Sets in the Chemical Engineering Transport Laboratory Introduction
More informationStatic Fluids. **All simulations and videos required for this package can be found on my website, here:
DP Physics HL Static Fluids **All simulations and videos required for this package can be found on my website, here: http://ismackinsey.weebly.com/fluids-hl.html Fluids are substances that can flow, so
More informationChapter 15 Fluid. Density
Density Chapter 15 Fluid Pressure Static Equilibrium in Fluids: Pressure and Depth Archimedes Principle and Buoyancy Applications of Archimedes Principle By Dr. Weining man 1 Units of Chapter 15 Fluid
More informationThe Study of Bubbly Gas-Water Flow Using
The Study of Bubbly Gas-Water Flow Using Displacement Current Phase Tomography Chris Zuccarelli 1, Benjamin Straiton 1, Joshua Sines 1, Qussai Marashdeh 1 1 Tech4Imaging, 1910 Crown Park Court, Columbus,
More informationIrrigation &Hydraulics Department lb / ft to kg/lit.
CAIRO UNIVERSITY FLUID MECHANICS Faculty of Engineering nd Year CIVIL ENG. Irrigation &Hydraulics Department 010-011 1. FLUID PROPERTIES 1. Identify the dimensions and units for the following engineering
More informationMEMORIAL UNIVERSITY OF NEWFOUNDLAND Faculty of Engineering and Applied Science FLUID MECHANICS LABORATORY PIPE FRICTION
MEMORIAL UNIVERSITY OF NEWFOUNDLAND Faculty of Engineering and Applied Science FLUID MECHANICS LABORATORY PIPE FRICTION Objective To estimate the fluid pressure drops and roughness specifications for copper
More informationExercise 5-2. Bubblers EXERCISE OBJECTIVE DISCUSSION OUTLINE. Bubblers DISCUSSION. Learn to measure the level in a vessel using a bubbler.
Exercise 5-2 Bubblers EXERCISE OBJECTIVE Learn to measure the level in a vessel using a bubbler. DISCUSSION OUTLINE The Discussion of this exercise covers the following points: Bubblers How to measure
More informationChapter 15 Fluids. Copyright 2010 Pearson Education, Inc.
Chapter 15 Fluids Density Units of Chapter 15 Pressure Static Equilibrium in Fluids: Pressure and Depth Archimedes Principle and Buoyancy Applications of Archimedes Principle Fluid Flow and Continuity
More informationAP B Fluids Practice Problems. Multiple Choice. Slide 2 / 43. Slide 1 / 43. Slide 4 / 43. Slide 3 / 43. Slide 6 / 43. Slide 5 / 43
Slide 1 / 43 Slide 2 / 43 P Fluids Practice Problems Multiple hoice Slide 3 / 43 1 Two substances mercury with a density 13600 kg/m 3 and alcohol with a density 0.8 kg/m 3 are selected for an experiment.
More informationHours / 100 Marks Seat No.
17421 21415 3 Hours / 100 Marks Seat No. Instructions : (1) All Questions are compulsory. (2) Answer each next main Question on a new page. (3) Illustrate your answers with neat sketches wherever necessary.
More informationThe Discussion of this exercise covers the following points: Range with an elevated or suppressed zero Suppressed-zero range Elevated-zero range
Exercise 4-3 Zero Suppression and Zero Elevation EXERCISE OBJECTIVE In this exercise, you will learn the effect that mounting a pressure transmitter above or below the reference level has on the hydrostatic
More informationChapter 9 Fluids and Buoyant Force
Chapter 9 Fluids and Buoyant Force In Physics, liquids and gases are collectively called fluids. 3/0/018 8:56 AM 1 Fluids and Buoyant Force Formula for Mass Density density mass volume m V water 1000 kg
More informationCHAPTER 9 Fluids. Units
CHAPTER 9 Fluids Units Fluids in Motion; Flow Rate and the Equation of Continuity Bernoulli s Equation Applications of Bernoulli s Principle Viscosity Flow in Tubes: Poiseuille s Equation, Blood Flow Surface
More informationMicro Motion Pressure Drop Testing
12/2018 Micro Motion Pressure Drop Testing www.emerson.com/micromotion Introduction Micro Motion has traditionally taken a very conservative approach to pressure drop, with single pressure measurements
More informationSlide 5 / What is the difference between the pressure on the bottom of a pool and the pressure on the water surface? A ρgh B ρg/h C ρ/gh D gh/ρ
Slide 1 / 47 1 Two substances mercury with a density 13600 kg/m3 and alcohol with a density 800 kg/m3 are selected for an experiment. If the experiment requires equal masses of each liquid, what is the
More informationPerformance Characteristics of Airlift Pumps with Vortex Induced by Tangential Fluid Injection
Bucknell University Bucknell Digital Commons Honors Theses Student Theses 2011 Performance Characteristics of Airlift Pumps with Vortex Induced by Tangential Fluid Injection Jacob Riglin Bucknell University
More informationMiddle East Technical University Department of Mechanical Engineering ME 305 Fluid Mechanics I Fall 2018 Section 4 (Dr.
Middle East Technical University Department of Mechanical Engineering ME 305 Fluid Mechanics I Fall 2018 Section 4 (Dr. Sert) Study Set 3 Reading Assignments You can find the answers of some of the following
More informationTWO PHASE FLOW METER UTILIZING A SLOTTED PLATE. Acadiana Flow Measurement Society
TWO PHASE FLOW METER UTILIZING A SLOTTED PLATE Acadiana Flow Measurement Society Gerald L. Morrison Presented by: Mechanical Engineering Department Daniel J. Rudroff 323 Texas A&M University Flowline Meters
More informationA child places a car of mass 95 g on the track. She adjusts the controller to a power of 4.2 W so the car accelerates from rest for 0.40 s.
1 The picture shows a track for racing toy electric cars. A guide pin fits in a groove in the track to keep the car on the track. A small electric motor in the car is controlled, with a hand-controller,
More informationγ water = 62.4 lb/ft 3 = 9800 N/m 3
CEE 42 Aut 200, Exam #1 Work alone. Answer all questions. Always make your thought process clear; if it is not, you will not receive partial credit for incomplete or partially incorrect answers. Some data
More informationDevelopment of High-speed Gas Dissolution Device
Development of High-speed Gas Dissolution Device Yoichi Nakano*, Atsushi Suehiro**, Tetsuhiko Fujisato***, Jun Ma**** Kesayoshi Hadano****, Masayuki Fukagawa***** *Ube National College of Technology, Tokiwadai
More information3 1 PRESSURE. This is illustrated in Fig. 3 3.
P = 3 psi 66 FLUID MECHANICS 150 pounds A feet = 50 in P = 6 psi P = s W 150 lbf n = = 50 in = 3 psi A feet FIGURE 3 1 The normal stress (or pressure ) on the feet of a chubby person is much greater than
More informationA centrifugal pump consists of an impeller attached to and rotating with the shaft and a casing that encloses the impeller.
Centrifugal pump How centrifugal pumps work A centrifugal pump consists of an impeller attached to and rotating with the shaft and a casing that encloses the impeller. In centrifugal pump, liquid is forced
More informationME 333 Fluid Mechanics. Lab Session VISCOUS LOSSES IN PIPES
ME 333 Fluid Mechanics Lab Session VISCOUS LOSSES IN PIPES Introduction Flow in pipes, laminar or turbulent, is subject to pressure losses that result from the viscous stresses on the wall of the pipe.
More information1. The principle of fluid pressure that is used in hydraulic brakes or lifts is that:
University Physics (Prof. David Flory) Chapt_15 Thursday, November 15, 2007 Page 1 Name: Date: 1. The principle of fluid pressure that is used in hydraulic brakes or lifts is that: A) pressure is the same
More informationExperiment Instructions. Circulating Pumps Training Panel
Experiment Instructions Circulating Pumps Training Panel Experiment Instructions This manual must be kept by the unit. Before operating the unit: - Read this manual. - All participants must be instructed
More informationCover Page for Lab Report Group Portion. Head Losses in Pipes
Cover Page for Lab Report Group Portion Head Losses in Pipes Prepared by Professor J. M. Cimbala, Penn State University Latest revision: 02 February 2012 Name 1: Name 2: Name 3: [Name 4: ] Date: Section
More informationQuiz name: Chapter 13 Test Review - Fluids
Name: Quiz name: Chapter 13 Test Review - Fluids Date: 1. All fluids are A gases B liquids C gasses or liquids D non-metallic E transparent 2. 1 Pa is A 1 N/m B 1 m/n C 1 kg/(m s) D 1 kg/(m s 2 ) E 1 N/m
More informationPHY131H1S - Class 23. Today: Fluids Pressure Pascal s Law Gauge Pressure Buoyancy, Archimedes Principle. A little pre-class reading quiz
PHY131H1S - Class 23 Today: Fluids Pressure Pascal s Law Gauge Pressure Buoyancy, Archimedes Principle Archimedes (287-212 BC) was asked to check the amount of silver alloy in the king s crown. The answer
More informationEFFECTS OF CHEMICAL ADDITIVES ON THE PRESSURE DROP IN THE PIPES
International Journal of Bio-Technology andresearch (IJBTR) ISSN(P): 2249-6858; ISSN(E): 2249-796X Vol. 4, Issue 1, Feb 2014, 1-6 TJPRC Pvt. Ltd. EFFECTS OF CHEMICAL ADDITIVES ON THE PRESSURE DROP IN THE
More informationApplied Fluid Mechanics
Applied Fluid Mechanics 1. The Nature of Fluid and the Study of Fluid Mechanics 2. Viscosity of Fluid 3. Pressure Measurement 4. Forces Due to Static Fluid 5. Buoyancy and Stability 6. Flow of Fluid and
More informationGas-liquid mass transfer in an external airlift loop reactor for syngas fermentation
Retrospective Theses and Dissertations 2007 Gas-liquid mass transfer in an external airlift loop reactor for syngas fermentation Samuel T. Jones Iowa State University Follow this and additional works at:
More informationDownhole Gas Separators
Gas Well De-Liquification Workshop Denver, Colorado February 27 March1, 2006 Downhole Gas Separators A Laboratory and Field Study Jim McCoy, Echometer Company Tony Podio, University of Texas at Austin
More informationUse equation for the cylindrical section and equation or for the ends.
Solution 13.1 See section 13.3.4, equations 13.7 to 13.18 Solution 13.2 Use equation 13.34. (a) rigid constant C = 0.43 (b) free to rotate, C = 0.56 Solution 13.3 See section 13.5.1 Use equation 13.39
More informationLab Problems. Lab Problems for Chapter Fluid Characterization by Use of a Stormer Viscometer L-1
Lab Problems This section contains end-of-the-chapter problems that involve data obtained from various simple laboratory experiments. These lab problems for any chapter can be obtained by clicking on the
More informationLong Win s Educational Facilities for Fluid Mechanics
Since 1985 F luid mechanics is a science to study how fluids flow and how fluids act on objects. T he wind tunnel is a comprehensive, complete and substantial system for students to study fundamental and
More informationAssistant Lecturer Anees Kadhum AL Saadi
Pressure Variation with Depth Pressure in a static fluid does not change in the horizontal direction as the horizontal forces balance each other out. However, pressure in a static fluid does change with
More informationComments on Homework. Class 4 - Pressure. Atmospheric Pressure. Gauge vs. Absolute Pressure. 2. Gauge vs. Absolute Pressure. 1.
Class 4 - Pressure 1. Definitions 2. Gauge Pressure 3. Pressure and Height of Liquid Column (Head) 4. Pressure Measurement and Manometers Please don t forget the special problem for the next HW assignment
More informationFlow Charts and Lubricated Transport of Foams
Flow Charts and Lubricated Transport of Foams Travis A. Smieja, Daniel D. Joseph and Gordon Beavers University of Minnesota July 2001 file: 2000/papers/LubTransport/foam.- Abstract The flow characteristics
More informationThe Discussion of this exercise covers the following points:
Exercise 3-2 Orifice Plates EXERCISE OBJECTIVE In this exercise, you will study how differential pressure flowmeters operate. You will describe the relationship between the flow rate and the pressure drop
More informationInstrumentation & Data Acquisition Systems
Instrumentation & Data Acquisition Systems Section 3 -Level Robert W. Harrison, PE Bob@TheHarrisonHouse.com Made in USA 1 Level Section Question Which level measuring technology is the best solution when
More informationPETROLEUM & GAS PROCESSING TECHNOLOGY (PTT 365) SEPARATION OF PRODUCED FLUID
PETROLEUM & GAS PROCESSING TECHNOLOGY (PTT 365) SEPARATION OF PRODUCED FLUID Miss Nur Izzati Bte Iberahim Introduction Well effluents flowing from producing wells come out in two phases: vapor and liquid
More informationDISTILLATION POINTS TO REMEMBER
DISTILLATION POINTS TO REMEMBER 1. Distillation columns carry out physical separation of liquid chemical components from a mixture by a. A combination of transfer of heat energy (to vaporize lighter components)
More informationFLOATING AND SINKING
NAME SCHOOL INDEX NUMBER DATE FLOATING AND SINKING 1. 1994 Q5a P2 (a) State Archimedes s principal (1 mark) 2. 1996 Q29 P1 A solid copper sphere will sink in water while a hollow copper sphere of the same
More informationPhys101 Lectures Fluids I. Key points: Pressure and Pascal s Principle Buoyancy and Archimedes Principle. Ref: 10-1,2,3,4,5,6,7.
Phys101 Lectures 21-22 Fluids I Key points: Pressure and Pascal s Principle Buoyancy and Archimedes Principle Ref: 10-1,2,3,4,5,6,7. Page 1 10-1 Phases of Matter The three common phases of matter are solid,
More informationProcess Dynamics, Operations, and Control Lecture Notes - 20
Lesson 0. Control valves 0.0 Context Controller output is a signal that varies between 0 and 100%. Putting this signal to use requires a final control element, a device that responds to the controller
More informationConstant Pressure Inlet (CCN) Operator Manual
Constant Pressure Inlet (CCN) Operator Manual DOC-0125 Revision J 2545 Central Avenue Boulder, CO 80301-5727 USA C O P Y R I G H T 2 0 1 1 D R O P L E T M E A S U R E M E N T T E C H N O L O G I E S, I
More informationJoint industry project on foam
Joint industry project on foam, E.D. Nennie (TNO Fluid dynamics) W. Schiferli (Shell Projects & Technology) 2 Introduction Foamers are used for gas well deliquification. Lab tests are being used to evaluate
More informationYutaek Seo. Subsea Engineering
Yutaek Seo Subsea Engineering Inlet receiving Gas and liquids that enter the gas processing facilities pass emergency shutdown valves, and then go to inlet receiving, where condensed phases drop out. Gas
More informationCover Page for Lab Report Group Portion. Drag on Spheres
Cover Page for Lab Report Group Portion Drag on Spheres Prepared by Professor J. M. Cimbala, Penn State University Latest revision: 29 September 2017 Name 1: Name 2: Name 3: [Name 4: ] Date: Section number:
More informationNotes Chapter 3. Buoyancy
Notes Chapter 3 Buoyancy Pressure in a Fluid 3.2 Pressure and the Buoyant Forces Liquids and gases are fluids materials that can flow and have no definite shape. Objects in a fluid experience a buoyant
More informationE 158 E 198 E 248. Tank top mounting Connection up to G11 / 4 Nominal flow rate up to 250 l/min e d
R e t u r n - S u c t i o n F i l t e rs E 158 E 198 E 248 Tank top mounting Connection up to G11 / 4 Nominal flow rate up to 250 l/min 20.90-5e 0.0-2d D e s c r i p t i o n Application For operation in
More informationENGINEERING FLUID MECHANICS
DEPARTMENT of MECHANICAL ENGINEERING FLUID MECHANICS Subject code: 10ME46B Faculty name: Naveen H E QUESTION BANK UNIT-1: FLUID PROPERTIES 1. Define the following: i) density, ii) weight density, iii)
More informationEDUCTOR. principle of operation
EDUCTOR principle of operation condensate and mixing eductor s are designed to mix two liquids intimately in various proportions in operations where the pressure liquid is the greater proportion of the
More informationBest Practices - Coiled Tubing Deployed Ball Drop Type Perforating Firing Systems
Best Practices - Coiled Tubing Deployed Ball Drop Type Perforating Firing Systems As a result of a recent job incident utilizing a Ball Drop Type firing system deployed on coiled tubing, the following
More informationSTUDY OF SLUG CONTROL TECHNIQUES IN PIPELINE SYSTEMS
STUDY OF SLUG CONTROL TECHNIQUES IN PIPELINE SYSTEMS JOSÉ L. A,VIDAL Petrobrás Research Center - CENPES/PDEP/TOOL Av.Horácio de Macedo 95- Cidade Universitária 191-915 -Rio de Janeiro-RJ E-mail:josearias@petrobras.com.br
More informationE 084 Tank top mounting Connection up to G1 / -16 SAE Nominal flow rate up to 80 l/min / 21.1 gpm
Return-Suction Filters E 08 Tank top mounting Connection up to G / -6 SE Nominal flow rate up to 80 l/min /. gpm Description pplication For operation in units with hydrostatic drives, when the return flow
More informationAnchor Load Cells. Among the different types that are used as anchor load cells
Chapter: 3.1 Anchor Load Cells Page No.: 1 Number of Pages: 1 In rock and base engineering anchors are applied as construction element. They stabilise the rock by absorbing axial load and shear forces.
More informationNew Approaches for Theoretical Estimation of Mass Transfer Parameters in Both Gas-Liquid and Slurry Bubble Columns
18 New Approaches for Theoretical Estimation of Mass Transfer Parameters in Both Gas-Liquid and Slurry Bubble Columns Stoyan NEDELTCHEV and Adrian SCHUMPE Institute of Technical Chemistry, TU Braunschweig
More informationFluid Flow. Link. Flow» P 1 P 2 Figure 1. Flow Model
Fluid Flow Equipment: Water reservoir, output tubes of various dimensions (length, diameter), beaker, electronic scale for each table. Computer and Logger Pro software. Lots of ice.temperature probe on
More informationUNUSUAL ASPECTS OF PUMP SYSTEMS. Jacques Chaurette p. eng. ww.lightmypump.com July 2003
UNUSUAL ASPECTS OF PUMP SYSTEMS Jacques Chaurette p. eng. ww.lightmypump.com July 2003 There are many unusual aspects to pump systems. It is some of these aspects that make pump systems fascinating for
More informationConcentration profile of jet gas in the feed injection zone of a FCC riser
Available online at www.sciencedirect.com Progress in Natural Science 18 (2008) 1285 1291 www.elsevier.com/locate/pnsc Concentration profile of jet gas in the feed injection zone of a FCC riser Chenglin
More informationTechnical Progress Report. Development of the Instrumentation and Modeling for Heat Transfer Characteristics in CFBC
Technical Progress Report No.2 Development of the Instrumentation and Modeling for Heat Transfer Characteristics in CFBC to U.S. Department of Energy Pittsburgh Energy Technology Center P.O. Box 10940,
More informationComments on Homework. Quiz. Class 3 - Pressure. Atmospheric Pressure. 2. Gauge vs. Absolute Pressure. 1. Definitions. Temperature conversion
Comments on Homework Quiz Temperature conversion T ( R) = T (K) 1.8 T ( C) = T(K) - 273.15 T ( F) = T( R) - 460 However, difference in temperature is: T ( C) = T (K) T ( F) = T ( R) T ( R) = 1.8 T ( C)
More information3. A fluid is forced through a pipe of changing cross section as shown. In which section would the pressure of the fluid be a minimum?
AP Physics Multiple Choice Practice Fluid Mechanics 1. A cork has weight mg and density 5% of water s density. A string is tied around the cork and attached to the bottom of a water-filled container. The
More informationDesign, Static Structural & Model Analysis of Water Ring Vacuum Pump Impeller
IJSRD - International Journal for Scientific Research & Development Vol. 6, Issue 03, 2018 ISSN (online): 2321-0613 Design, Static Structural & Model Analysis of Water Ring Vacuum Pump Impeller Ajay A.
More information12 fa. eel), Ara, Fl eat Mobi eu) r V14,:srholki CV -65 P- 1 1). e2r 46. ve, lactogin. 1 V eil - ( - t Teo. c 1 4 d 4. .'=- tit/ (4 nit) 6 --)
1). e2r 46 h eel), /pea lactogin Yd / In 1 V eil - ( - Cw ve, P- 1 Ara, Fl eat Mobi eu) r V14,:srholki 5e 0 (44,4 ci4) CV -65 So 0 t Teo.'=- tit/ (4 nit) 6 --) ci Seco (df_ 1 c 1 4 d 4 5-40 C 12 fa 4)
More informationCOURSE NUMBER: ME 321 Fluid Mechanics I Fluid statics. Course teacher Dr. M. Mahbubur Razzaque Professor Department of Mechanical Engineering BUET
COURSE NUMBER: ME 321 Fluid Mechanics I Fluid statics Course teacher Dr. M. Mahbubur Razzaque Professor Department of Mechanical Engineering BUET 1 Fluid statics Fluid statics is the study of fluids in
More informationLab 3 Introduction to Quantitative Analysis: Pumps and Measurements of Flow
Georgia Institute of Technology School of Earth and Atmospheric Sciences EAS 4641, Spring 2008 Lab 3 Introduction to Quantitative Analysis: Pumps and Measurements of Flow Purpose of Lab 3: 1) To gain a
More information