Trial runs of loading equipment for proposed test of oven wall

Similar documents
MET 335W Fluid Mechanics Laboratory. Lab 1: Bourdon Tube Calibration. Nick Peak

3 1 PRESSURE. This is illustrated in Fig. 3 3.

and its weight (in newtons) when located on a planet with an acceleration of gravity equal to 4.0 ft/s 2.

TEST FOR STABILOMETER VALUE OF BITUMINOUS MIXTURES

Heat Engine. Reading: Appropriate sections for first, second law of thermodynamics, and PV diagrams.

CONTENTS 1. INTRODUCTION DESCRIPTION OF TEST SAMPLE TEST RIG GENERAL ARRANGEMENT TEST SEQUENCE...7

LABORATORY EXERCISE 1 CONTROL VALVE CHARACTERISTICS

Follow this and additional works at:

Experiment. THE RELATIONSHIP BETWEEN VOLUME AND TEMPERATURE, i.e.,charles Law. By Dale A. Hammond, PhD, Brigham Young University Hawaii

TEACHING SCIENCE BY OCEAN INQUIRY Pressure

Unit 2 Kinetic Theory, Heat, and Thermodynamics: 2.A.1 Problems Temperature and Heat Sections of your book.

Laboratory Hardware. Custom Gas Chromatography Solutions WASSON - ECE INSTRUMENTATION. Custom solutions for your analytical needs.

Introduction. Objectives. Hazards. Procedure

Glass tube flowmeters Series 2000

Copyright ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA , United States.

(fig. 3) must be at the same temperature as the water in this chamber CALORIMETRIC STUDIES OF THE EXTREMITIES

LAB 13: FLUIDS OBJECTIVES

International Journal of Technical Research and Applications e-issn: , Volume 4, Issue 3 (May-June, 2016), PP.

MEMORIAL UNIVERSITY OF NEWFOUNDLAND Faculty of Engineering and Applied Science FLUID MECHANICS LABORATORY PIPE FRICTION

Experiment Instructions. Circulating Pumps Training Panel

σ = force / surface area force act upon In the image above, the surface area would be (Face height) * (Face width).

AUTOMATIC FLOW CARTRIDGES. Competition Analysis Not All Automatics Are Created Equal

Experiment 11: The Ideal Gas Law

Hydrostatic Force on a Submerged Surface

Exercise 2-3. Flow Rate and Velocity EXERCISE OBJECTIVE C C C

CHEMICAL ENGINEERING LABORATORY CHEG 239W. Control of a Steam-Heated Mixing Tank with a Pneumatic Process Controller

APPENDIX B TESTING PROTOCOLS. Method A: Straight Test Method B: Angular Deflection Test. Method C: Shear Load Test

. In an elevator accelerating upward (A) both the elevator accelerating upward (B) the first is equations are valid

Glass tube flowmeters Series 2000 Variable area flowmeter for low flows of liquids and gases

(Received 9 September 1940)

LAB 13: FLUIDS OBJECTIVES

Characterizers for control loops

Physics 1021 Experiment 4. Buoyancy

Laboratory Hardware. Custom Gas Chromatography Solutions WASSON - ECE INSTRUMENTATION. Engineered Solutions, Guaranteed Results.

Chapter 3 PRESSURE AND FLUID STATICS

Lecture 19 Fluids: density, pressure, Pascal s principle and Buoyancy.

DETERMINING OPTIMUM RESIDUAL ASPHALT CONTENT (RAC) FOR POLYMER-MODIFIED SLURRY SEAL (MICROSURFACING) MIXTURES

DO NOT, under any circumstances, throw this away! This packet MUST be saved for the final exam.

The Discussion of this exercise covers the following points:

TXDOT DESIGNATION: TEX-922-K

LOW PRESSURE EFFUSION OF GASES adapted by Luke Hanley and Mike Trenary

OIL SUPPLY SYSTEMS ABOVE 45kW OUTPUT 4.1 Oil Supply

Pressure of the atmosphere varies with elevation and weather conditions. Barometer- device used to measure atmospheric pressure.

Model 687 Mouse Ventilator User s Manual. Model 687 Mouse Ventilator

ME 333 Fluid Mechanics. Lab Session VISCOUS LOSSES IN PIPES

Activities for Measuring Acceleration and Deceleration due to Gravity and Friction. Grade Level: Middle School

River Bridge - Test Shaft-1 Clarke County, MS, 4/2/2012

Analysis of the Motion of Plate Type Suction or Discharge Valves Mounted on Reciprocating Pistons

Item 404 Driving Piling

RESIDENTIAL IRRIGATION WORKSHOP IRRIGATION 101 AND BEYOND FOR WEST BENCH RESIDENTS

Stadium Project - DP-70 Atlanta, GA, 9/30/2014

TESTING APPLICATION STANDARD (TAS)

Physics Experiment 17 Ideal Gas Law Qualitative Study

OP CHECKLIST FOR 1D CONSOLIDATION LABORATORY TEST

LOW PRESSURE EFFUSION OF GASES revised by Igor Bolotin 03/05/12

3. 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?

09 - Choosing /sizing a cylinder and valve

DETRMINATION OF A PLUNGER TYPE WAVE MAKER CHARACTERISTICE IN A TOWING TANK

Chlorinator MODEL MK-I

Pressure Control. where: p is the pressure F is the normal component of the force A is the area

By Syed Ahmed Amin Shah 4 th semester Class No 8 Submitted To Engr. Saeed Ahmed

TXDOT DESIGNATION: TEX-922-K

MEMORANDUM. Investigation of Variability of Bourdon Gauge Sets in the Chemical Engineering Transport Laboratory

HCMTCB MATERIALS SAMPLING & TESTING PERFORMANCE CHECKLIST

Ozobot Bit Classroom Application: Boyle s Law Simulation


Aug 17, 2001 LAB MANUAL MAXIMUM SPECIFIC GRAVITY (RICE VOIDS TEST) OF PAVING MIXTURES AASHTO Designation T 209 (Mn/DOT Modified))

INSTRUCTOR RESOURCES

Please welcome for any correction or misprint in the entire manuscript and your valuable suggestions kindly mail us

This experiment will develop skills in graphing and graphical analysis.

Unit A-2: List of Subjects

A New and Simplified Method for Determination of Conductor Surface Casing Setting Depths in Shallow Marine Sediments (SMS)

Smart Water Application Technologies (SWAT)

where ρ f is the density of the fluid, V is the submerged volume of the object, and g is the acceleration due to gravity.

Cover Page for Lab Report Group Portion. Pump Performance

O-Calc Pro Sag Tension Calculations Explained

γ water = 62.4 lb/ft 3 = 9800 N/m 3

CHAPTER 3 RESULTS AND DISCUSSION

Cover Page for Lab Report Group Portion. Head Losses in Pipes

Exercise 2-2. Second-Order Interacting Processes EXERCISE OBJECTIVE DISCUSSION OUTLINE. The actual setup DISCUSSION

This portion of the piping tutorial covers control valve sizing, control valves, and the use of nodes.

m v = 1.04 x 10-4 m 2 /kn, C v = 1.29 x 10-2 cm 2 /min

Torsional rigidity of structural sections, Civil Engineering, Vol. 5, (1935), p. 698

Presented to the International Technical Rescue Symposium, November Abstract

Boyle s Law VC 09. Experiment 9: Gas Laws. Abstract

γ water = 62.4 lb/ft 3 = 9800 N/m 3

Pole Foundation Design with Spreadsheet

Old-Exam.Questions-Ch-14 T072 T071

MS.RAJA ELGADY/PRESSURE PAPER 3

HEATEC TEC-NOTE. Setting Siemens Pressure Transmitter. Used on Heatec Vertical Asphalt Tanks. Publication No , Revised

Modeling Diffusion Rates of a Gas in an Enclosed Space

Pneumatic dead-weight tester Model CPB3500

Lab 10 - Fluids. Fluids are an important part of our body. To learn how some fundamental physical principles apply to fluids.

PERFORMANCE OF GORMAN-RUPP BACKPACK PUMP WITH RESPECT TO SUCTION LIFT. LENGTH OF HOSE AND DISCHARGE HEAD

Method of Test for Sieve Analysis

Process Nature of Process

2. Practical way of realization of adiabatic process 2.1 Introduction

Interception of a Projectile Using a Human Vision-Based Strategy

Pneumatic Power Topics:

13.1!"#$#%"&'%()$*+%,+-.$+/*$#

Transcription:

Lehigh University Lehigh Preserve Fritz Laboratory Reports Civil and Environmental Engineering 1955 Trial runs of loading equipment for proposed test of oven wall I. J. Taylor S. J. Errera Follow this and additional works at: http://preserve.lehigh.edu/engr-civil-environmental-fritz-labreports Recommended Citation Taylor, I. J. and Errera, S. J., "Trial runs of loading equipment for proposed test of oven wall" (1955). Fritz Laboratory Reports. Paper 1656. http://preserve.lehigh.edu/engr-civil-environmental-fritz-lab-reports/1656 This Technical Report is brought to you for free and open access by the Civil and Environmental Engineering at Lehigh Preserve. It has been accepted for inclusion in Fritz Laboratory Reports by an authorized administrator of Lehigh Preserve. For more information, please contact preserve@lehigh.edu.

"Trial Runs of Loading Equipment for Proposed Test of Oven Wallet Report to Armstrong Cork Company by 8.3. Errera and I.J o Taylor Fritz Engineering Laboratory Lehigh University Report 246.2 February 18, 1955

246.2, Table of Contents Page - Object 1 Test Equipment 1 Test Procedure 2 Test Results 2 Discussion of Test Results 2 Conclusions 3 List of Tables Table 1 - Results of Trial Run No. 1 Table 2 - Results of Trial R~ No. 2 Table 3 - Results,of Trial Run No. 3 Figure 1 - Cross-section of Loading Chamber Figure 2 - Loading Chamber Figure 3 Loading Chamber, View from Above Figure 4 - Diagr~m of Supply and Pressure Line Arrangement Figure 5' - Manometer Indicated Pressure vs. Total Load

246.2 Trial Runs of Loading Equipment for ---~-..--_-...---_.,----...".-..._---~~------ ~roij2.2ed T~t of Ove~~l..! by S.J. Errera and I.J. Taylor Fritz Engineering Laboratory Report 246.1, "Proposed Test of Oven Hall", by I.J. Taylor, outlined a procedure for tests to determine the resistance to uniform lateral loading of a typical masonry wall as used in the material processing ovens.. of the Armstrong Cork Company, Lancaster, Penna. The object of this report is to describe the results of laboratory tests made on the loading components recommended for use in the previous report. ~j;_~!1ipment: To simulate the proposed test conditions, a loading chamber was constructed of plywood and 2" x 3" framing. chamber was composed of two sections, the bottom section acting as a cylinder, and the top section acting as a piston. Figures 1, 2 and 3.) The normal air space in the chamber The (See measured about 4 feet by 8 feet in plan, and 2 feet 6 inches in depth. J8~42-7000, A meteorological balloon, Dewey and Almy type with an uninflated diameter of 10 feet, was inserted into the chamber. Air was supplied to the balloon from a 100 psi supply line, and the pressure within the balloon was indicated by a differential water manometer. pressure line arrangement is shown in Figure 4. The supply and A plastic window

246.2-2, ", in one side of the cylinder enabled observatiori of the balloon under pressure. Test Procedure: Three complete trial runs were made to determine the behavior of the apparatus. Sufficient dead weight was added to the piston to give it a tare weight of 200 1bs., then the balloon was inflated until the piston floated freely on the balloon, and manometer pressure readings were taken by two observers. Calibrated dead weights of,0 1bs. each were added in increments of 200 1bs. up to a maximum total load of 1400 1bs., (equalt'o a manometer indicated pressure of nearly 50 1bs. per sq. ft.), with manometer readings taken after each increment as. the piston floated freely, on tl$. balloon. Test Results: The test results are given in Tables 1, 2 and 3, where the manometer differential, manometer indicated pressure, and the actual dead load divided by the total surface area of the piston are recorded. ~he results are plotted in Figure 5. For all readings, the manometer pressure in pounds per square foot exceeded the total load divided by surface area of the piston by 2.3 to 4.6 pounds per square foot. Discussion of Test Results: -~-- --'--"-, The plastic window in the side of the loading chamber enabled observation of the behavior of the balloon at its contact with the piston surface, and showed clearly that full contact did not exist between the balloon and the total piston surface. (Note that failure to make contact along a one-inch perimeter reduces the effective piston area by more than six per cent).

246.2..3 ", I. This could account for part or all of the observed difference between manometer pressure and average loading pressure based on full piston area. However, while the contact area appeared to increase with an increasing load, the observed difference did not decrease. It should be noted, also, that consecutive readings taken at the same total load indicated a difference in manometer reading of 0.2 inches, or an observed pressure difference of more than one pound per square foot. (See Table 3, at 1400 lbs. total load.) The discrepancy may be due to differences in the height at which the piston was permitted to float (though this,~s limited to about a one-inch range), differences in frictional forces, or errors in reading the manometer. The space required to be filled by the meteorological balloon in the loading chamber is about half as great as the same balloon would be required to fill in the proposed wall test o Also, the uninflated balloon was horizontal in the lab test, and would be vertical on the wall test. It was observed that only a small part of the balloon actually came into play in the lab test, hence it 1s believed that the balloon would satisfactorily cover the required wall area. -...,,--- Conclusions: The following conclusions are drawn from the tests: 1. The elements of the loading and pressure measuring system behaved satisfactorily during the tests. The meteorological balloon exhibited toughness and durability, and gave indications that it would perform well at pressures greatly above those used in the laboratory tests.

246.2-4 While there was a definite qifference between the pressures indicated by the manometer and those obtained by dividing the total piston load by total piston area, the differences are sufficiently constant that a correction could be made in the actual 1!Jall test which would reduce the probable error to a minimum. A linear correction of 3.5 lbs. per sq. ft. is suggested. In the actual test, errors of the magnitude encountered in the trials are not likely to be of any consequence. The proposed procedure for testing a brick wall outlined in Fritz Engineering Laboratory Report 246.1 is recommended for use in any actual tests.

246.2 Table 1 Results of Trial Run No. 1 (1) Q) @ @ Load Total Manometer IvIanometer Total Load Dif- Increment Load Differen- Indicated.;.. Piston ference (lbs. ) (lbs.) tia1 Pressure Area (Ths./ftf) (inches) (lbs./ft.2) (lbs./ft?) Q)x 5.2 :- 30.7 -@ 200 200 1.8 9.36 6.51 2.85 200 400 3.15 16.38 13.03 3.35 200 600 4.4 22.88 19.54 3.34 200 800 5.7 29~64 26.06 3.58 200 1000 6.9 35.88 32.57 3.31 200 1200 8.2 42.64 39.09 3.55 200 1400 9835 48.62 45.60 30 02-200 1200 8.2 42 0 64 39.09 3.55-200 1000 6.9 35 0 88 32.57 3.31-200 800 5.7 29.64 26.06 3.58-200 600 4.4 22.88 19.54 3.34-200 400 3.15 16.38 13.03 3.35-200 200 1.7 8.84 6.51 2.33

246.2 Table 2 Results of Trial Run No. 2 CD @ (2) Load Total Manometer Hanometer Total Load Dif- Increment Load Differen- Indicated ~ Piston ferenc~ (lbs.) (lbs. )- tia1 Pressure Area (Ibs/ft. ) (inches) (lbs./ft. 2 ) (lbs./ft. 2 ) @x 5.2 @:- 30.7 -cv 0 0.08.42 0 0.42 200 200 1.80 9.36 6.51 2.85 100 300 2.42 12.58 9.77 2.81 100 400 3.12 16.22 13.03 3.19, 200 600 4.47 23.24 19.54-3.70 200 800 5.65 29.38 26.06 3.32 200 1000 6.91 35.93 32.57 3.36 200 1200 8.05 41.86 39.09 2.77 200 1400 9.22 47.94 45.60 2.34-200 1200 8.04 41.81 39.09 2.72-200 1000 6.86 35.67 32.57 3.10-200 800 5.48 28.50 26.06 2.44-200 600 4.23 22.00 19.54-2.46-200 400 3.06 15.91 13.03 2.88-200 200 1.78 9.26 6.51 2.75

246.2 Table 3 Results of Trial Run No. 3 CD cv Load Total Manometer Manometer Total Load Dif- Increment Load Differen- Indicated..;.. Piston ferenc~ (lbs.) (lbs.) tial Pressure Area (lbs./ft. ) (inches) (lbs./f't.2). (lbs./ft~) G)x 5.2 :- 30.7 -<2> 200 200 1.82 9.46 6.51 2.95 200 400 3.20 16.64 13.03 3.61 200 600 4.64 24.13 19.54 4.59 200 800 5.81 30.21 26.06 4.15 200 1000 6.94 36.09 32.57 3.52 200 1200 8.22 42.74 39.09 3.65 200 1400 9.36 48.67 45.60 3.07 1400 9.56 49.71 45.60 4.11-200 1200 8.13 42.28 39.09 3.19-200 1000 6.95 36.14 32.57 3.57-200 800 5.76 29.95 26.06 3.89-200 600 4.50 23.40 19.54 3.86-200 400 3.14 16.33 13.03 3.30-200 200 1.75 9.10 6.51 2.59

." -.! Rl...---.-.----.~-- I I,' Ii L- \" 1- --- 4-0 "I ~ I," Ii '1 ----- 3 -ii ----il i i 1 11. j l,h----_----!--l,. I / I.t=::==========!J ~ /' - ""<t / I. I I BP--LLOON CAVITY -,- ri--!---...l.!--h=!::=======::=!:::::#-+i.:...----ll, Fig. 1 CROSS-SECTION Ot" LOADING CHAMBER

Figure 2. Loading Chamber

,..'. Figure 3. Loading Chamber, View from Above

BLEEDER VALVE IO_O_~~PS_\ ~~_l»"~ SUPPLY SlOP VALVE _ 30 Inc,h MANOM ETER n+ i- +i I ± 1- I... I, - I -+-... -,.- -+- T +.--_.. ' A.,I 1 _. z:=-----. J BALLOON 0 /- FIG.4 DIAGRAM OF SUPPLY AND PRESSURE LINE ARRANGEMENT

a LJ Z w t.:l. t' -' :J w w~ Z. w ~ :J '" II' W Q. < II. r Il. ~ r ~ u z Z '"0 a W N Il. t- '" L, 0 (\j x o c <'i (\j a: 0 '1 <'l ci z 1.0 \0.., f zoo 400 12.00 1400