ABSTRACT Firstly‚ the objectives of the experiment are to observe the characteristics of the flow and to compute the Reynold’s number. Using the Solteq Osbourne Reynold’s Demonstration (model FM 11) in this experiment‚ with different of water volume flowrate‚ the characteristics of the flow could be determined. The rock inside the stilling tank are to calm the inflow water so that there will not be any turbulence interfere with the experiment. The water inlet and outlet valve and dye injector utilized
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SUMMARY This experiment has four objectives to it of which are measuring the standard performance characteristics of the pump‚ comparing the performance characteristics for three different Reynolds numbers and explaining the effects observed and to also make predictions about the performance for a pump with an impeller diameter of 228mm using the data obtained in the experiments. This experiment was conducted under room temperature. The motor was first adjusted to 3000 rpm and the input valve which
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increases velocity and decrease pressure while an Orifice plate is a device which measures the rate of fluid flow. The Venturi Tube and Orifice Plate are basically used to determine flow rate in piping systems. Both of them used the same principle which is Bernoulli’s Equation. Based on Bernoulli’s Equation which says that there is a relationship between the pressure of the fluid and velocity of the fluid. In a flow metering device‚ the downstream pressure before an obstruction will be higher than the
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cerebrospinal fluid for laboratory analysis to measurepressure or instill medications 1. Preprocedure: * Obtain a written consent * Instruct the client to empty the bladder * Instruct the client to lie still during the procedure 2. Procedure: * Assist the client to assume a lateral recumbent position with knees flexed 3. Post procedure: * Instruct the client to lie flat‚ generally 4-8 hrs. to prevent spinal headache * Encourage fluids * Monitor
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constant (C) Must decrease (D) Can increase‚ decrease or remain constant 6. A coolant fluid at 30°C flows over a heated flat plate maintained at a constant temperature of 100°C. The boundary layer temperature distribution at a given location on the plate may be approximated as T = 30 + 70 exp ( −y ) where y (in m) is the distance normal to the plate and T is in °C. If thermal conductivity of the fluid is 1.0W/mK‚ the local convective heat transfer coefficient (in W/m2K) at that location will
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Types of Physical Evidence Found at a Crime Scene-Part 1 1. Bodily Fluids- (Blood‚ semen‚ and saliva). All suspected blood‚ semen‚ or saliva-liquid or dried animal or human-present in a form to suggest in relation to the offense or the people involved in a crime. This includes blood or semen dried onto fabrics or other objects‚ as well as cigarette butts that contain saliva residue. These substances are subjected to serological and biochemical analysis to determine their identity and possible origin
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Hydraulics – CIVL 2130 Conservation of Energy Aim The aim of this lab experiment is to observe the flow behaviour of water through a pipe of variable section. Firstly‚ we will investigate the interchange of pressure and kinetic energy at each diameter change. Secondly‚ we will study the application of this interchange to the flow metering devices. Lastly‚ energy losses due to friction and pressure effects are estimated. Experimental Apparatus [pic] Pre-lab Question Pressure varies
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and quantity‚ there is an inverse relationship between the volume and pressure for an ideal gas. Pascal’s Law states that if pressure is applied to a non-flowing fluid in a container‚ then that pressure is transmitted equally in all directions within the container. Archimedes’ principles is an upward force on an object immersed in a fluid (a liquid or a gas)‚ enabling it to float or at least to appear to become lighter. If the buoyancy exceeds the weight‚ then the object floats; if the weight exceeds
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run : 14.0 ppg Density of Completion/Packer fluid : 8.6 ppg Packer Depth : 11000 Expected gas gradient : 0.15 psi/ft Design Factors : (Burst) 1.1 (Collapse) 1.0 Solution: Burst Design - Production : Internal Load: Assuming that a leak occurs in the tubing at surface and that the closed in tubing head pressure (CITHP) is acting on the inside of the top of the casing. This pressure will then act on the column of packer fluid. The 9 5/8” casing is only exposed to these pressure
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engineering where I am in the list of top students of the branch with 9.02 GPA out of 10. In my undergraduate years I learned a lot of interesting subjects and acquired a strong background in the fundamentals of thermodynamics‚ heat and mass transfer‚ fluid mechanics‚ strength of materials‚ design of machine elements‚ theory of machines etc. I have also had an introduction to specified areas like AUTOCAD and
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