"Fluid dynamics" Essays and Research Papers

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    Psv Criteria

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    NORSOK STANDARD P-001 Edition 5‚ Sep. 2006 Process design This NORSOK standard is developed with broad petroleum industry participation by interested parties in the Norwegian petroleum industry and is owned by the Norwegian petroleum industry represented by The Norwegian Oil Industry Association (OLF) and The Federation of Norwegian Industry. Please note that whilst every effort has been made to ensure the accuracy of this NORSOK standard‚ neither OLF nor The Federation of Norwegian Industry or

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    Venturi Meter

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    both the Venturi Meter and the Orifice Meter. Theory: A Venturi meter and an Orifice are both instruments used for measuring the rate of discharge for a fluid flowing in a pipe. These instruments are based on the same principle which states the following: "The pressure difference between any two points on a tapering pipe through which the fluid is flowing depends on the change of levels and on the change in velocities and therefore on the volume rate of flow" Where the flow is led to narrow cross

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    Friction Loss Along Pipe

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    occurs in the pipe flow due to viscous effects generated by the surface of the 3mm ID pipe. It is understandable that friction loss is a major loss rather than minor loss including energy lost due to obstructions. Loss of head occurred by the mixing of fluid which occurs at fittings such as bends or valves‚ and also frictional resistance at the pipe wall. Besides‚ the major part of the head loss will be due to the local mixing near the fittings. Figure 1.0 Illustration of Fully Developed Flow along a

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    length 3.5” is mounted inside a wind tunnel running at a suitable at a suitable wind speed. Pressure at different points on the surface of the aerofoil is measured using wall tappings. These tappings are connected to a multi-tube manometer. The dynamic pressure is measure using the tunnel reference pressure (hs) and atmospheric pressure (ha). Pressure readings will be taken for angles of attack from -1° to 16° at intervals of 5°. Theory: The Pressure coefficient can be calculated from the manometer

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    Absorber

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    operated co-currently or counter currently. In the former‚ both fluids involved are fed into the unit from the same point causing them to flow along each other. In counter current operation‚ the liquid is fed at the top of the absorber‚ flows downwards and contacts with rising gas fed from beneath. Absorbers can be classified as tray towers or packed towers. In tray towers‚ the interfacial surface area required for contact between the two fluids is provided by stepwisely arranged plates or trays whereas

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    Hazop study

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    validating engineering system (P&I) drawings designed for warships. INTRODUCTION Piping is an important element of every stage of project design‚ purchasing and construction. Piping systems are comparable to the veins and arteries through which fluids‚ vapours‚ slurries‚ solids etc flow under varying conditions. Piping networks onboard warships are subjected to the severest conditions of their process/system such as high pressure‚ temperature‚ flow and a combination of all these. In addition to

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    Research Council‚ 1994: Alternatives for ground water cleanup‚ National Academy Press‚ Washington‚ D National Research Council‚ 1996: Rock Fracture and Fracture Flow: Contemporary Understanding and Applications‚ Committee on Fracture Characterization and Fluid Flow‚ National Academy Press‚ Parker‚ J. C. and R. J. Lenhard‚ 1987: A model for hysteretic constitutive relations governing multiphase flow: 1 Parker‚ J. C. and R. J. Lenhard‚ 1990: Determining three-phase permeability-saturation-pressure relations

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    LabReportFULL EXP4

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    1.0 SUMMARY: The reactor test rig (RTR) experiment is purposely done to compare the performance of single stage CSTR‚ 3-stages CSTRs and PFR. The solutions that been used in this experiment is dilution of 0.1M of sodium hydroxide‚ NaOH and 0.1M of ethyl acetate‚ Et(Ac) to 60L. There are four common measures of reactor performance and the most important one is conversion. Then the speed is set to be at 300rpm and reading is taken every 5 minutes till the outlet conductivity remains constant. From

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    MODELING LEACHATE MIGRATION FROM A LANDFILL December‚ 2003 1 INTRODUCTION A two-dimensional‚ steady state transport modeling using MODFLOW/CTRAN was carried out following the particle tracking calculations to simulate potential contamination for leachate migration from Gibraltar landfill. Gibraltar landfill was a disposal waste site in Bogotá (Colombia) until 1988. The site presented problems related to contamination for leachate migration after its closure‚ since the operation

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    impact of jet

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    References: 1. Massey‚ B.S. (1989). Mechanics of Fluids. 6th Ed‚ Chapman & Hall. 2. White F.M. (1994). Fluid Mechanics. 3rd Ed.‚ McGraw-Hill.

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