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Measuring principles Introduction 1
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Agenda Measurement 2. Flow technologies 3. Fluid properties
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Measurements | flow Certain quantity, which passes section of pipeline or channel in certain time whereby quantity is generic term for mass or volume on gases, volume is depending on pressure and temperature volume on liquids is not depending on pressure because they are not compressible
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Flow measurement | orientation
Purpose of measurement? Required accuracy, reproducibility? Pipe work lay-out (incl. flow profile, straight in-/outlet length)? Location, surrounding environment? Medium to be measured? Norms, rules, regulations, legislation? Engineering effects (process, pump capacity, personnel, etc.)? Calibration, recalibration? Financial consequences? Cost of ownership?
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Agenda 1. Measurement Flow technologies 3. Fluid properties
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Technologies | electromagnetic flowmeter
Used with electrically conductive fluids Based on Faraday’s law Electrode voltage directly proportional to fluid velocity
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Technologies | OPTIFLUX
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Technologies | coriolis mass flowmeter
Used with fluids and gases Based on Gaspard-Gustave Coriolis Amplitude phase shift is directly proportional with mass flow no flow mass flow
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Technologies | OPTIMASS
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Technologies | vortex flowmeter
Used with fluids and gases Based on Theodore von Karman Frequency of vortices is directly proportional with flow velocity
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Technologies | OPTISWIRL
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Technologies | ultrasonic flowmeter
Doppler used for fluids based on reflection of sound by entrained solids/air frequency shift is proportional with velocity (of entrained solids/air) Transit time used for fluids and gases based on ultrasonic signal travelling diagonally back and forth time difference is proportional with velocity
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Technologies | ultrasonic flowmeter
Inline single beam dual beam triple beam multi-beam Clamp-on stationary portable
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Technologies | OPTISONIC
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Technologies | variable are flowmeter
Used for fluids and gases Variable area have conical section where float is working Three forces are acting on float: gravity force and weight from top, volumetric flow from bottom Float is pushed up from flow and resides at point where differential pressure below upper and lower surface balances weight of float Movement from float is transported to local display
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Technologies | OPTIFLOAT
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Technologies | flow switches
Flow / no flow detection Fluid / gas detection Examples (flow / no flow) Examples (fluid / gas) mechanical, target or flap switch thermal level and flow switch thermal flow switch vibration fork variable area with contact capacitive sensor dP electromagnetic insertion
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Technologies | DW(M)
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Technologies | overview
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Agenda 1. Measurement 2. Flow technologies Fluid properties
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Flow measurement | fluid types
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Fluid Properties Density (r) Viscosity (n or h) Reynolds Number (Re)
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Fluid Properties - Density
Liquids: Density changes much less with Temperature and Pressure (effect nearly zero) Gases: Ideal gas law: r = p x M Z x R x T Where: P=pressure [N/m2] R=Universal gas constant [J /kmol K] Z= compressibility factor (about 1) r= Density [kg/m3] T= Temperature [K] ( K = degC ) M= mole mass of fluid [kg/kmol]
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Fluid Properties - Viscosity
Viscosity: the resistance to flow Dynamic viscosity h [N.s/m2, Pa.s, cP] Kinematic viscosity n [m2/s, cSt]) The relation between kinematic – and dynamic viscosity: n = h / r
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Fluid Properties - Viscosity
Different viscosity behaviour Dynamic viscosity Newtonian t=h.dv/dy Non-Newtonian Time independent Time dependent
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Fluid Properties - Viscosity
Newtonian: Ratio Shear stress with shear rate is constant Viscosity changes only with respect to temperature Examples: water, oil, gases Shear rate, dv/dy [s-1] Shear stress [N/m2] Newtonian
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Fluid Properties - Viscosity
Non-Newtonian & time independant viscosity varies with given temperature and (flow) velocity Dilatant : e.g. starch suspension Structurviscos : e. g. yoghurt, dressing, ketchup Plastic : e.g. tooth paste, hand cream
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Fluid Properties - Viscosity
Non-Newtonian & time dependant viscosity varies with …. Visco-elastic : e.g. polymer solutions, plastics, flour dough Thixotropic : e.g. pseudo plastic emulsions of soaps Rheopectic : e.g. printer ink
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Fluid Properties - Viscosity
Shear rate, dv/dy [s-1] Shear stress [N/m2] Newtonian Bingham fluid Dilatant/ Thixotrop Pseudo plastic
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Fluid Properties – Effect of viscosity and flow
Shape of flow profile is affected This may result in flow measurement errors (especially if you measure in one section Bingham Pseudoplastic Newtonian Dilatant
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Fluid Properties - Reynolds Number
Reynolds number describes the relation between - flow velocity (v) - diameter (D) - dynamic viscosity () and density (r) Re = v x D x r The Reynolds number is the only parameter that describes the flow Consequently the flow profile is described by the Reynolds number
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Re Reynolds number T R A N S I E Re < 2300 Laminar flow profile
Turbulent flow profile T R A N S I E
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Flow profile Reynolds Number: Turbulent flow Laminar flow
Turbulent flow - Flattened shape - Re > 4.000 Laminar flow - Parabolic shape - Re < 2.300 Transition region - in unfavourable process conditions e.g high viscosities, low flow rates < Re < Unpredictable measurement uncertainty Reynolds Number:
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Reynolds Number Water Always turbulent Re > 2.300
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Reynolds Number Oil Viscosity: 50 cSt Can have both Turbulent & Laminar flow profiles Viscosity ↑ Re ↓ Meter size ↑ Re ↑ Flow rate ↑ Re ↑
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