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Mass flow rate

From Wikipedia, the free encyclopedia
Mass of a substance which passes per unit of time
Not to be confused withVolumetric flow rate.
Mass flow rate
Common symbols
m˙{\displaystyle {\dot {m}}}
SI unitkg/s
DimensionMT1{\displaystyle {\mathsf {MT^{-1}}}}

Inphysics andengineering,mass flow rate is therate at whichmass of a substance changes overtime. Itsunit iskilogram persecond (kg/s) inSI units, andslug per second orpound per second inUS customary units. The common symbol ism˙{\displaystyle {\dot {m}}} (pronounced "m-dot"), although sometimesμ{\displaystyle \mu } (Greek lowercasemu) is used.

Sometimes, mass flow rate as defined here is termed "mass flux" or "mass current".[a]Confusingly, "mass flow" is also a term formass flux, the rate of mass flow per unit of area.[2]

Formulation

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Mass flow rate is defined by thelimit[3][4]m˙=limΔt0ΔmΔt=dmdt,{\displaystyle {\dot {m}}=\lim _{\Delta t\to 0}{\frac {\Delta m}{\Delta t}}={\frac {dm}{dt}},}i.e., the flow of massΔm{\displaystyle \Delta m} through a surface per timeΔt{\displaystyle \Delta t}.

The overdot onm˙{\displaystyle {\dot {m}}} isNewton's notation for atime derivative. Since mass is ascalar quantity, the mass flow rate (the time derivative of mass) is also a scalar quantity. The change in mass is the amount that flowsafter crossing the boundary for some time duration, not the initial amount of mass at the boundary minus the final amount at the boundary, since the change in mass flowing through the area would be zero forsteady flow.

Alternative equations

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Illustration of volume flow rate. Mass flow rate can be calculated by multiplying the volume flow rate by the mass density of the fluid,ρ. The volume flow rate is calculated by multiplying the flow velocity of the mass elements,v, by the cross-sectional vector area,A.

Mass flow rate can also be calculated by

m˙=ρV˙=ρvA=jmA,{\displaystyle {\dot {m}}=\rho \cdot {\dot {V}}=\rho \cdot \mathbf {v} \cdot \mathbf {A} =\mathbf {j} _{\text{m}}\cdot \mathbf {A} ,}

where

The above equation is only true for a flat, plane area. In general, including cases where the area is curved, the equation becomes asurface integral:m˙=AρvdA=AjmdA.{\displaystyle {\dot {m}}=\iint _{A}\rho \mathbf {v} \cdot d\mathbf {A} =\iint _{A}\mathbf {j} _{\text{m}}\cdot d\mathbf {A} .}

Thearea required to calculate the mass flow rate is real or imaginary, flat or curved, either as a cross-sectional area or a surface, e.g. for substances passing through afilter or amembrane, the real surface is the (generally curved) surface area of the filter,macroscopically - ignoring the area spanned by the holes in the filter/membrane. The spaces would be cross-sectional areas. For liquids passing through a pipe, the area is the cross-section of the pipe, at the section considered. Thevector area is a combination of the magnitude of the area through which the mass passes through,A{\displaystyle A}, and aunit vector normal to the area,n^{\displaystyle \mathbf {\hat {n}} }. The relation isA=An^{\displaystyle \mathbf {A} =A\mathbf {\hat {n}} }.

The reason for thedot product is as follows. The only mass flowingthrough the cross-section is the amount normal to the area, i.e.parallel to the unit normal. This amount is

m˙=ρvAcosθ,{\displaystyle {\dot {m}}=\rho vA\cos \theta ,}

whereθ{\displaystyle \theta } is the angle between the unit normaln^{\displaystyle \mathbf {\hat {n}} } and the velocity of mass elements. The amount passing through the cross-section is reduced by the factorcosθ{\displaystyle \cos \theta }, asθ{\displaystyle \theta } increases less mass passes through. All mass which passes in tangential directions to the area, that isperpendicular to the unit normal,doesn't actually passthrough the area, so the mass passing through the area is zero. This occurs whenθ=π/2{\displaystyle \theta =\pi /2}:m˙=ρvAcos(π/2)=0.{\displaystyle {\dot {m}}=\rho vA\cos(\pi /2)=0.}These results are equivalent to the equation containing the dot product. Sometimes these equations are used to define the mass flow rate.

Considering flow through porous media, a special quantity, superficial mass flow rate, can be introduced. It is related withsuperficial velocity,vs{\displaystyle v_{s}}, with the following relationship:[5]m˙s=vsρ=m˙/A{\displaystyle {\dot {m}}_{s}=v_{s}\cdot \rho ={\dot {m}}/A}The quantity can be used inparticle Reynolds number ormass transfer coefficient calculation for fixed and fluidized bed systems.

Usage

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In the elementary form of thecontinuity equation for mass, inhydrodynamics:[6]ρ1v1A1=ρ2v2A2.{\displaystyle \rho _{1}\mathbf {v} _{1}\cdot \mathbf {A} _{1}=\rho _{2}\mathbf {v} _{2}\cdot \mathbf {A} _{2}.}

In elementary classical mechanics, mass flow rate is encountered when dealing withobjects of variable mass, such as a rocket ejecting spent fuel. Often, descriptions of such objects erroneously[7] invokeNewton's second lawF=d(mv)/dt{\displaystyle \mathbf {F} =d(m\mathbf {v} )/dt} by treating both the massm{\displaystyle m} and the velocityv{\displaystyle \mathbf {v} } as time-dependent and then applying the derivative product rule. A correct description of such an object requires the application of Newton's second law to the entire, constant-mass system consisting of both the object and its ejected mass.[7]

Mass flow rate can be used to calculate the energy flow rate of a fluid:[8]E˙=m˙e,{\displaystyle {\dot {E}}={\dot {m}}e,}wheree{\displaystyle e} is the unit mass energy of a system.

Energy flow rate has SI units ofkilojoule per second orkilowatt.

See also

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Notes

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  1. ^See, for example,Schaum's Outline of Fluid Mechanics.[1]

References

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  1. ^Fluid Mechanics, M. Potter, D. C. Wiggart, Schaum's Outlines, McGraw Hill (USA), 2008,ISBN 978-0-07-148781-8.
  2. ^"ISO 80000-4:2019 Quantities and units – Part 4: Mechanics".ISO. Retrieved2024-10-02.
  3. ^"Mass Flow Rate Fluids Flow Equation".Engineers Edge.
  4. ^"Mass Flow Rate".Glenn Research Center. NASA.
  5. ^Lindeburg M. R. Chemical Engineering Reference Manual for the PE Exam. – Professional Publications (CA), 2013.
  6. ^Essential Principles of Physics, P. M. Whelan, M. J. Hodgeson, 2nd Edition, 1978, John Murray,ISBN 0-7195-3382-1.
  7. ^abHalliday; Resnick (1977).Physics. Vol. 1. Wiley. p. 199.ISBN 978-0-471-03710-1.It is important to note that wecannot derive a general expression for Newton's second law for variable mass systems by treating the mass inF =dP/dt =d(Mv) as avariable. [...] Wecan useF =dP/dt to analyze variable mass systemsonly if we apply it to anentire system of constant mass having parts among which there is an interchange of mass. [Emphasis as in the original]
  8. ^Çengel, Yunus A.; Boles, Michael A. (2002).Thermodynamics : an engineering approach (4th ed.). Boston: McGraw-Hill.ISBN 0-07-238332-1.OCLC 45791449.
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