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Continuity Equation (Mass Balance)

States that mass flow rate is conserved along a pipe or duct, linking cross-sectional area and velocity at two points.

Chemical EngineeringFluid MechanicsProcess Design

Continuity Equation Calculatorρ₁ · A₁ · v₁ = ρ₂ · A₂ · v₂

ṁ = ρ · A · v
ρ density (kg/m³)  ·  A area (m²)  ·  v velocity (m/s)
⟹ ṁρ, A, v
kg/m³
m/s
kg/m³
m/s
Solve for:
Mass Flow Rate (ṁ)
✓ Copied!
Mass Flow Rate
Low (<1) Medium (1–10) High (10–50) Very High (>50)
v₂ vs. A₂fixed ρ₁, A₁, v₁, ρ₂
v₂(A₂) Computed point
ṁ = ρ₁·A₁·v₁ = ρ₂·A₂·v₂  ·  Mass flow rate (kg/s)

Interpretation

Continuity equation: ρ₁A₁v₁ = ρ₂A₂v₂ for mass conservation. For incompressible flow, A₁v₁ = A₂v₂. Example: Area reduced from 0.01 to 0.005 m² → velocity doubles if density constant.

rho1 * A1 * v1 = rho2 * A2 * v2
Continuity Equation (Mass Balance)

Variables

SymbolQuantityUnit
rhoFluid densitykg/m3
ACross-sectional aream2
vAverage velocitym/s

What it means

The continuity equation expresses the conservation of mass for a fluid flowing in a conduit. For steady, one‑dimensional flow, it states that the mass flow rate is constant along the flow path: ρ₁ A₁ v₁ = ρ₂ A₂ v₂. If the fluid is incompressible (density constant), this simplifies to A₁ v₁ = A₂ v₂, meaning that the volumetric flow rate is constant. This principle is used to determine velocity changes when the cross‑sectional area changes, e.g., in a converging nozzle or a pipe of varying diameter. It is the basis for many flow measurement devices like venturi meters and orifice plates. The continuity equation is also applied to multi‑component mixtures and reactive flows, where it is extended with source terms. In engineering, it is essential for designing piping networks, sizing pumps, and analysing distribution systems. The equation is a fundamental law of fluid mechanics and is also used in other fields like acoustics and magnetohydrodynamics.

Worked example

Continuity Equation – Two Examples

Real‑World
Scenario: Water flows in a pipe with A₁ = 0.05 m², v₁ = 2 m/s. The pipe narrows to A₂ = 0.02 m². Find v₂.
ParameterValue
ρ1000 kg/m³
A₁0.05 m²
v₁2 m/s
A₂0.02 m²
1v₂ = A₁v₁/A₂ = 0.05×2/0.02 = 5 m/s
Result v₂ = 5 m/s ✓ Faster
Scenario: A₁ = 0.1 m², v₁ = 1 m/s, A₂ = 0.05 m². Compute v₂.
ParameterValue
A₁0.1 m²
v₁1 m/s
A₂0.05 m²
1v₂ = 0.1×1/0.05 = 2 m/s
Result v₂ = 2 m/s ✓ Mass conserved
Key insight: Mass flow rate is conserved – velocity increases when area decreases.

Common mistakes

  • Density ρ: For incompressible flow, ρ is constant; for compressible, use the appropriate average density.
  • Area and velocity: A and v are cross‑sectional area and average velocity normal to that area.
  • Mass flow rate: The product ρAv gives mass flow rate (kg/s) – ensure units are consistent.
  • Steady flow: The equation assumes steady, one‑dimensional flow; for unsteady or multi‑dimensional, use differential form.
  • Different streams: For branched systems, apply the continuity equation at each junction.

Applications

The continuity equation, ρ₁A₁v₁ = ρ₂A₂v₂, embodies the conservation of mass in fluid flow. For incompressible flow, it simplifies to A₁v₁ = A₂v₂, stating that the volumetric flow rate is constant along a pipe. This principle is used to design piping networks, to determine velocities at different cross‑sections, and to size nozzles and diffusers. In chemical engineering, it is essential for designing reactors and separators where multiple streams merge or split. The continuity equation also underpins the analysis of compressible flows, such as in gas pipelines and supersonic nozzles, where density changes must be accounted for. Engineers apply this equation to ensure that mass is conserved in all process calculations, from simple water distribution to complex chemical plant simulations.

  • Sizing of pipe systems and ductwork
  • Design of mixing and splitting junctions
  • Nozzle and diffuser design for flow acceleration/deceleration
  • Compressible flow analysis (gas pipelines, jet engines)
  • Process simulation and mass balance calculations

Frequently Asked Questions

Q01What is the continuity equation and what does it represent?
A01

The continuity equation is a statement of conservation of mass for a fluid flow. For steady, one‑dimensional flow, it is ρ₁·A₁·v₁ = ρ₂·A₂·v₂. For incompressible flow (ρ constant), it simplifies to A₁·v₁ = A₂·v₂.

Q02What are the assumptions of the continuity equation?
A02

  • Steady flow (no accumulation).
  • No sources or sinks of mass.
  • Flow is normal to the cross‑sectional area.
  • For the incompressible form, density is constant.

Q03What are the common mistakes when applying the continuity equation?
A03

  • Applying the incompressible form to gases where density changes significantly.
  • Using the wrong area (e.g., using the outer diameter instead of the inner flow area).
  • Ignoring the effect of temperature or pressure on density.
  • Not accounting for multiple inlets or outlets.

Q04How does the continuity equation relate to flow rate?
A04

The volumetric flow rate Q = A·v (for incompressible). The mass flow rate ṁ = ρ·A·v = ρ·Q. The continuity equation ensures ṁ is conserved along a pipe.

Q05What happens to velocity when the pipe diameter changes?
A05

For incompressible flow, if the diameter decreases, the area decreases, so velocity must increase to maintain constant Q. This is the principle behind nozzles and constrictions.

Q06How do you apply the continuity equation to a branching pipe network?
A06

At a junction, the sum of mass flow rates entering equals the sum leaving: Σṁ_in = Σṁ_out. For incompressible flow, ΣQ_in = ΣQ_out.

Q07What is the difference between the continuity equation in differential and integral form?
A07

The integral form is used for control volumes: ṁ_in – ṁ_out = dm/dt. The differential form is ∂ρ/∂t + ∇·(ρv) = 0, which describes the conservation law at a point.

Q08What are the applications of the continuity equation?
A08

  • Design of pipe networks.
  • Analysis of flow through compressors and turbines.
  • Mixing and blending operations.
  • Environmental fluid dynamics (river flow).