Knowledge card
Energy ODE
Mathematical Modelling — Fluid Dynamics & Heat TransferContinuum mechanics; boundary-layer similarity theory
Symbol
The second-order similarity-reduced energy equation; its formula is composed on demand from the conduction–radiation, convective, and unsteady terms.
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In words:equals(minusplus)divided by.
Open full derivation chain: 5 stepsDerivation
- 1
Open Step 1: Given / definition · The boundary-layer energy PDE [proposal eq. 3.25]: unsteady plus convective heat transport equa…
The boundary-layer energy PDE [proposal eq. 3.25]: unsteady plus convective heat transport equals the effective thermal diffusion — conduction and the radiative-flux divergence gathered as one diffusion block (the Rosseland-linearised radiation acts as an extra conduction).Given / definition Defining ruleThe starting relation of a derivation — the definition or established equation every later step transforms; it justifies no change itself.Level 0 · more availableBrief — named quantitiesAbout levels
Why the levels load one at a time
Only level 0 travels with this article. The complete expansion is several megabytes, so deeper levels are fetched one at a time when you ask for them — and how deep it goes is not known until you get there.
To go deeper still, open any quantity in the reading as its own concept card — it carries its own derivation and its own depth ladder.
How many levels remain is not yet known — the depth is discovered one level at a time.
- 2
Open Step 2: Similarity transformation · Substitute the maps into EVERY block [eqs. 3.56–3.57]: T−T∞ = (T_r−T∞)θ with T_r−T∞ = ΔT₀x/(1−γ…
Substitute the maps into EVERY block [eqs. 3.56–3.57]: T−T∞ = (T_r−T∞)θ with T_r−T∞ = ΔT₀x/(1−γt)², plus the velocity and temperature-derivative maps. ΔT₀ (K/m) is independent of the stretching rate c (1/s). Because the reference excess grows with x, u∂T/∂x survives as f′θ.Similarity transformation Defining ruleu(x, y, t) = U(x, t)·F(η), η = y/δ(x, t)A change of variables that collapses several independent variables into one similarity coordinate, reducing a PDE to an ODE; each substituted term splits into a dimensional scale times a dimensionless group.Substitution · η Operand nodeSimilarity Variable ηThe self-similar wall-normal coordinate that collapses the boundary layer; its definition is composed on demand from the rate constant, viscosity, and time.Substitution: The operand (a map or model) replaces the source directly.Open operand record: Substitution η
Substitution:L0L2Open term-change ledger: 3 records
Open record 1: ∂T/∂t → γ(ΔT₀x/(1−γt)³)(2θ+ηθ′/2)
Consumes:L0L1Produces:L0L1The similarity transform inserts T−T∞ = (T_r−T∞)θ(η) into ∂T/∂t; differentiation gives γΔT₀x/(1−γt)³ times 2θ+ηθ′/2.γ(ΔT₀x/(1−γt)³)(2θ+ηθ′/2)Resulting expressionSubstituted Unsteady HeatingThe unsteady heating after substitution — the independent heating amplitude and transient rate times the temperature group.Open record 2: u·∇T → (cΔT₀x/(1−γt)³)(f′θ−fθ′)
Consumes:L0L1Produces:L0L1The similarity transform inserts u=U_wf′ and T−T∞=(T_r−T∞)θ into both advection terms; because T_r−T∞=ΔT₀x/(1−γt)² grows with x, u∂T/∂x survives as f′θ.(cΔT₀x/(1−γt)³)(f′θ−fθ′)Resulting expressionSubstituted Convective Heat TransportThe convective heat transport after substitution, with the independent thermal amplitude ΔT₀.Open record 3: α∂²T/∂y²−(1/ρCp)∂q_r/∂y → k̃_eff[ΔT₀x/(1−γt)²][c/(ν_f(1−γt))]θ″
Consumes:L0L1Produces:L0L1The similarity transform inserts ∂²T/∂y²=(T_r−T∞)[c/(ν_f(1−γt))]θ″ into both conduction and linearised Rosseland diffusion.k̃_eff[ΔT₀x/(1−γt)²][c/(ν_f(1−γt))]θ″Resulting expressionSubstituted Effective DiffusionThe substituted conduction and radiative-conduction block uses the independent prescribed thermal excess and the similarity curvature factor; it carries the common scale cΔT₀x/(1−γt)³.Level 0 · more availableBrief — named quantitiesAbout levels
Why the levels load one at a time
Only level 0 travels with this article. The complete expansion is several megabytes, so deeper levels are fetched one at a time when you ask for them — and how deep it goes is not known until you get there.
To go deeper still, open any quantity in the reading as its own concept card — it carries its own derivation and its own depth ladder.
How many levels remain is not yet known — the depth is discovered one level at a time.
- 3
Open Step 3: Rearrange terms · Move every term to one side and set the equation to zero [eq. 3.60], the standard homogeneous f…
Move every term to one side and set the equation to zero [eq. 3.60], the standard homogeneous form: subtracting the effective-diffusion block collects the whole thermal balance against zero — the SAME three blocks, now equated to nought.Rearrange terms Defining rulea + b = c ⟺ a = c − bMoving terms across an equality by applying the same operation to both sides; the solution set is unchanged.Level 0 · more availableBrief — named quantitiesAbout levels
Why the levels load one at a time
Only level 0 travels with this article. The complete expansion is several megabytes, so deeper levels are fetched one at a time when you ask for them — and how deep it goes is not known until you get there.
To go deeper still, open any quantity in the reading as its own concept card — it carries its own derivation and its own depth ladder.
How many levels remain is not yet known — the depth is discovered one level at a time.
- 4
Open Step 4: Non-dimensionalisation · Divide by the thermal scale cΔT₀x/(1−γt)³, multiply the homogeneous balance by −1, and identify…
Divide by the thermal scale cΔT₀x/(1−γt)³, multiply the homogeneous balance by −1, and identify γ/c ≡ A and k₁ = (1/Pr)(1/φ_Cp)(φ_k + 4Rd/3). The canonical result is k₁θ″ + fθ′ − f′θ − A(2θ+ηθ′/2) = 0.Non-dimensionalisation Defining rulex* = x/x_ref ⟹ dimensionless groups (Π-theorem)Scaling every variable by a reference quantity so the equation is left with named dimensionless groups as its only coefficients.Divisor · cΔT₀x/(1−γt)³ Operand nodeConvective Thermal ScaleThe common temperature-rate scale of u∂T/∂x and v∂T/∂y after substitution.Divisor: The source is divided by the operand, leaving a named remainder.Open operand record: Divisor cΔT₀x/(1−γt)³
Divisor:L0L1Open term-change ledger: 3 records
Open record 1: γ(ΔT₀x/(1−γt)³)(2θ+ηθ′/2) → A(2θ+ηθ′/2)
Consumes:L0L1Produces:L0L1Dividing γΔT₀x(2θ+ηθ′/2)/(1−γt)³ by cΔT₀x/(1−γt)³ leaves γ/c=A.A(2θ+ηθ′/2)Resulting expressionThermal Unsteadiness TermThe transient heat term — the unsteadiness parameter times its temperature group.Open record 2: (cΔT₀x/(1−γt)³)(f′θ−fθ′) → fθ′−f′θ
Consumes:L0L1Produces:L0L1After division and the final sign reversal, the canonical advection block is fθ′−f′θ; expanding this block exposes both terms retained directly by the ODE root.fθ′−f′θResulting expressionCanonical Dimensionless Heat-advection BlockThe wall-normal contribution plus the opposite streamwise contribution after the homogeneous balance is multiplied by −1.Open record 3: k̃_eff[ΔT₀x/(1−γt)²][c/(ν_f(1−γt))]θ″ → k₁θ″
Consumes:L0L1Produces:L0L1Dividing the effective-diffusion block by the thermal scale and applying the definitions of Pr and Rd GATHERS conduction and radiation into the single verified coefficient k₁ = (1/Pr)(1/φ_Cp)(φ_k+4Rd/3).k₁θ″Resulting expressionThermal Diffusion TermThe conduction-plus-radiation term — the effective coefficient times the temperature curvature θ″.Level 0 · more availableBrief — named quantitiesAbout levels
Why the levels load one at a time
Only level 0 travels with this article. The complete expansion is several megabytes, so deeper levels are fetched one at a time when you ask for them — and how deep it goes is not known until you get there.
To go deeper still, open any quantity in the reading as its own concept card — it carries its own derivation and its own depth ladder.
How many levels remain is not yet known — the depth is discovered one level at a time.
- ★
Open Step 5: Separation of variables · Isolate the highest derivative: factor θ″ out of the thermal-diffusion term and divide the bala…
Isolate the highest derivative: factor θ″ out of the thermal-diffusion term and divide the balance by its coefficient, giving the explicit normal form θ″ = … that the numerical solver marches.Separation of variables Defining ruledy/dx = f(x)g(y) ⟹ ∫dy/g(y) = ∫f(x)dxSplitting a differential equation so each side carries one variable, then integrating both sides.Divisor · k₁ Operand nodeEffective Thermal Diffusivity CoefficientThe leading coefficient of the energy ODE — (1/Pr)(1/φ_Cp)(φ_k + 4Rd/3). Verified grouping: 1/φ_Cp divides the WHOLE diffusive group, because conduction AND radiation are both stored against the mixture’s volumetric heat capacity.Divisor: The source is divided by the operand, leaving a named remainder.Open term-change ledger: 2 records
Open record 1: k₁θ″ → k₁
Consumes:L0Produces:L0k₁The thermal-diffusion term k₁θ″ separates into the common factor θ″ (isolated on the left as the highest derivative) and its coefficient k₁, by which the isolated balance is divided.Open record 2: fθ′−f′θ → fθ′ + f′θ
Consumes:L0Produces:L0L0The heat-advection block fθ′−f′θ, moved to the right and subtracted, is written out as its two terms −fθ′+f′θ so the explicit form stays unambiguous.Level 0 · more availableBrief — named quantitiesAbout levels
Why the levels load one at a time
Only level 0 travels with this article. The complete expansion is several megabytes, so deeper levels are fetched one at a time when you ask for them — and how deep it goes is not known until you get there.
To go deeper still, open any quantity in the reading as its own concept card — it carries its own derivation and its own depth ladder.
How many levels remain is not yet known — the depth is discovered one level at a time.
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Domain Analysis
Unit status, dimensional trails, per-step checks, and custom unit expressions.
Domain Analysis
Unit status, dimensional trails, per-step checks, and custom unit expressions.
Step-by-step unit check (5 steps)
Step 1 given
Expand checked this step.Step 2 similarity_transform
Expand checked this step.Step 3 rearrange
Expand checked this step.Step 4 non_dimensionalise
Expand checked this step.Step 5 separation_of_variables
Expand checked this step.
Try your own — the unit calculator
Ever wondered whether a formula “adds up”? This tool answers one plain question: do the units match? Pick a couple of quantities (distance, time, a speed…), join them with ×, ÷, +, or =, and press Run. It works out the resulting unit — for example distance ÷ time gives a speed, LT⁻¹ (metres per second) — and flags anything that can’t be right, like adding a length to a time.
Reads as: θ″
“θ″” is analysed by expanding its full defining equation (its children and their relations), not as a bare symbol. Use Check this concept’s units above for the same result.
Mathematical Analysis
Object type, lawful operations, conditions, comparisons, and derivation-step checks.
Mathematical Analysis
Object type, lawful operations, conditions, comparisons, and derivation-step checks.
Check one step at a time (5 steps)
Step 1 — given
Step 2 — similarity transform
Step 3 — rearrange
Step 4 — non dimensionalise
Step 5 — separation of variables
Essence
S1The SAME balance after substitution: substituted unsteady plus substituted convective heat transport equals the substituted effective diffusion.
- S1.1essenceThe sum of γ(ΔT₀x/(1−γt)³)(2θ+ηθ′/2) and (cΔT₀x/(1−γt)³)(f′θ−fθ′). [1.1]
- S1.2essence(γ(ΔT₀x/(1−γt)³)(2θ+ηθ′/2) + (cΔT₀x/(1−γt)³)(f′θ−fθ′)) set equal to k̃_eff[ΔT₀x/(1−γt)²][c/(ν_f(1−γt))]θ″. [1.1]
S2The substituted thermal balance in homogeneous form: substituted unsteady plus substituted convective heat transport minus the substituted effective diffusion equals zero.
- S2.1essenceThe sum of γ(ΔT₀x/(1−γt)³)(2θ+ηθ′/2) and (cΔT₀x/(1−γt)³)(f′θ−fθ′). [1.1]
- S2.2essence(γ(ΔT₀x/(1−γt)³)(2θ+ηθ′/2) + (cΔT₀x/(1−γt)³)(f′θ−fθ′)) reduced by k̃_eff[ΔT₀x/(1−γt)²][c/(ν_f(1−γt))]θ″. [1.1]
- S2.3essence((γ(ΔT₀x/(1−γt)³)(2θ+ηθ′/2) + (cΔT₀x/(1−γt)³)(f′θ−fθ′)) − k̃_eff[ΔT₀x/(1−γt)²][c/(ν_f(1−γt))]θ″) set equal to 0. [1.1]
S3Isolate the highest derivative: factor θ″ out of the thermal-diffusion term and divide the balance by its coefficient, giving the explicit normal form θ″ = … that the numerical solver marches.
- S3.1essenceA(2θ+ηθ′/2) reduced by fθ′.
- S3.2essenceThe sum of (A(2θ+ηθ′/2) − fθ′) and f′θ.
- S3.3essence((A(2θ+ηθ′/2) − fθ′) + f′θ) divided by k₁.
- S3.4essenceθ″ set equal to (((A(2θ+ηθ′/2) − fθ′) + f′θ) / k₁).
Dimension I
Definition
What it is — and what it is not
- What it is
- Wisdoms
- Attributes
- S7Balances effective conduction and thermal radiation against convective heating and unsteadiness; the equation is composed on demand. [1.1]
Dimension II
In practice
How to deal with it
- Consequences
- S8The convective term carries f, coupling it to the momentum ODE.