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Rate controlling step: halving the particle moves nothing, doubling the velocity does

Type three resistances on one basis. Halving the particle moves only the pore term and doubling the velocity only the film term, and two of the worked terms end too close to separate.

Live result

At the typed reference, the largest resistance is consistent with Surface kinetics. Halving size gives 1.14 times the rate and doubling velocity gives 1.09 times.
At the typed reference, the largest resistance is consistent with Surface kinetics. Halving size gives 1.14 times the rate and doubling velocity gives 1.09 times.

Typed resistances and response sweep

Sweep rail

Live chart
Three resistance terms at the typed referenceFilm resistance is 1, pore resistance is 1, and surface resistance is 4. The response is consistent with Surface kinetics.External film transport1Diffusion inside pores1Surface kinetics4024Resistance on your typed basis
Live chart
Observed rate across checked particle sizesThe particle rail contains 5 checked values and first changes at 2.0.330.711.1123Observed rate on typed basisParticle sizeFirst checked change

Try a scenario

Purpose

The mechanism request is outside this instrument and stops the finding.

Typed resistance case

Use one consistent resistance basis throughout. No unit conversion is applied.

Particle size sweep

External velocity sweep

Tracked answer and response fingerprint

ResistanceTyped value
External film transport1
Diffusion inside pores1
Surface kinetics4
Observed rate
1
Rate after halving particle size
1.143
Rate after doubling velocity
1.091
Candidates within tolerance
Surface kinetics
Other typed terms
External film transport, Diffusion inside pores

First checked changes

Particle size rail
First checked value: 2, No single resistance
Velocity rail
No change on the checked grid

The boundary is three typed resistance terms on one consistent basis, their reference size and velocity, two declared scaling exponents, and checked sweep grids. First changes are sampled values, not interpolated boundaries.

Here is the maths

▾

The formula, in words

Pore resistance scales with particle size raised to its exponent. Film resistance scales with the inverse velocity ratio raised to its exponent. Surface resistance stays fixed, and observed rate equals driving force divided by the sum of all three.

Rp=Rp,ref(ddref)pR_p = R_{p,\mathrm{ref}} \left(\frac{d}{d_{\mathrm{ref}}}\right)^pRp​=Rp,ref​(dref​d​)p

where RpR_pRp​ is pore resistance, Rp,refR_{p,\mathrm{ref}}Rp,ref​ its reference value, ddd the particle size, drefd_{\mathrm{ref}}dref​ the reference size, and ppp its exponent.

Rf=Rf,ref(vrefv)qR_f = R_{f,\mathrm{ref}} \left(\frac{v_{\mathrm{ref}}}{v}\right)^qRf​=Rf,ref​(vvref​​)q

where RfR_fRf​ is film resistance, Rf,refR_{f,\mathrm{ref}}Rf,ref​ its reference value, vrefv_{\mathrm{ref}}vref​ the reference velocity, vvv the velocity, and qqq its exponent.

r=FRf+Rp+Rsr = \frac{F}{R_f + R_p + R_s}r=Rf​+Rp​+Rs​F​

where rrr is the observed rate, FFF the driving force, and RsR_sRs​ surface resistance.

A worked example

At reference size 1 and velocity 1, type surface resistance 4, pore resistance 1, film resistance 1, and zero tie tolerance. Surface is the largest term.

At size 1.5, pore resistance is 1 times 1.5 squared, or 2.25, so surface remains largest.

At size 2, pore resistance reaches 4 and ties surface resistance. A 0.5 step therefore names size 2 as the first checked change and returns no single resistance.

What this does not model

The terms are typed on one basis. The model does not convert units, fit kinetic constants, represent every transport effect, or establish a physical mechanism.

Check it yourself

Halving particle size changes only the pore term. Doubling external velocity changes only the film term. Their two rate ratios are the response fingerprint.

Sources

  • NPTEL, Catalyst Science and Technology, public module on external and pore diffusion limitations
  • NPTEL, porous catalyst effectiveness factor
  • Open access review on mass transport in porous catalysts

Model version

1.0.0

The whole record prints. Your browser can save it as a PDF instead of printing it.

A response pattern is consistent with a typed resistance regime and establishes no mechanism. One sensitivity cannot settle rate control, and no resistance is fitted from plant data here.

Related

  • Levenspiel plot: mixed flow is the rectangle and plug flow the areaType four to eight rate points and the reciprocal rate curve draws itself. The area under it between two conversions is the ideal plug flow volume, 3.70 cubic metres on the worked figures. The rectangle standing on the exit rate is the ideal mixed flow volume, 8.00. Read the same five points in the other order and the area does not move while the rectangle falls to 1.60, which is why the reactor label decides nothing and the shape of the curve decides everything.
  • Multiple steady states: the branch depends on which way you arrivedType a small vessel model and one feed temperature. Over one interval there are three steady solutions, two of them stable, and the setting alone does not say which one you are on.

Resistance response record

Rate controlling step: halving the particle moves nothing, doubling the velocity does

Accepted inputs

Purpose
Describe pattern
Surface resistance
4
Pore resistance at reference
1
Film resistance at reference
1
Reference particle size
1
Reference external velocity
1
Particle size exponent
2
Velocity exponent
1
Driving force
6
Tie tolerance
0

Computed readings

Tracked answer and response fingerprint
Surface kinetics
Candidates within tolerance
Surface kinetics
Observed rate
1
Rate after halving particle size
1.143
Rate after doubling velocity
1.091
Particle size rail
2, No single resistance
Velocity rail
No change on the checked grid

Record fields

Model version
1.0.0
Boundary
The boundary is three typed resistance terms on one consistent basis, their reference size and velocity, two declared scaling exponents, and checked sweep grids. First changes are sampled values, not interpolated boundaries.
Sources
NPTEL, Catalyst Science and Technology, public module on external and pore diffusion limitations. NPTEL, porous catalyst effectiveness factor. Open access review on mass transport in porous catalysts

A response pattern is consistent with a typed resistance regime and establishes no mechanism. One sensitivity cannot settle rate control, and no resistance is fitted from plant data here.

Badr Alghamdi · badralghamdi.com/tools/whichever-step-was-slowest

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