Catalyst Selectivity from Competing Paths
Branching barriers, intermediate coverage and product desorption
Lesson 4213 of 4,500 · Catalyst Design and Comparison
Learning objectives
- Calculate selectivity for simple parallel paths
- Explain how coverage and desorption alter product distribution
- Design experiments that distinguish intrinsic branching from secondary reactions
Introduction
A catalyst need not produce only one product. At a branching intermediate, two elementary pathways compete; afterward, a desired product may react again before it leaves the surface. Selectivity therefore reflects branching barriers, the populations of intermediates and how quickly products desorb. Measuring conversion without a full product balance can conceal a fast but wasteful catalyst.
Core explanation
Consider A → P and A → Q , with P desired. In a simple parallel, irreversible, first-order model, formation rates are rP = kPθA and rQ = kQθA. If both products are stable and one-to-one in A, selectivity to P is rP/(rP + rQ) = kP/(kP + kQ). Lowering the barrier of the P route can improve selectivity. However, real networks may have different site requirements, reversible steps or coverage-dependent barriers, so the neat ratio is an approximation.
Surface coverage can change branching. One path may need two adjacent vacant sites while another needs one; high adsorbate coverage can suppress the pair-dependent route. Reactants or spectator species can stabilise one transition state through lateral interactions. Temperature can alter the relative rates because pathways have different activation energies and entropies. Feed composition and potential may change the active surface itself. Consequently, selectivity reported without operating conditions is incomplete.
Product release can be as important as the initial branch. If P desorbs quickly, P escapes. If P remains bound, it may convert to Q through an overreaction. In a reactor, even desorbed P can readsorb and react further at high conversion. A catalyst might make P selectively at low conversion but deliver mostly Q after long residence time. To identify intrinsic branching, measure at several conversions and extrapolate toward low conversion where secondary chemistry is reduced.
Use an atom balance appropriate to stoichiometry. For carbon products, carbon selectivity is often clearer than raw mole fraction: a C₂ product contains twice as many carbon atoms as a C₁ product. Analyze gas, liquid and adsorbed or deposited carbon where relevant. Incomplete mass balance means unmeasured products can make apparent selectivity too high. ACS microkinetic research on activity and selectivity illustrates how networks, coverage and experiment must be connected.
Step-by-step reasoning
1. Draw all plausible paths from a common intermediate and note later product reactions. 2. Define selectivity on a conserved-atom basis and close the product balance. 3. Compare rates at equal conversion and controlled temperature, feed and transport. 4. Test product addition and residence-time variation for secondary reactions. 5. Use mechanism and coverage evidence to explain changes in branching.
Visual explanation
Draw A at a fork: one arrow to P , another to Q . From P , draw a fast arrow to desorbed P and a competing arrow to Q . Above each arrow mark an activation barrier; below, mark site requirements. Draw a selectivity-to-P curve that falls as conversion rises if secondary P → Q becomes important.
Real-world analogy
A rail junction sends passengers to two destinations; the switching mechanism controls the first branch. But passengers sent toward P can still transfer to Q at the next station unless they exit promptly. Catalyst selectivity similarly depends both on initial path choice and on product release. The analogy cannot represent molecular stoichiometry or adsorption energies, which must be calculated separately.
Real-world example
In a partial oxidation, the desired oxygenated product can be further oxidised. One catalyst activates the starting hydrocarbon rapidly but holds the oxygenated intermediate strongly, giving more complete oxidation at long contact time. A second catalyst may release the partial-oxidation product more readily. Researchers compare carbon selectivity at matched conversion and vary contact time to identify whether the first catalyst's lower selectivity comes from initial branching or subsequent product oxidation.
Why?
Why does equal conversion matter when comparing selectivity? If secondary reactions increase with residence time, a high-conversion experiment naturally exposes product to further reaction. Comparing it with a low-conversion run confounds catalyst choice with reaction extent. A series of matched-conversion measurements is more informative.
Common misconception
“The catalyst with highest conversion is most selective” is false. “The lower branch barrier alone fixes final product distribution” ignores product desorption and later chemistry. “A chromatogram showing only P means 100% selectivity” may overlook undetected gases, soluble species or deposits. “Mole selectivity is always the correct basis” fails when products contain different numbers of conserved atoms.
Worked example
Under a simple one-to-one parallel model, kP = 4 s⁻¹ and kQ = 1 s⁻¹, giving initial selectivity SP = 4/(4 + 1) = 0.80. If a catalyst modification doubles kP while leaving kQ unchanged, the simplified initial selectivity becomes 8/9 ≈ 0.889. But suppose 25% of initially formed P further converts to Q before leaving the reactor. Of 100 converted A units, initial formation is 80 P and 20 Q; secondary conversion changes this to 60 P and 40 Q, so final selectivity is 60%. The 80% branching selectivity and 60% outlet selectivity answer different questions. A residence-time test can reveal the secondary step.
Quick check
1. Why can outlet selectivity differ from selectivity at the first branching intermediate? Answer: Initially formed product may remain bound, readsorb or react further before leaving the reactor.
Exam focus
Calculate selectivity on a stated atom basis and distinguish parallel from consecutive pathways. Explain why equal conversion, product balance and residence-time variation matter. Give one way coverage can alter the relative rate of competing paths.
Advanced insight
Rate control for selectivity need not match rate control for total activity. A transition state that barely affects overall conversion may strongly shift the ratio of two product fluxes. Catalyst optimisation should therefore compute or measure sensitivities for the desired-product rate and undesired-product rate separately, then consider separation and waste burdens.
Summary
Selectivity emerges from competing paths, site populations and product release. A complete atom balance and conversion-controlled experiments are essential to distinguish intrinsic branching from downstream overreaction.
Practice questions
1. If rP = 3 mmol/s and rQ = 2 mmol/s from the same one-to-one intermediate, what is initial selectivity to P? Answer: 3/(3 + 2) = 60%. 2. Why can fast product desorption improve selectivity? Answer: It removes desired product from sites where it could undergo further unwanted reaction. 3. What does falling P selectivity at increasing residence time suggest? Answer: Secondary conversion of P or changing surface coverage is possible and should be tested. 4. Why use carbon selectivity for products with different carbon counts? Answer: It tracks the fraction of converted carbon reaching each product, enabling a conserved-atom balance.