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Chemistry · Lesson

Homogeneous catalysis and industrial transformations

Compare selected hydrogenation, hydroformylation, carbonylation and metathesis nets. Connect these classes to documented applications while keeping stoichiometry, measured performance and an industrial process boundary distinct.

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By the end, you can

  • Balance the selected transformations and their product inventories.
  • Distinguish linear and branched hydroformylation products.
  • Calculate a restricted net atom-economy metric.
  • Explain why a balanced net or historical application does not prove a universal mechanism or process advantage.
01

An application is a specific process, rather than a universal metal property

Homogeneous catalysis places the catalyst and reacting species in the same phase under the relevant conditions; it does not require that the catalyst retain one unchanging molecular identity throughout. Ligand loss, solvent coordination, aggregation and activation can alter the active pool. Recovery and deactivation can be process concerns even when a proposed net regenerates the starting metal state.

Selected metal catalysts participate in hydrogenation, hydroformylation, carbonylation and carbon–carbon bond transformations. Metal-mediated catalysis also includes C–N, C–O and C–S bond formation in documented research. Those categories organize actual studies, but an element name alone does not predict conversion, tolerance or selectivity for every substrate and environment.

02

Hydrogenation adds a conserved hydrogen inventory

The selected formal propene net is C₃H₆+H₂→C₃H₈. One mol of desired propane corresponds to one mol of propene and one mol of H₂ in this net. A stipulated starting propene amount 0.800 mol and desired-product yield 0.800 therefore give 0.640 mol desired propane and 0.640 mol H₂ assigned to that desired product.

Yield alone does not specify how much of the remaining substrate is unreacted versus converted to other products, or whether other routes consumed additional H₂. It also does not identify the catalyst’s active state. RhCl(PPh₃)₃ is a documented coordination precursor for a class of homogeneous hydrogenations, with dissociation and other equilibria complicating a simple cycle. No operating conditions or universal substrate suitability are given here.

03

A carbonyl carbon enters a new aldehyde skeleton

Hydroformylation combines an alkene with CO and H₂ to give an aldehyde net. For propene, C₃H₆+CO+H₂→C₄H₈O preserves the atoms while adding one carbon from CO. The selected constitutional products are linear butanal and branched 2-methylpropanal; the shared formula does not make their connectivities identical.

In an invented product inventory of 100 mmol total aldehyde with linear/branched amount ratio 3:1, the amounts are 75 and 25 mmol. Their selected nets incorporate 100 mmol CO and 100 mmol H₂ in total. The ratio is a teaching input rather than a measured catalyst performance or an equilibrium constant.

A primary industrial account documents development of organophosphine–rhodium hydroformylation technology. That historical application does not establish current market figures or one selectivity for every ligand and condition. A simplified cobalt or rhodium cycle also does not prove that the same step controls every actual industrial rate.

04

A perfect formal atom ledger is a limited process metric

The selected methanol carbonylation net CH₄O+CO→C₂H₄O₂ gives acetic-acid composition. Using explicitly rounded atomic masses C=12, H=1, O=16 g mol⁻¹, the reactant molar masses are 32 and 28 and the desired product 60 g mol⁻¹. The formal net atom economy is 60/(32+28)× 100=100%.

That restricted metric includes only the stoichiometric atoms in the written desired net. It does not include catalyst, promoters, solvent, energy, separation, side products, material loss or actual conversion. One hundred percent here therefore cannot establish a sustainable or efficient overall plant. Compare metrics only with their stated boundaries.

The inspected 2000 primary industrial abstract describes methanol carbonylation with rhodium and a subsequent iridium Cativa process introduced in 1996. This is dated application evidence, not a present market estimate, a full inspected mechanism or a universal claim that one metal is superior for every process.

05

A formula exchange does not describe literal pairwise bond swapping

The selected propene metathesis net is 2C₃H₆→C₂H₄+C₄H₈, with ethene and but-2-ene as the chosen product identities. Consuming 0.400 mol propene in a stipulated complete net gives extent 0.200 mol and 0.200 mol of each product. The E/Z composition of the but-2-ene is unspecified.

The net conserves C₆H₁₂ per event, but does not mean that two intact alkenes directly swap fragments in one elementary collision. Original metathesis research summarized in an author’s Nobel lecture supports metal-alkylidene-mediated steps, including metallacyclic intermediates in the appropriate model. Catalyst activation and ligand loss are part of the actual chemistry.

A balanced net cannot by itself determine equilibrium extent, product ratio, functional-group tolerance or whether a polymerization is controlled. Distinguish an alkyl chain-growth insertion into a metal–carbon interaction from an initial metal–hydride insertion. Repeated generic M–H insertion alone is not a complete explanation of the growing metal–carbon chain.

Four selected transformation nets conserve different atom inventories
Selected classBalanced formal netTeaching resultBoundary
HydrogenationC₃H₆+H₂→C₃H₈0.800 mol substrate× 0.800 desired yield=0.640 mol desired productH₂ assigned to desired product 0.640 mol; other outcomes unspecified
HydroformylationC₃H₆+CO+H₂→C₄H₈O100 mmol aldehyde at 3:1 gives 75 linear/25 branchedBoth products share a formula but differ in connectivity
CarbonylationCH₄O+CO→C₂H₄O₂Formal atom economy 60/(32+28)=100%Only written net atoms; actual process inputs/losses excluded
Metathesis2C₃H₆→C₂H₄+C₄H₈0.400 mol propene gives 0.200 mol of each chosen productStipulated net; E/Z and actual equilibrium unspecified

Original formal nets and stipulated teaching inventories. The hydroformylation ratio and hydrogenation yield are invented. The carbonylation 100% value uses rounded C=12, H=1, O=16 and only the written stoichiometric net. No operating process, universal catalyst pathway, actual equilibrium extent or whole-process environmental metric is supplied.

Worked examples

Assign the hydrogen only to the specified desired net

Use 0.800 mol propene and stipulated desired yield 0.800.

  1. Desired propane=0.800× 0.800=0.640 mol.
  2. The selected net requires one H₂ per propane, assigning 0.640 mol H₂.
  3. Yield alone leaves the other substrate outcomes unspecified.

A desired-product stoichiometric inventory, without total gas-consumption or conversion proof.

Use the same formula with two connectivities

Use 100 mmol aldehyde and invented linear/branched ratio 3:1.

  1. Linear fraction 3/4 gives 75 mmol butanal.
  2. Branched fraction 1/4 gives 25 mmol 2-methylpropanal.
  3. Each selected product incorporates one CO and one H₂ per propene.

100 mmol CO and H₂ assigned to these products; the ratio is not a universal catalyst measurement.

Calculate only the chosen net atom economy

Use rounded C=12, H=1, O=16 in CH₄O+CO→C₂H₄O₂.

  1. Methanol 32 g mol⁻¹ and CO 28 g mol⁻¹ sum to 60 g mol⁻¹.
  2. Desired product mass 60 gives 60/60× 100=100%.
  3. Catalyst, other process inputs, losses and energy are outside this metric.

One hundred percent formal net atom economy, without a whole-process efficiency or sustainability conclusion.

Respect the two-substrate coefficient

Use stipulated complete consumption of 0.400 mol propene in the selected net.

  1. Extent=0.400/2=0.200 mol.
  2. Ethene amount 0.200 mol and but-2-ene amount 0.200 mol.
  3. C and H totals remain those of the consumed propene.

Balanced selected amounts, without E/Z, kinetic or direct pairwise-exchange claims.

Try it yourself

  1. A separate invented 100 mmol hydroformylation product pool has linear/branched ratio 4:1. Find both amounts.

    Show the answer and reasoning

    80 mmol linear and 20 mmol branched.

    Fractions 4/5 and 1/5 use the same total product pool; the ratio is still a stipulated teaching input.

  2. Use the same stipulated propene metathesis net with 0.600 mol propene completely consumed. Find the extent and each product amount.

    Show the answer and reasoning

    Extent 0.300 mol; each chosen product 0.300 mol.

    Divide by the propene coefficient two; product coefficients are each one.

  3. Why does 100% formal atom economy fail to specify a real plant’s material use or energy demand?

    Show the answer and reasoning

    Its boundary includes only the stoichiometric atoms in the written net.

    Catalysts, solvents, other inputs, recovery, losses and energy require separate process data.

  4. Does the shared formula C₄H₈O make butanal and 2-methylpropanal the same constitutional product?

    Show the answer and reasoning

    No.

    Their carbon connectivities differ despite the same atom inventory.

What to carry forward

  • Balance the product identities and the whole net.
  • Keep desired-product yield separate from other outcomes.
  • A shared formula does not determine connectivity.
  • State the boundary of an atom-economy calculation.
  • Application history and reaction mechanism need their own evidence.

References

Teaching resources and reference material supporting this lesson’s explanations and examples.

  1. CatalystInternational Union of Pure and Applied ChemistrySourceold.goldbook.iupac.orgRead source
  2. 14.3.5 Hydrogenation by Wilkinson’s CatalystKathryn HaasSourcechem.libretexts.orgRead source
  3. 14.3.2 HydroformylationKathryn Haas; selected cycle caption credits A.Vedernikov University of MarylandSourcechem.libretexts.orgRead source
  4. Industrial Low Pressure Hydroformylation: Forty-Five Years of Progress for the LP Oxo ProcessRichard Tudor; Atul ShahSourcetechnology.matthey.comRead source
  5. The Cativa Process for the Manufacture of Acetic AcidJane H. JonesSourcetechnology.matthey.comRead source
  6. Olefin-Metathesis Catalysts for the Preparation of Molecules and Materials (Nobel Lecture2005)Robert H. GrubbsSource · PDFits.caltech.eduRead source
  7. 10.2 Insertion and Elimination ReactionsM. S. Balakrishna; Prasenjit GhoshSourcechem.libretexts.orgRead source
  8. New Classes of Cross-CouplingsJohn F. Hartwig research groupSourcehartwig.cchem.berkeley.eduRead source