Unit 1 Flashcards
What is the structure of Wilkinson’s catalyst and what reaction does it catalyse?
[Rh(PPh3)3(Cl)]
It catalyses the hydrogenation of alkenes to the alkane
Calculate the NVE, oxidation state and dn configuration for Wilkinsons catalyst
16 e, Rh(I) and d8
What are the steps in the catalytic cycle for the hydrogenation of an alkene using Wilkinson’s catalyst?
- OA of H2
- Alkene coord
- MI (RDS) of an H onto the alkene
- RE → alkane product
What is the turn-over limiting step for the hydrogenation of an alkene using Wilkinson’s catalyst?
Migratory insertion
What factors effect the selectivity of Wilkinsons catalyst?
Unconjugated alkenes + alkynes hydrogenated
* Donor solvents (e.g. ethanol) speed up rxn since e density is increased → helps MI step (RDS)
* Less substituted alkenes preferred as highly substituted alkenes bind more weakly to M → MI has a higher activation barrier → decreases the rate
* Kinetic control: preference for the reduction of less substituted double bond
* high level of functional group tolerance → doesn’t reduce nitro groups
What is the productivity of a catalyst?
Mass of product per moles of catalyst per unit time, g/mmol.h or g/mol.h
What is a catalysts turnover number (TON) and formula?
How many times a catalyst completes a complete cycle of the reaction in a given time before becoming deactivated
TON = moles of product / moles of catalyst
What is the turnover frequency TOF of a catalyst?
Number of moles of product per moles of catalyst per unit time
TOF = TON / time (s⁻¹, h⁻¹, min⁻¹)
What is methanol carbonylation?
Conversion of methanol to acetic acid by the addition of CO
What are the two processes used for methanol carbonylation
- Monsanto process
- BP’s Cativa process
What is the catalyst for the Monsanto process of methanol carbonylation, its VE count, electronic configuration and geometry?
[Rh(CO)₂I₂]- , 16e, d8 and SP
Draw the mechanism for the Monsanto Process of methanol carbonylation
- Organometallic cycle:
* OA of methyl iodide (RDS)
* Migratory insertion of CO → intermediate 18 e- acyl complex
* Reductive elimination → acetic acid + regeneration of catalyst - Organic cycle:
* methanol reacts rapidly w/ HI - CH3I + H2O
* Acyl iodide reacts w/ H2O (hydrolysed) → acetic acid that we want as a product which regenerates HI
Why won’t methanol oxidatively add to Rh?
The hydroxyl group (-OH) is a weak leaving so it’s not good at OA which is an SN2 like reaction, need good LG + OH is not a good LG whereas I- = good LG
Explain the OA step in the Monsanto process?
SN2-like
* [Rh(CO)2I2]– is highly nucleophilic (-ve charge)
* Neutral analogues of [Rh(CO)2I2]– e.g. [Rh(AsPh3)2(CO)I] = 105 times less reactive
* Can be accelerated by electron donor ligands (e.g. PEt3) but these are unstable in real reactor conditions: PEt3 + HI -> [HPEt3]I after ligand dissociation
What are the main issues with the Monsanto process?
*↑ [HI] and [H₂O] is needed to stabilise the catalyst to prevent formation of insoluble Rh(III) salts
*↑ [H₂O] → CO loss via WGS rxn:
H₂O + CO → CO₂ + H₂ → ∼ 30% of CO to be lost, + H2 → product purity issues
*HI is v corrosive + requires expensive reactor metallurgy
What is the catalyst for BP’s Cativa process for methanol carbonylation?
[Ir(CO)₂I₂]-
Why is the OA of iodide methane in BP’s Cativa process is much faster than the Monsanto Process?
Ir has a higher e- density than Rh ∴ has greater nucleophilicity
OA is accelerated by stronger Ir-Me and Ir-I bond
Why is the migratory insertion of CO in BP’s Cativa process slower than the Monsanto Process?
Ir has a higher e- density than Rh ∴ has greater nucleophilicity
Migratory insertion is slowed by stronger Ir-Me bond
How is the migratory insertion step sped up in BP’s Cativa process?
Rate = k[Ir][CO]/[Iodide] ∴ removing iodide ligand from will speed up reaction
Promoter = group 3 halide, e.g. InCl3 or Ru-CO complexes
Acts as iodide ‘shuttle’→ forms neutral [Ir(CH3)(CO)3I2] complex
- Replace I w/ CO ∴ catalyst = neutral [Ir(CH3)(CO)3I2]
- Migratory insertion is fast since CO = good π acceptor ligand (removes e- density from M → makes Ir-Me bond weaker → faster rxn
- Add iodide back in + loose CO
Draw the mechanism for BP’s Cativa Process?
- OA of MeI (fast)
- Rather than slow MI
- Replace I w/ CO ∴ catalyst = neutral [Ir(CH3)(CO)3I2]
* via a promoter (lewis acid I= v big,soft anion ∴ needs fairly soft lewis acid or TM Ru-CO complexes
rather than slow MI
loss of Iodide via promoter
addition of CO - Fast CO MI
* Additon of iodide via promoter → back into main cycle
* Forms acetyl complex - Reductive elimination to regenerate catalyst
What are the advantages of of BP’s Cativa Process?
Catalyst = more stable at ↓ [H2O] – WGSR not a problem
IR = cheaper than Rh
Product is purer – fewer distillation columns required
What is hydroformylation?
Conversion of an alkene to a linear (desired) and branched aldehyde
Alkene + CO + H₂ → RCOH
What is the catalyst used in hydroformylation?
Pre-catalys = [Co(CO)₄(H)], Co (1), SP, d8
Active catalyst = [Co(CO)₃(H)]
Or Rh carbonyl complex
Draw the mechanism for the unmodified Cobalt catalyst used in hydroformylation
- Alkene coordination
Binds to M centre → TBP compound - 1,2 migratory insertion
* Co-H in cis orientation to Co-alkene
* Hydride undergoes MI w/ alkene → alkyl
* Side rxn: 2,1 migratory insertion of alkene → i-alkene (iso/ branched) - CO coordination
* 5 coordinate species - Migratory insertion
* Alkyl in cis orientation to carbonyl
* Alkyl undergoes MI w/ carbonyl → acyl
* Forms metallic ketone - OA of H2
* Concerted OA:
* H2 = non-polar
* Co (1) = low OS + 4 coordinate species - Reductive elimination
* Organic group in cis orientation to hydride
* Forms n-aldehyde product (linear)
What is the RDS of unmodified cobalt hydroformylation?
OA of H2
What is the rate equation of unmodified cobalt hydroformylation?
Rate = k [Co][alkene][H2][CO]-1
Why is the unmodified cobalt hydroformylation reaction run at high CO pressure and temperature despite the inverse [CO] order?
Inverse order in CO due to need for CO dissociation from pre-catalyst to form 16e active species
Implies rxn should run under ↓ [CO] → faster catalyst decomp + ↓ l:b selectivity (bc of competitive Co-catalysed alkene isomerisation)
Rxn = run at high CO P + ↑ T to ↑ productivity