L11: Carbonylation of methanol, alkene polymerisation Flashcards
1
Q
How is acetic acid produced industrially?
A
- Direct carbonylation of methanol
- Monsanto; original process using Rhodium catalyst
- Cativa; modern version with similar conditions but a cheaper Iridium catalyst, w/ an additional promoter
2
Q
Monsanto process: processes in each cycle
A
- Cycles are inter-dependent (iodide and carbonylation cycles)
- Iodide cycle…
A. Nucleophilic attack by I-, substitutes for OH2+ in acidic conditions
B. Hydrolysis of acetyl iodide - Carbonylation…
1. Oxidative addition of CH3I (RDS)
2. Methyl migration
3. Carbonyl addition
4. Reductive elimination
3
Q
Monsanto process: explain the use of Me-I and omission of R3P ligand
A
- Me-I is preferred over other alkyl halides since rate of oxidative addition to 16 e- M centres depends on R-X bond strength
- R-I bond is weaker than R-Br
- Although R3P ligands would make the M centre more e- rich and speed up oxidative addition, but under the reaction conditions the modified catalyst soon reverts so is too short-lived to be useful
4
Q
Why is Rh preferred over other group 9 metals in the Monsanto process
A
- Cobalt is much less active so higher temperature and pressure would be required for MeOH carbonylation
- Iridium would have a much higher oxidative addition step (~150x) but the subsequent methyl migration becomes the rds as rates decrease from 5d to 3d due to decreasing M-R bond strength up the group (3000x slower for Ir vs Rh)
5
Q
Promoter in cativa process
A
- Ru(CO)4I2 or Hg2
- Dramatically accelerates methyl migration
- Acts as a reversible iodide acceptor and aids substitution of an iodide ligand prior to Me migration
6
Q
Alkene polymerisation catalysts (prior and post Ziegler Natta)
A
- Originally, LDPE was produced form ethene using radical polymerisation via R2O2 initiator a 2000 atm and 200 degrees
- LDPE is of poor quality and branching is inevitable
- Ziegler Natta produced HDPE from ethene (LA catalyst, 25 degrees, 1 atm) and isotactic polypropylene from propene (same conditions)
7
Q
Z-N catalyst; type of catalyst, formation, role of AlEt3, key features
A
- Heterogenous, surface sites of solid TiCl3 particles formed by in situ reduction of TiCl4 w/ AlEt3, which reduces it and activates the surface by exchange of Cl for Et
- Early transition M centre
- alkyl group
- vacant coordination site
8
Q
Mechanism employed by Z-N catalyst
A
- Cossee-Arlman mechanism
- Termination of the alkyl chain is either beta-elimination or cleavage of M-R using H2
- Regulating the amount of H2 in the feed gives some control over polymers RMM
9
Q
Why does Z-N catalysis produce highly stereoregular propylene?
A
- ‘Head-to-tail’ coupling of the propene units occurs because steric interactions at rhe M centre strongly favour primary M alkyl formation
- Only isotactic PPE is formed at the active sites on the TiCl3 surface
10
Q
Metallocene catalysts for Z-N
A
- Homogenous analogues for Z-N system
- Metallocene dihalides of Ti, Zr, Hf activated by MAO are highly active for alkene polymerisation (Zr best)
- MAO: methylaluminoxane
11
Q
Exception to rule: atactic polymers from Z-N
A
- Catalysed by (Cp)2MCl2 pre-catalysts; no control over tacticity
12
Q
ansa-metallocenes in Z-N
A
- Used to control polymer tacticity
- Normally, whether the Me group of the eta-2 propene points up or down it has identical steric interactions with the Cp rings; orientations equally favoured, only atactic PPE produced
- With ansa metallocenes, it produces either isotactic or syndiotactic (depends on type)