introduction - shodhgangashodhganga.inflibnet.ac.in/bitstream/10603/32787/7/07_chapter 1.pdf · o...
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Introduction
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1. Introduction
1.1. Overview
Organometallic chemistry, which involves metal complexes containing direct
metal-to-carbon bonds, has grown since the early 1950s at an almost exponential rate,
mostly owing to the development of an impressive array of highly sophisticated
apparatus of which in particular NMR and single-crystal X–ray equipments have been
invaluable [1]. Theoretical studies of the bonding in metal compounds and of the
course of reaction pathways have not only contributed to new knowledge, but also to
the purposeful design of complexes and their use in stoichiometric and catalytic
reactions.
Platinum metal complexes of unsymmetrical chelating ligands such as
functionalized phosphines have aroused much interest in recent time because of their
structural novelty, reactivity and catalytic applications, namely carbonylation [2–4],
hydrogenation [2c,5,6] and hydroformylation [2c,7,8] reactions. Homogeneous
catalysis by transition metal complexes has become a major synthetic tool in industrial
processes [2–8]. The potential of such catalytic reactions is due to the fact that most of
these reactions are highly selective, low energy processes and show high rate of
conversion. Among the platinum metals, rhodium, iridium and ruthenium complexes
have been given special attention in this thesis due to their versatile catalytic activity
and unique character.
1.2. Rhodium
Rhodium is one of the rarest and expensive precious metals. It has a typical
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electronic configuration ([Kr]4d85s
1) and exhibits mainly the principal oxidation
states of +1 and +3. RhCl3.xH2O is a versatile starting material for the synthesis of
different rhodium(I) complexes. One of the most famous rhodium(I) complexes is the
Wilkinson’s catalyst, [RhCl(PPh3)3] [9a]. Great varieties of rhodium complexes are
prepared from RhCl3.xH2O and the methods for preparation of some selected starting
rhodium complexes are shown in Scheme 1.1.
Scheme 1.1. Important preparative routes for starting rhodium complexes
The primary use of rhodium is in automobiles as a catalyst converter, which
converts harmful emission like CO, unburned hydrocarbon (HC) and oxide of nitrogen
(NOx) from the engine into less harmful gases like CO2, N2 and H2O [10].
Rhodium(I)-complexes play an important role as industrial homogeneous catalysts for
the synthesis of value added products. A few important examples are: (i) Synthesis of
L-DOPA (a drug for curing Perkinson's disease) [11], (ii) Production of acetic acid by
RhCl3.3H2OCO, moisture, 100 oC
[RhCl(CO)2]2
trans-[RhCl(CO)(PPh3)2]
Ref. 9a
C2H5OH, CO, PPh3
Ref. 9b
PPh3, C2H5OH
Ref. 9c
[RhCl(PPh3)3]
COD, C2H5OH / H2O
Ref. 9d[RhCl(COD)]2
COE, Me2CHOH / H2O
Ref. 9e
[RhCl(COE)2]2
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Monsanto’s process [12,13] (iii) hydroformylation of alkene to synthesize highly
selective linear to branch aldehydes [8,14], (iv) hydrosilylation crosslinking of
silicone rubber [15] and many other organic transformations [16].
1.3. Iridium
Iridium is the most corrosion-resistant metal, even at temperatures as high as
2000 °C. The electronic configuration of iridium is [Xe]4f14
5d76s
2, which exhibits
different oxidation states ranging from -3 to +6 and the most stable oxidation states
are +3 and +4 [5d]. Iridium forms a number of organometallic compounds used in
industrial catalysis, and in research [5d]. Some organometallic iridium(I) compounds
are notable enough to be named after their discoverers. Two important examples are:
(i) Vaska's complex, [IrCl(CO)(PPh3)2], which has the unusual property of binding to
the dioxygen molecule, O2 [17], and (ii) Crabtree's catalyst, [Ir(COD)(Pcy3)(Py)]+PF6
–,
a homogeneous catalyst for hydrogenation reactions [18]. These compounds are both
square planar, d8 complexes, with a total of 16 valence electrons, which accounts for
their reactivity [19]. Although iridium complexes are less frequently used than their
rhodium analogues, in some processes they may be more effective– the Cativa process
for carbonylation of methanol being an excellent example in the arena of bulk
chemistry [3a,b]. Perhaps the most important catalytic applications of iridium
complexes, however, are in the manufacture of fine chemicals, most notably in areas
of chemoselective and enantioselective hydrogenation [5d]. Great varieties of iridium
complexes are prepared from IrCl3.xH2O and the methods of preparation of a few
selected starting iridium complexes are shown in Scheme 1.2.
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Scheme 1.2. Some important preparative routes for starting iridium complexes
1.4. Ruthenium
Ruthenium is a rare transition metal belonging to the platinum group of the
periodic table. It has an electronic configuration [Kr]4d75s
1 and can show a much
wider scope of oxidation states e.g. -2, 0, +2, +3, +4, +5, +6 and +8 valence states in
[Ru(CO)4]2-
, [Ru(CO)5], [Ru(H2O)6]2+
, [Ru(NH3)6]3+
, [RuO2], K[RuF6], [RuF6] and
[RuO4] respectively and various coordination geometries in each electronic
configurations [21]. For instance, in the principal oxidation states of +2 and +3,
ruthenium complexes normally prefer trigonal-bipyramidal and octahedral structures
respectively. Due to this variable oxidation states and higher economy of ruthenium
compared to the other platinum metals, ruthenium catalyzed processes have become
IrCl3.3H2O trans-[IrCl(CO)(PPh3)2]Ref. 20c
Ref. 20a
COD, C2H5OH / H2O
Ref. 20a[IrCl(COD)]2
COE, Me2CHOH / H2O
Ref. 20d
[IrCl(COE)2]2
PPh3, DMF
Cp*, alcohol[IrCl2(Cp*)]2
2-methoxyethanol,
120 oC, Ref. 20e
Et4NX/ / KI, CO
(X/ = Cl, Br)[Ph4As][IrX2(CO)2]
CO, Ref. 20bPPh3
[X = Cl, Br, I]
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one of the most important and interesting methodologies in organic synthesis [21b,22–
24]. In particular, ruthenium complexes catalyzed hydrogenation reaction is one of the
most appealing routes for the reduction of various organic substrates [23]. The
development of Noyori’s transfer hydrogenation catalysts has attracted the attention of
the researchers towards the use of ruthenium catalysts in asymmetric hydrogenation
reactions [21b,22a,24c,25]. The ruthenium complexes also exhibit a variety of suitable
characteristics like high Lewis acidity, high electron transfer ability, low redox
potentials, stabilities of different reactive species etc. RuCl3.xH2O can be utilized for
the synthesis of ruthenium complexes of different ligands and the methods for
preparation of some selected starting ruthenium complexes [25d] are shown in
Scheme 1.3.
1.5. Carbon monoxide (CO) ligand
Carbon monoxide is the most common π-acceptor ligand in organometallic and
coordination chemistry. It plays a key role in many catalytic processes. Over the last
few decades, transition metal carbonyl complexes have become one of the most
important families of compounds in organometallic chemistry [27]. Rhodium and
iridium carbonyls are very active catalysts for carbonylation and hydroformylation
reactions to synthesize industrially important products [2,3,8,28]. Some prominent
examples are: (i) Rhodium catalyzed Monsanto’s process [12,13] for producing acetic
acid from methanol, (ii) A recent industrial catalytic process called ‘Cativa’ [3] where
[IrI2(CO)2]- species with ruthenium-complex activator are used for carbonylation of
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methanol with high efficiency and (iii) Hydroformylation of alkenes to synthesize
highly selective linear to branch aldehydes [8,14].
Scheme 1.3. Some important preparative routes for ruthenium complexes [25d].
1.6. Functionalized phosphine
Tertiary phosphines functionalized with chalcogen donors like oxygen [29],
sulfur [30] and selenium [31] containing ‘Soft’ phosphorus and ‘Hard’ oxygen donors
or ‘Soft’ phosphorus and relatively less ‘Softer’ sulfur and selenium donor ligands
with distinctly different π-acceptor strength [5a] form a variety of metal complexes
RuCl3.nH2O
CO, Ethanol,
PPh3, CO,
[RuCl2(CO)2]n
[RuCl2(CO)(PPh3)2]
Ref. 26e,f[Ru3(CO)12]
CO, MeOH / CO, Zn
PPh3, EtOH[RuCl2(PPh3)3]
C5Me5H[RuCl2Cp*]n
1,5-C8H12, Zn[Ru(COD)(cot)]
Ref. 26h
Ref. 26d
Ref. 26g
PPh3, HCHO[RuH2(CO)(PPh3)3]
Ref. 26c
Reflux.
alc., Boil
1,5-C8H12, Zn [RuCl2(COD)]n
Ref. 26a
Ref. 26i
Ref. 26b
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due to their different bonding abilities. Oxygen being a ‘Hard’ donor is capable of
stabilizing metal ions in higher oxidation states which can be ascribed due to the
absence of dπ-back bonding. On the other hand, ‘Soft’ phosphorus donors stabilize
metal ion in low oxidation state by dπ–σ* back bonding. The metal-oxygen bond is
weak and may dissociate reversibly to generate a vacant site for substrate binding and
such ligands are called ‘Hemilabile’. The M–S/Se bonds are comparatively labile than
the M–P bonds in the chelated complexes of P–S and P–Se donors ligands and thus
may permit facile generation of a ‘Vacant site’ at the metal centre [5a,32] and may
show interesting dynamic stereo-chemistry. Creation of such vacant coordination site
through a reversible ‘Opening and Closing’ mechanism [32b] is useful for
coordination and activation of the small molecules for further reaction with other
organic substrates (Scheme 1.4).
Scheme 1.4. Ring “Opening and Closing” mechanism (Hemilabile)
A thermodynamically stable metal complex will have the substitutionally
inert ligand group (X) binding to soft metals if X is a soft base, such as the case with
phosphorus based hemilabile ligands, or to hard metals if X is a hard base such as
oxygen or fluorine. These ligands were first described in a kinetic context as
‘Hemilabile ligands’ in 1979 by Jeffrey and Rauchfuss [32c].
LnM
X
Y
+ S
- SLnM
X
SY
M = Metal centre, Ln = Ligand, X = Inert group,
Y = Labile group, S = Solvent,
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1.7. Rhodium, iridium and ruthenium complexes of functionalized phosphine: A
brief summary of the prior art.
Platinum metals particularly rhodium, iridium and ruthenium form a wide
variety of complexes with functionalized phosphine ligands. A brief summary of
different potential metal complexes are highlighted below:
1.7.1. Complexes of mono- and bidentate phosphines
A large number of coordination metal complexes of the first row transition
metals [33], lanthanides [34] and actinides [35] with phosphine-chalcogenide ligands
have been reported. However, the platinum metals like rhodium, iridium and
ruthenium complexes have got less attention. A few interesting neutral rhodium(I)
complexes of the type [Rh(COD)ClL] (L = Me3PS, Me2PhPS, Me2PhPSe, Me3AsS
[36]), [RhCl(CO)2(Cy3PO)] (Cy = C6H11) [37] and [RhCl(CO)2Ph3PX] (X = O, S, Se)
[38], and cationic complexes of the type [Rh(COD)(OER3)2]ClO4 and [Rh(CO)2-
(OER3)2]ClO4 ( E = P, As; R = Ph, p-MeC6H4, p–MeOC6H4 ) [39] have been reported.
There are also some reports on the rhodium(III) phosphineoxide complexes such as
[RhCl(ylide)2(OPR3)] [40], [Rh(dimethylglyoximate)2(OPPh3)] [41] etc. Reports on
the iridium complexes of chalcogen functionalized phosphines are limited except a
series of Vaska type complexes, [IrX(CO)L2], where X = Cl, Br, I and L = substituted
PPh3 [42]. The interesting monodentate ruthenium complexes reported so far are
[RuCl2(DMSO)3(PPh3O)] [43] and [RuCl2(CO)2(Ph3PX)x], (X = O, S, Se) [44].
During last two decades, increasing attention has been focused on the complex
chemistry of hemilabile ligands, particularly, bidentate tertiary phosphines
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functionalized with oxygen [5b,32a,45], sulfur [46,47] and selenium [48] donors.
Reports on catalytic reactions of complexes containing sulfur or selenium donor are
scanty because of metal poisoning by sulfur atom [49a] and deselination of selenide
under the reaction condition [49b]. However, a few metal complexes containing P–S /
P–Se ligands have been reported to exhibit efficient catalytic activity in potential
organic synthesis [4e,50]. A few interesting metal complexes of unsymmetrical
chalcogen functionalized phosphines have been discussed with special emphasis on
bidentate phosphines.
There are different types of hemilabile P–O donor ligands such as ester-
phosphine [51], ether-phosphine [52], keto-phosphine [53], phosphine-acids [54],
diphosphine-monoxide [55] etc. An outstanding feature of these ligands is their
capability of coordinating to the metal centre either through a monodentate (ƞ1-P) or
bidentete (ƞ2-P,O) coordinated fashion depending upon the metal and its environment
The complexes [RhCl(CO)(ƞ2-P,O-BPMO)] (BPMO = dppmO, dppeO,
dpppO, and dppbO) [56a] and the iodo dppmO analogue [56b] are prepared by
reacting [RhX(CO)2]2 (X = Cl, I) with corresponding BPMOs (Eqn. 1). The five-
membered complex [RhCl(CO){ƞ2-P,O-Ph2PCH2P(O)Ph2}] does not react with
CO under low pressure (1 atm.), however, on increasing the pressure to 3 atm., a trace
amount of dicarbonyl complex cis-[RhCl(CO)2{ƞ1–P-Ph2PCH2P(O)Ph2}] is formed
[56c]. On the other hand, the six-membered complex [Rh(CO)Cl{ƞ2-P,O-Ph2PCH2-
CH2P(O)Ph2}] can reversibly be cleaved by CO even at low pressure (1–3 bar) to give
cis-[RhCl(CO)2{ƞ1-P-Ph2PCH2CH2P(O)Ph2}] (Scheme 1.5).
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Scheme 1.5. ‘Hemilabile’ behaviour of P,O donor ligand.
Two complexes of the types [RhCl(CO)(2-Ph2PC6H4COOMe)] (ƞ2-P,O
chelate) and trans-[RhCl(CO)(2-Ph2PC6H4COOMe)2] (ƞ1-P coordinated) are reported
[4a]. The X-ray structure (Figure 1.1) of the latter complex indicates the presence of
‘Secondary’ Rh–O interactions with the ester groups of the phosphines, which exhibits
(CO) band at 1949 cm-1
indicating the lowest value so far reported of such
complexes.
P,S ligands show an interesting feature as [RhCl(CO)2]2 reacts with
Ph2PCH2SCH3 to produce a binuclear complex [Rh2Cl2(CO)2(µ-Ph2PCH2SCH3)2],
while with Ph2PCH2CH2SCH3 it yields a mononuclear complex [RhCl(CO)(Ph2P-
CH2CH2SCH3)] (Scheme 1.6) [57a].
Rh
OC
ClP
PPh2O
Ph2
Rh
OC
OC
Cl
P
PPh2O
Ph2
+ CO
[RhX(CO)2]2
CH2Cl2 / toluene
P
OP
Rh
OC X
[Eqn 1]
X = Cl; BPMO = dppmO, dppeO, dpppO, dppbOX = I; BPMO = dppmO
BPMO
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Figure 1.1. X-ray structure of trans-[RhCl(CO)(2-Ph2PC6H4COOCH3)2] [Ref. 4a]
Scheme 1.6. Mono and binuclear rhodium carbonyl complexes of P,S donor ligands
Unsymmetrical phosphine–phosphine monoselenide ligands react with
[RhCl(CO)2]2 to form chelate [RhCl(CO)(ƞ2-P,Se-Ph2PCH2P(Se)Ph2)], [RhCl(CO)-
(ƞ2-P,Se-Ph2PN(CH3)P(Se)Ph2)] [4d] and non-chelate [RhCl(CO)2(ƞ
1-P-Ph2P-
(CH2)nP(Se)Ph2)] {n = 2–4} complexes depending on the nature of the ligands [4e].
L2: Ph2PCH2SCH3
L1: Ph2PCH2CH2SCH3
RhOC
Cl
Rh
OC
Cl
Ph2P SCH3
H3CS PPh2
L1L2
Rh
Cl CO
H3CS PPh2
OC
OCRh
Cl
ClRh
CO
CO
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The molecular structure of [RhCl(CO)(ƞ2-P,Se-Ph2PN(CH3)P(Se)Ph2)] (Figure 1.2)
shows a stable five-member heterocyclic (Rh, P, N, P and Se) ring.
Figure 1.2. X-ray structure of [RhCl(CO){ƞ
2-P,Se-Ph2PN(CH3)P(Se)Ph2}] [Ref. 4d].
In addition to the several rhodium carbonyl complexes of unsymmetrical
phosphine-phosphine chalcogenides, the complexes of symmetrical phosphine-
phosphine chalcogenides are also reported [57b]. The preparation of rhodium carbonyl
complex [Rh(CO)2(dppmS2)][ClO4], where dppmS2 = Ph2P(S)CH2P(S)Ph2 is reported
[57b] and the molecular structure of which was established by single crystal X-ray
diffraction studies.
Some interesting complexes [Rh(CO)(PPh3){ƞ2-P,O-Ph2PNP(O)Ph2}],
[Rh(CO)2{ƞ2-Se,Se
/-Ph2P(Se)NP(Se)Ph2}] and [Rh(CO)(PPh3){ƞ
2-Se,Se
/-Ph2P(Se)-
NP(Se)Ph2}], are synthesized by stepwise reactions of CO and PPh3 with
[Rh(COD){ƞ2-P,O-Ph2PNP(O)Ph2}] and [Rh(COD){ƞ
2-Se,Se
/-Ph2P(Se)NP(Se)Ph2}]
respectively [57c]. The structure of the complex [Rh(CO)(PPh3){ƞ2-Se,Se
/-
Ph2P(Se)NP(Se)Ph2}] (Figure 1.3) exhibits a slightly distorted boat ring conformation.
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Figure 1.3. The structure of [Rh(CO)(PPh3)(ƞ2-Se,Se-{Ph2P(Se)}2N)] [Ref. 57c].
Iridium also forms interesting complexes by the reaction of [IrL2]Cl (L =
Ph2PCH2CH2PPh2) with S8 or Se8 to yield [IrS2L2]Cl or [IrSe2L2]Cl, respectively;
where S2 and Se2 act as bidentate ligands [58a].
The neutral complex [IrCl(COD)(ƞ1-P-L)] (I) (L = dicyclohexyl(2-methoxy-
ethyl)phosphine), obtained from the reaction of [Ir(µ-Cl)(COD)]2 with L, reacts with
AgBF4 to undergo Cl- abstraction and subsequent occupation by the ether O atom at
the empty coordination site to produce cationic complex, [Ir(COD)(ƞ2-P,O-L)]Cl (II)
In the presence of H2 and L, the reactive Ir–O bond in II is cleaved with formation of
cis-[H2Ir(COD)L2] (III) (Figure 1.4) [58b].
A few more interesting iridium complexes are obtained by the reaction of
trans-[IrI(CO)(PEt3)2] with Y(SiH3)2 (Y = O, S, Se) in benzene to give [IrI(CO)H-
(PEt3)2(SiH2YSiH3)] or [IrI(CO)H(PEt3)2(SiH2)]2Y, although when Y = O the
formation of the former species is difficult to detect. The reaction of the complexes
with P(SiH3)3 leads to the formation of IrI(CO)H(PEt3)2[SiH2P(SiH3)2],
[IrI(CO)H(PEt3)2(SiH2)]2PSiH3, or [IrI(CO)H(PEt3)2(SiH2)]3P, depending on the
proportions of the reactants used [58c].
Rh
OC
Ph3P
Se
Se
PPh2
N
PPh2
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Figure 1.4. Synthesis of different neutral and anionic iridium complexes of P,O donor
ligand.
Ruthenium forms various types of complexes containing chalcogen
functionalized phosphines as coordinating ligands. The polymeric complex
[RuCl2(CO)2]n reacts with Ph3PX; X = O, S and Se in an appropriate Ru : Ligand mole
ratio to yield five- and six-coordinated complexes of the types [RuCl2(CO)2(Ph3PX)]
and [RuCl2(CO)2(Ph3PX)2] respectively (Scheme 1.7) [44]. The ν(PX) bands of the
complexes show significantly lower wavenumber than the corresponding free ligands
indicating the formation of Ru–X bonds.
The reactions of [ƞ6-C6Me6)RuCl2]2 and [(ƞ
5-C5Me5)RhCl2]2 with the ligands L
= Ph2PCH2PPh2 or Ph2PCH2P(Se)Ph2 in benzene yield neutral complexes
[(ring)RuCl2(ƞ1-L)], [ring = (ƞ
6-C6Me6) or (ƞ
5-C5Me5)] [59]. However, cationic
complexes of the type [(ring)RuCl(ƞ2-L)]ClO4 can be prepared using acetone as
solvent in the presence of NaClO4 [59].
IrCl
P
H3CO
Ir
P
OAgBF4
H2 L
Ir
H L
H
L
(I)
(II)
(III)
P
H3CO
L :
+ BF4-
+ BF4-
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Scheme 1.7. The reactions between [RuCl2(CO)2]n and Ph3PX (X = O, S, Se)
Interesting complex is formed by the reaction of diphosphine, oxygen-
functionalized diphosphine ligands and RuCl3 in the presence of formaldehyde (Figure
1.5) [60], where the Ru–P bond trans- to oxygen is considerably shorter (222 pm) than
the other two Ru–P bonds. The complex [RuCl2(P∩O)(P~O)2], formed by the reaction
between [RuCl2(PPh3)3] and P,O ligands, shows fluxional behaviour (Scheme 1.8)
[61].
Figure 1.5. Ruthenium complexes of P,P and P,O donor ligands [Ref. 60]
The bisphosphine monoxides (R)- and (S)-BINAPO(O), prepared by the mono-
oxidation of (R)- and (S)-BINAP respectively, form [(p-cymene)RuCl{ƞ2-P,O-
BINAPO(O)}]Cl and [(p-cymene)Ru{ƞ2-P,O-BINAPO(O)}](SbF6)2 complexes [62].
The BINAPO(O) ligand binds diastereo selectively, and form a single thermo-
[RuCl2(CO)2]n
n[RuCl2(CO)2(Ph3PX)2]n[RuCl2(CO)2(Ph3PX)]Ph3PX
2n mol Ph3PXn mol Ph3PX
X = O, S, Se
P
P
Ru
P
O P
Ph MeCl
Cl
Me Ph
Ph MePhMe
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dynamically stable diastereomer of the two possible isomers. The compound [(p-
cymene)Ru{ƞ2-P,O-BINAPO(O)}](SbF6)2 is an efficient catalyst for the Diels-Alder
reaction of methacrolein and cyclopentadiene in moderate ee.
Scheme 1.8. Fluxional behaviour of trans-,cis-,cis- [RuCl2(P∩O)(P~O)2]
The hexa-coordinated chelate complex cis-[RuX2(CO)2(P∩S)] {P∩S= ƞ2-P,S-
coordinated, X = Cl, I} and penta-coordinated non-chelate complexes cis-[RuCl2-
(CO)2(P~S)] {P~S = ƞ1-P-coordinated} are synthesized [63a,b] by the reaction of
[RuX2(CO)2]n with equimolar quantity of the ligands Ph2P(CH2)nP(S)Ph2 (n = 1–4) at
room temperature (Scheme 1.9, 1.10). The bidentate nature of the ligand
Ph2PCH2P(S)Ph2 in the complex leads to the formation of five-member chelate ring
which confers extra stability to the complex. While, the reaction with 1:2 (Ru:L) mol
ratio affords the hexa-coordinated non chelate complexes cis-[RuX2(CO)2(P~S)2]
irrespective of the ligands.
[RuCl2(PPh3)3]
RuO
P3P1~O
P2~O
Cl
Cl
RuO
O3~P P1~O
P2
Cl
Cl[P,O : (CH3)2PCH2CH2OCH3]
P,O
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Scheme 1.9. Synthesis of iodo-carbonyl ruthenium(II) complexes of P,S ligands.
Scheme 1.10. Synthesis of chloro carbonylruthenium(II) complexes of P,S ligands.
[RuI2(CO)2]n
n mol (i)
2n mol (i-iv)
n mol (ii-iv)
Ru
OC
IS
P
I
CO
Ru
OC
I P~S
I
P~S
CO
Ru
S~P
I CO
I
CO
n mol (ii-iv)n mol (i)
Ru
OC
OC S~P
P~S
I
I
Ru
CO
CO
I
I
Ligands: PPh2(CH2)xPPh2, x = 1(i), 2(ii), 3(iii) and 4(iv)
P~S : ƞ1-P coordinated or -P,S- coordinated; P∩S : ƞ
2-P,S coordinated
[RuCl2(CO)2]n
n mol (i)
2n mol (i-iv)
n mol (ii-iv)
Ru
OC
ClS
P
Cl
CO
Ru
OC
Cl P~S
Cl
P~S
CO
Ru
S~P
Cl CO
Cl
CO
n mol (ii-iv)n mol (i)
Ru
OC
S P
S
P
CO
(ClO4)2
2AgClO4
Ru
OC
Cl P
SCO
(ClO4)
AgClO4
Ligands: PPh2(CH2)xPPh2, x = 1(i), 2(ii), 3(iii) and 4(iv)
P~S : ƞ1-P coordinated; P∩S : ƞ
2-P,S coordinated
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Neutral and cationic half-sandwich complexes of ruthenium, rhodium and
iridium with chiral [(S)-1-[(R)-2-(diphenylphosphino)ferrocenyl]ethyl]di-tbutyl
phosphine selenide (L) are reported [64]. The ligand L is the first example of a chiral
bisphosphine monoselenide prepared by direct monoselenation of a commercially
available chiral bisphosphine.
1.7.2. Complexes of poly-phosphines
Polyphosphines as ligands show several advantages like (i) excellent bonding
ability to metal, (ii) create high electron density at the metal centre (high
nucleophilicity), (iii) formation of stable metal-complexes, (iv) stabilize different
oxidation states of metals, (v) provide structural and bonding information due to the
metal-phosphorus and phosphorus-phosphorus coupling constants. Metal complexes
of such ligands are thermodynamically more stable than monophosphine analogues.
Tripod, HC(PPh2)3 with least steric constraints forms small rhodium cluster
having metal-metal bond (Figure 1.6) [65a].
Figure 1.6. Rhodium complex of HC(PPh2)3 containing Rh–Rh bond.
In metal-tripod [tripod: MeC(CH2PPh2)3] complex based catalytic reactions
like hydroformylation, one of the metal-ligand bonds dissociate to create vacant site
C
Rh Rh
Ph2PPPh2
H
S
S
OC
OC CO
2+
Ph2P
(S = solvent)
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for substrate binding (Figure 1.7) [65b].
Figure 1.7. Reversible dissociation of Rh–P bond [Ref. 65b]
Though a large number of rhodium complexes of polyphosphine ligands have
been reported [65], there are only a few reports of rhodium complexes containing
chalcogen functionalized polyphosphine ligands (P–X). The cationic complex
[Rh(COD){ƞ3–P,S,S-(CH(PPh2)(P(S)Ph2)2}] is prepared as fluoroborate salts by the
reaction of the ligand CH(PPh2)(P(S)Ph2)2 with chlorobridged complex
[Rh2Cl2(COD)2] under mild conditions in presence of NaBF4 [66a]. The structure of
the complex is assigned by 31
P NMR spectroscopic studies indicating the formation of
tripodal ƞ3-P,S,S coordinated ligand.
The conventional oxidation of triphos with H2O2 is nonselective, but the ligand
can be mono-oxidized selectively [66b] in the form of its ƞ2-P,P-triphos metal
complex (Eqn. 2). The dicarbonyl rhodium complex that is originally formed loses a
molecule of CO upon bubbling argon through its solution.
The cationic complexes [(arene)RuCl{ƞ2-L}]A are synthesized by the reaction
between triphosphine CH(PPh2)3 or its mono / bichalcogenide derivatives with
suitable ƞ6-arene-Ru(II) species, where, arene = C6Me6, p-MeC6H4
iPr; L = CH(PPh2)3,
CH(PPh2)2{P(E)Ph2} (E = S, Se), CH(PPh2){P(S)Ph2}2 and A = PF6-, BF4
- [67a]. An
RhP
P
P
H
RhP
P
H
CO CO
OCP
CO
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interesting complex [(arene)Ru{ƞ3-S,S,S-{P(S)Ph2}3C}]BF4; is prepared by deproto-
nation of the coordinated ligand [{P(S)Ph2}3CH], where the ligand is coordinated to
the ruthenium centre by tridentate ƞ3-S mode (Figure 1.8).
Figure 1.8. Synthesis of [(arene)Ru{ƞ3-S,S,S-{P(S)Ph2}3C}]BF4 [arene = p-
MeC6H4iPr] [Ref. 67a]
The complex [RuCl2(CO)2]n reacts with one mol equivalent of triphos to
afford [RuCl2(CO)2(ƞ2-P2-triphos)] (Scheme 1.11). However, the complex on setting
aside for about two weeks in DCM solution undergoes decarbonylation to yield a
tridentate monocarbonyl complex [RuCl2(CO)(ƞ3-P3-triphos)] (Scheme 1.12) [67b].
iPrMe
P P P
R
R
S
R
RS
RR
S
Ru
BF4
PPh2
PPh 2
Ph2P
Rh
Cl
CO
CO
PhC(OOH)Me2
CO
PPh2
PPh 2
Ph2P
Rh
Cl
CO
CO
O
-CO
[Eqn 2]PPh2
PPh 2
Ph2P
Rh
Cl
CO
O
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Scheme 1.11. Synthesis of [RuCl2(CO)2(ƞ2-P2-triphos)].
Scheme 1.12. Decarbonylation of [RuCl2(CO)2(ƞ2-P2-triphos)]
1.8. Activation of small molecules
One important general problem in organometallic chemistry is the binding and
activation of the small molecules of nature. Thus, it is an interesting area to carry out
research to activate the less reactive molecules like CO, CO2, O2, H2, alkane etc. with
a goal to convert these relatively common compounds into useful organic chemicals
RuCl3.xH2OCO
Alcohol / Reflux[RuCl2(CO)2]n
PPPRu
Cl
CO
P
P
Cl
OC
P
CH3OH, reflux
3 h
P
P
P
P P P
=
RuCl
CO
P
P
OC
RuCl
CO
P
P
P
Cl-CO
Cl
P
P
P
PP P P
=
DCM/Hexane
Two weeks
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[68]. For example, natural gas (methane) is wasted by being flared off in certain oil
fields, for lack of an economic method of transport. A method of turning this methane
into easily transportable liquids, such as methanol or higher alkanes, would be very
valuable. Therefore, much fundamental chemistry research has therefore been aimed
to address couple of questions such as:
How do metal ions coordinate to and modulate the reactivity of small, often
rather inert molecules?
What is the basis for the selectivity of natural and synthetic metal-containing
systems for specific small-molecule substrates?
Can one use knowledge of metal/small-molecule chemistry for the development
of new catalytic processes useful in the laboratory and / or in industry?
The activation of small molecules such as CO, CH3I, H2, O2, etc., by metal
complexes [69] is important and interesting due to their catalytic reactions; for
instance, OA of CH3I is an important step in the rhodium-catalyzed Monsanto [12,13]
and iridium-based Cativa [3a,b] process for acetic acid production. Activation of
molecular oxygen by metal complexes has attracted great interest in recent years for
producing model oxidation catalysts for chemical processes in terms of cost, atom
economy and the potential for limited by-products [69e, 70]. Similarly, the activation
of dihydrogen by metal centers is a fundamental step in nearly all metal catalytic
hydrogenation reactions [71].
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1.9. Catalytic applications
Rhodium, iridium and ruthenium-catalyzed reactions have made a significant
contribution to the recent growth of organic synthesis particularly in carbonylation,
hydrogenation, hydroformylation, carbon-carbon bond formation etc. [3,5,11–14,16,
21–23]. In this section, two potential catalytic reactions, namely, carbonylation and
hydrogenation have been highlighted.
1.9.1. General aspects of carbonylation catalysis
Acetic acid is an important industrial commodity chemical, with a worldwide
demand of about 7–8 million tons per year. One of the largest and fastest growing uses
of acetic acid is in the production of vinyl acetate, an important industrial monomer.
The major part of the remaining acetic acid production is used to manufacture other
acetate esters. Cellulose acetate is used extensively in the preparation of fibers and
photographic films. Inorganic acetates are used in the textile, leather and paint
industries. Acetic acid is also used in the manufacture of chloroacetic acid and
teraphthalic acid [72].
The synthesis process of acetic acid has changed over the years with
changing technologies and several problems are associated due to their lack of
selectivity and formation of many byproducts. Novel acetic acid processes and
catalysts have been introduced, commercialized and improved continuously since the
1950s. The objective of the development of new acetic acid processes has been to
reduce raw material consumption, energy requirements and investment costs.
Significant cost advantages resulted from the use of carbon monoxide (derived from
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natural gas) and of low-priced methanol (from synthesis gas) as feedstock. A few
carbonylation processes and their recent advances are highlighted below:
1.9.1.1. The cobalt-based BASF process
The first methanol-to-acetic acid carbonylation process was commercialized in
1960 by BASF. It used an iodide-promoted cobalt catalyst and required high pressures
(600 atm) as well as temperatures (230 °C), but gave acetic acid in ca. 90% selectivity
[73]. The process generates a few by-products like methane, acetaldehyde, ethanol and
ethers. The proposed mechanism of the process (Scheme 1.13) indicated that
[HCo(CO)4] is the active catalytic species to propagate the cycle. However, the
postulated intermediates are not well characterized [73].
Scheme 1.13. BASF catalytic cycle for the synthesis of acetic acid from methanol.
It is interesting to note that slightly lower CO pressures are possible in the
presence of Ru, Ir, Pd, Pt, or Cu salts as activators [74]. Cobalt catalysts can also be
used for the carbonylation of higher alcohols, such as benzyl alcohol [75].
[HCo(CO)4]
[CH3Co(CO)4]
[CH3COCo(CO)3]
[CH3COCo(CO)4]
CO
H2O
HICH3COOHCH3OH
CH3ICH3COI
HIHI
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1.9.1.2. Nickel-based processes
Nickel carbonyl, as well as a variety of nickel compounds, is also catalytically
active for the carbonylation of methanol in the presence of iodine. Ni(CO)4 is formed
from NiI2 according to Eq. 3.
The hydrogen iodide formed in Eq. 3 is used to transform the alcohol into an
alkyl halide, which adds oxidatively to nickel, as described in Scheme 1.14 [76].
Scheme 1.14. Catalytic cycle of the nickel-catalyzed methanol carbonylation.
Nickel catalysts usually operate under high pressures and temperatures [77],
but with high methyl iodide concentrations, carbonylation occurs readily under milder
conditions [78]. Molar ratios of CH3I:CH3OH at least 1:10, pressures as low as 35 bar
can be applied at 150 °C, using Ni(OAc)2.4H2O and Ph4Sn as catalyst systems [79].
Although nickel systems can approach the reaction rates and selectivities of rhodium
based catalytic systems, and nickel is much cheaper than rhodium, commercialization
NiI2 + H2O + 5CO Ni(CO)4 + 2HI + CO2 [Eq. 3]
Ni(CO)4
CH3I
2CO
Ni(CO)2(CH3)I
CO
Ni(CO)2(COCH3)I
2CO
CH3COI
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of these systems has not been achieved to date, which may be due to the very toxic
and volatile nature of the Ni(CO)4 compound.
1.9.1.3. The rhodium-based Monsanto process
The Monsanto acetic acid process is commercially an important process since
it produces over 50% of the world’s annual acetic acid demand, i.e. 7 million metric
tons [80]. The process involves the homogeneous catalysis in the carbonylation of
ethanol to yield acetic acid (Scheme 1.15).
Scheme 1.15. Catalytic cycle of the rhodium-catalyzed methanol carbonylation
Furthermore, the effect of the rhodium metal centre on the catalytic system is
very high, since the metal centre facilitates both the OA and reductive elimination
steps. The key reaction in the Monsanto process is the facial OA of methyl iodide,
(step A), to the square planar rhodium(I) metal centre to form the octahedral
CO
H2O
HICH3COOH CH3OH
CH3ICH3COI
Rh
CO
CO
I
I
-
Rh
CO
CO
I-I
I
Rh
CO
CO
I
I
-H3C
I
Oxidative addition(A)
CH3
Migratory insertion
(B)
Ligand addition(C)
Reductive elimination(D)
Rh
CO
CO
I-I
I
CH3
OC
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rhodium(III) species. Carbon monoxide insertion (step B) into the cis- CH3–Rh bond
yields a five-coordinated acyl intermediate, which undergoes addition of carbon
monoxide (step C), reductive elimination of the acetyl iodide (step D) to yield the
original rhodium(I) complex. Hydrolysis of the acetyl iodide by water in the aqueous-
methanol feed gives acetic acid and HI, the latter reacts with methanol to regenerate
methyl iodide and the cycle repeats itself.
The mechanism presented, including all intermediates, was resolved after
extensive research [81] into the area and as recently as 1991 by Maitlis et al. [82], the
existence of the intermediate (after step A) was confirmed in low concentrations
utilizing FT-IR and FT-NMR spectroscopy.
1.9.1.4. Heterogenized rhodium catalysts
An important additional requirement for all homogeneous processes is that the
dissolved catalyst must be separated from the liquid product and recycled to the
reactor without significant catalyst loss [83]. In order to overcome the need for a
separation catalyst recycle step, the active rhodium complex was made heterogeneous
by using different support [80a,84]. Although the activity of these catalysts in the
liquid phase was comparable to Monsanto’s homogeneous catalyst, there were
problems with rhodium metal leaching from the support and the decomposition of the
support during operation at elevated temperature. Such problem was overcome by
Chiyoda by introducing a novel catalytic system containing pyridine resins where the
catalysts exhibited high activity, long catalyst life, and no significant rhodium loss
[85]. Based on this heterogeneous rhodium catalyst, Chiyoda and UOP (Universal Oil
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Products) have jointly developed an improved methanol carbonylation process, called
‘Acetica process’, for the production of acetic acid. Until the recent development of a
commercial heterogeneous rhodium catalyst system by Chiyoda, no successful
demonstration of such a catalyst had been known [80a]. The heterogeneous catalyst
commercialized for the ‘Acetica process’ consists of rhodium complexes on a novel
polyvinyl pyridine resin [86] which is tolerant of elevated temperatures and pressures.
Very recently, Haynes et al. reported an alternative strategy for catalyst
immobilization, using ion-pair interactions between ionic catalyst complexes and
polymeric ion exchange resins [83]. These results demonstrated that the same
sequence of organometallic reactions occur for the polymer-supported rhodium
catalyst as already established for the homogeneous system.
1.9.1.5. The iridium-based Cativa process:
In 1996, BP chemicals introduced a new carbonylation process called ‘Cativa’
to produce acetic acid using iridium/iodide based catalyst, in combination with a
promoter metal such as ruthenium [3,87]. This catalytic system has high rates at
low water concentrations and exhibits high stability which allows for a wide range of
process conditions. The Cativa catalytic process is shown in Scheme 1.16.
The OA of CH3I to the activated iridium complex is faster than for similar
rhodium complexes. The equilibrium of this OA favors the Ir(III) state. Therefore the
OA is not the rate-determining step of the Cativa process. Instead the migratory
insertion of the methyl group to the co-ordinated CO has been found to be the slow
rate-determining step. The metal-to-carbon σ-bonds of third row metals are stronger,
more localized and more covalent than those in second-row metal complexes. A larger
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amount of iridium is required to achieve an activity comparable to the rhodium
catalyst based processes, however the catalyst system is able to operate at lower water
levels (less than 8 wt.%). Hence, there is lower side-product formation and improved
carbon monoxide efficiency is achieved while the steam consumption is also
decreased.
Scheme 1.16. Iridium based Cativa process for the synthesis of acetic acid from
methanol.
The high stability of the iridium catalyst is one of its major advantages. It is
robust at low water concentrations (0.5 wt.%), which is significant and ideal for the
optimization of the methanol carbonylation process. The catalyst remains stable under
a wide range of experimental conditions that would cause similar rhodium analogues
to decompose completely to an inactive and largely unrecoverable rhodium salt.
Iridium is much more soluble than rhodium in the reaction medium which allows the
H2O
HICH3COOH
CH3OH
CH3ICH3COI
Ir
CO
CO
I
I
-
Ir
CO
CO
I
I
-H3C
I
Ir
CO
CO
ICOCH3
I
I-
CO
Ir
CO
CO
I
I
H3C
CO
I-
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use of greater catalyst concentrations, making much higher reaction rates obtainable
[3c].
There are two groups of promoters which affect the reaction, namely simple
iodide complexes of zinc, cadmium, mercury, indium and gallium, and carbonyl
complexes of ruthenium, osmium, rhenium and tungsten [88]. The promoters are
highly successful when combined with iodide salts such as lithium iodide at low water
concentration [89]. The best rate is found at low water conditions. The selectivity of
acetic acid is greater than 99% based on methanol and there are fewer side products
than the Monsanto process.
1.9.1.6. Ligand-accelerated carbonylation of methanol
The migratory insertion reaction of CO into metal-alkyl bonds is a
fundamental step in the metal iodide-catalyzed carbonylation of methanol to acetic
acid (and also in hydroformylation reactions) [90]. The original [RhI2(CO)2]˗ catalyst,
developed at the Monsanto laboratories and studied in detail by Forster and co-
workers, [13] is largely used for the industrial production of acetic acid and anhydride.
However, the conditions used industrially (30–60 bar pressure and 150–200 °C) [91]
have spurred the search for new catalysts, which could work in milder conditions [92].
The rate-determining step of the rhodium-based catalytic cycle is the OA of CH3I, so
that catalyst design focused on the improvement of this reaction. The basic idea was
that ligands which increase the electron density at the metal should promote OA, and
consequently increase the overall rate of the reaction. For this purpose, other rhodium
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compounds have been synthesized in the last few years, which show comparable or
better performance as compared to the Monsanto’s catalyst [92, 93].
1.9.2. Hydrogenation
The two important terms ‘Hydrogenation’ and ‘Transfer Hydrogenation’ have
distinct features i.e. in the former, hydrogen gas (H2) is involved while in the latter,
the hydrogen source must be different from H2.
The study of homogeneous hydrogenation reactions catalyzed by transition
metal complexes has been far more extensive than that of any other catalytic process
in solution [94]. One of the most popular homogeneous catalysts for hydrogenation
reaction is Wilkinson's catalyst, [RhCl(PPh3)3] [9a,95]. Recent survey shows that the
use of asymmetric hydrogenation for the production of fine chemicals is limited, but
expanding [96]. Two major factors that hamper its use are the cost of the catalysts,
and in particular the ligands that are often prepared in a multistep synthesis. However,
the demand for enantiomerically pure compounds with a desired biological activity is
growing rapidly in fine-chemical synthesis. An obvious reason for this development is
that one of the enantiomers of a chiral pharmaceutical or chemical has at best no
activity, or worse, causes side effects. One of the important success stories is the
synthesis of fine chemicals like L-DOPA (Scheme 1.17) by an asymmetric
hydrogenation of prochiral substrates with rhodium(I)-complexes containing optically
active ligand DiPAMP [16]
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Scheme 1.17. Synthesis of L-DOPA
1.9.2.1. Transfer hydrogenation
Environmental concerns in chemistry have increased the demand for more
selective chemical processes with a minimum amount of waste (Green Chemistry).
Hydrogen transfer reactions are mild methodologies for reduction of ketones or imines
and oxidation of alcohols or amines in which a substrate-selective catalyst transfers
hydrogen between the substrate and a hydrogen donor or acceptor, respectively [97].
Furthermore, the donor (e.g. 2-propanol) and the acceptor (e.g. a ketone or a quinone)
are environmentally friendly and also easy to handle. Two main pathways have been
proposed for hydrogen transfer to ketones or aldehydes depending on the type of
metal used. Direct hydrogen transfer is claimed to occur with main group element and
was proposed for the Meerwein-Ponndorf-Verley reduction [98]. This is a concerted
process involving a six-member transition state, in which both the hydrogen donor and
the hydrogen acceptor are coordinated to the metal centre. The hydridic route includes
transition metal catalysts and gives rise to a characteristic metal hydride that involves
in the hydrogen transfer reaction [99].
COOH
NHAc
MeO
AcO
Rh(DiPAMP)
H2
COOH
NHAc
MeO
AcOH
* H3O+ COOH
NH2
HO
HOH
*
P P
OMe
MeO
DiPAMP
Conversion: 100%
Selectivity: 99.5%
[L-DOPA or S-DOPA]
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Bäckvall et al. reported that the hydridic route can be further divided into
metal monohydride and metal dihydride pathways depending on the catalyst used
[100,101]. In the monohydride mechanism, the metal hydride arises purely from the α-
C–H of the hydrogen donor (e.g. 2-propanol), and this M–H is only transferred to the
carbonyl carbon of the substrate and thereby the hydride keeps its identity (Scheme
1.18, path A). In the dihydride pathway the metal hydride arise from both α-C–H and
the OH of the hydrogen donor, and therefore the catalyst does not distinguish between
the proton and the hydride (Scheme 1.18, path B).
Scheme 1.18. Hydridic routes of metal catalyzed transfer hydrogenation
There are two types of catalysts operating through the monohydride
mechanism that have been suggested to operate differently. The formation of the
metal monohydride from the hydrogen donor may involve the formation of a
transition metal alkoxide followed by β-elimination to give the M–H. Alternatively, it
may proceed through a concerted pathway with simultaneous transfer of proton and
hydride from 2-propanol to a basic site of the ligand and to the metal, respectively,
without coordination of the alcohol to the metal. In both pathways the metal hydride
gives rise to the α-C–H.
H1H2O
LnMX
Path A
LnM
Path B
O
O
LnMH1+ + H2X
LnMH1H2+R1 R2
O
R1 R2
O
H1H2O
R2R1
H1H2O
R2R1
H1H2O
R2R1
+
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In the pathway via a transition metal alkoxide a coordinated carbonyl inserts
into the metal hydride 1 and forms metal alkoxide 2 (Scheme 1.19). This insertion
should proceed via π-bonded ketone (metal bound to the double bond). 2-Propanol
exchanges the alkoxide and releases the product. The metal isopropoxide then
undergoes β-elimination forming the metal hydride.
Scheme 1.19. Catalytic cycle via a metal alkoxide.
There is ample support for this alkoxide mechanism [102] and it has been
shown that transition metal hydrides are obtained from β-elimination of the corres-
ponding alkoxide complexes [103]. Even ligand assisted versions of this
transformation have been reported [104]. Many transition metal catalysts are
operating via a metal alkoxide in transfer hydrogenation, for example the Wilkinson
HM
R1 R2
OM
H
insertion
R1 R2
OM
HOHR1 R1
OH
OM
H
O
elimination
R1 R2
O
(1)
(2)
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catalyst [RhCl(PPh3)3] [101]. A common feature of catalysts that are proposed to
operate through a concerted mechanism is that one of the donor atoms of the ligand
acts as a basic centre and activates the substrate. This mechanism was first proposed
by Noyori for 16-electron Ru complexes such as 3 (Scheme 1.20) [105,106].
Scheme 1.20. Catalytic cycle via a concerted six-member transition state.
The reaction cycle involves a simultaneous transfer of the proton and the
hydride from 4 to the carbonyl in a cyclic six-member transition state forming the
alcohol and 3. Then the proton and the hydride from 2-propanol are delivered to
Ru
H2N N
R R
Ts
H R1 R2
O
Ru
N N
R R
Ts
H
H
O
R2
H
R1
R1 R2
OH
Ru
HN N
R R
TsOH
Ru
N N
R R
Ts
H
H
O H
R1 R2
O
(4)
(3)
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the ligand and the metal, respectively, in the same fashion forming 4 and acetone. It is
worth to note that the reaction is proposed to proceed without coordination of either
alcohol or ketone (aldehyde) to the metal (Scheme 1.20).
1.10. Aim and objectives of the Thesis
The literature survey presented here reveals that basic as well as applied
science of organometallic chemistry of platinum group metals particularly rhodium,
iridium and ruthenium have aroused much interest and importance in recent time. The
catalytic processes of carbonylation and hydrogenation reaction find tremendous
importance in industrial production of bulk and fine chemicals. Newer concepts of
ligand design and coordination of metal complexes proceeded promisingly in respect
of catalyst precursors. It is therefore important to synthesize and characterize novel
metal complexes and to determine their reactivities, kinetics of reactions and
applications in different catalytic processes. The specific objectives of the thesis are:
To synthesize and characterize Rh(I), Ir(I) and Ru(II) complexes of symmetrical
/ unsymmetrical chelating functionalized phosphine and nitrogen donor ligands
like P–P, P–X (X = O, S, Se) and N,O.
To study the reactivity [OA reactions, kinetics] of the suitable metal complexes
with the small molecules like CO, O2, CH3I, C2H5I, C6H5CH2Cl etc.
To study the hemilabile nature of different P–X (X = O, S) donor chelating
ligands.
To evaluate the catalytic efficiency of the synthesized complexes for
carbonylation of methanol and transfer hydrogenation of aldehydes and ketones.
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