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Methane metathesis

Another important point that must be borne in mind is that failure to account for tunneling, or to recognize its contribution in die first place, can lead to significant errors in the interpretation of experimental data. For example, Watson (1990) analyzed an Eyring plot of apparent rate constants for methane metathesis by methyllutetiocene (Figure 15.5) to infer... [Pg.536]

Figure 15.5 Transition-state structure for rate-determining hydrogen atom transfer in the methane metathesis reaction of methyllutetiocene. Note that the kinetics for this narcissistic reaction may be followed by using a label either in the reacting methane or in the methyl group of the starting organometallic... Figure 15.5 Transition-state structure for rate-determining hydrogen atom transfer in the methane metathesis reaction of methyllutetiocene. Note that the kinetics for this narcissistic reaction may be followed by using a label either in the reacting methane or in the methyl group of the starting organometallic...
Woodrum NL, Cramer CJ (2006) Density functional characterization of methane metathesis with Cp 2MR (M = Sc, Y, Lu R = Me, BuCH2). Structural and kinetic consequences of alkyl steric bulk. Organometallics 25 68-73... [Pg.35]

While alkane metathesis is noteworthy, it affords lower homologues and especially methane, which cannot be used easily as a building block for basic chemicals. The reverse reaction, however, which would incorporate methane, would be much more valuable. Nonetheless, the free energy of this reaction is positive, and it is 8.2 kj/mol at 150 °C, which corresponds to an equihbrium conversion of 13%. On the other hand, thermodynamic calculation predicts that the conversion can be increased to 98% for a methane/propane ratio of 1250. The temperature and the contact time are also important parameters (kinetic), and optimal experimental conditions for a reaction carried in a continuous flow tubiflar reactor are as follows 300 mg of [(= SiO)2Ta - H], 1250/1 methane/propane mixture. Flow =1.5 mL/min, P = 50 bars and T = 250 °C [105]. After 1000 min, the steady state is reached, and 1.88 moles of ethane are produced per mole of propane consmned, which corresponds to a selectivity of 96% selectivity in the cross-metathesis reaction (Fig. 4). The overall reaction provides a route to the direct transformation of methane into more valuable hydrocarbon materials. [Pg.184]

Fig. 4 Methane-propane cross-metathesis catalyzed by tantalum hydride supported on silica... Fig. 4 Methane-propane cross-metathesis catalyzed by tantalum hydride supported on silica...
Additionally, grafting molecular entities on surfaces has already allowed to discover several reactions the low temperature hydrogenolysis of alkanes including the depolymerization of polyolefins, the alkane metathesis and the cross-metathesis of methane and alkanes. These two latter reactions can allow higher molecular weight alkanes to be built. [Pg.185]

The mechanism for the reaction catalyzed by cationic palladium complexes (Scheme 24) differs from that proposed for early transition metal complexes, as well as from that suggested for the reaction shown in Eq. 17. For this catalyst system, the alkene substrate inserts into a Pd - Si bond a rather than a Pd-H bond [63]. Hydrosilylation of methylpalladium complex 100 then provides methane and palladium silyl species 112 (Scheme 24). Complex 112 coordinates to and inserts into the least substituted olefin regioselectively and irreversibly to provide 113 after coordination of the second alkene. Insertion into the second alkene through a boat-like transition state leads to trans cyclopentane 114, and o-bond metathesis (or oxidative addition/reductive elimination) leads to the observed trans stereochemistry of product 101a with regeneration of 112 [69]. [Pg.241]

The observed methane generation points to a plausible I —> III or II - III transformation, but it does not distinguish which of the structures (II or III) is the metathesis-active carbene. This matter is mechanistically significant with regard to the chain termination process. Type III may terminate by a bimolecular dimerization sequence as in Eq. (11), or it may convert to a 7r-olefin complex via an uncommon 1,2-hydride shift ... [Pg.454]

As a simple model for the cr-metathesis pathway, let us examine the key orbital interactions for reaction of H2 with Hfl-FMe to produce HfH4 and methane ... [Pg.499]

Fig. 4. Relevant structures for the discussion of methane activation by (bipyrimi-dine)PtCl2 Methane complex of Pt(II) (A) methyl(hydrido)platinum(IV) complex, the product of the oxidative addition (B) transition state for intramolecular deprotonation of the methane complex ( cr-bond metathesis , sometimes also called electrophilic , C) intermolecular deprotonation of the methane complex ( electrophilic pathway , D). Fig. 4. Relevant structures for the discussion of methane activation by (bipyrimi-dine)PtCl2 Methane complex of Pt(II) (A) methyl(hydrido)platinum(IV) complex, the product of the oxidative addition (B) transition state for intramolecular deprotonation of the methane complex ( cr-bond metathesis , sometimes also called electrophilic , C) intermolecular deprotonation of the methane complex ( electrophilic pathway , D).
In a study of the methane complex [(diimine)Pt(CH3)(CH4)]+ (diimine = HN=C(H)-C(H)=NH), relevant to the diimine system experimentally investigated by Tilset et al. (28), theoretical calculations indicate preference for the oxidative addition pathway (30). When one water molecule was included in these calculations, the preference for oxidative addition increased due to the stabilization of Pt(IV) by coordinated water (30). The same preference for oxidative addition was previously calculated for the ethylenediamine (en) system [(en)Pt(CH3)(CH4)]+ (151). This model is relevant for the experimentally investigated tmeda system [(tmeda)Pt(CH3)(solv)]+ discussed above (Scheme 7, B) (27,152). For the bis-formate complex Pt(02CH)2, a a-bond metathesis was assumed and the energies of intermediates and transition states were calculated... [Pg.290]

Hydrogen abstraction from methane by Cl and H occurs via the following bimolecular metathesis reactions ... [Pg.156]

This is a major achievement, mainly due to Basset and his group, in surface organometallic chemistry because it has been thus possible to prepare single site catalysts for various known or new catalytic reactions [53] such as metathesis of olefins [54], polymerization of olefins [55], alkane metathesis [56], coupHng of methane to ethane and hydrogen [57], cleavage of alkanes by methane [58], hydrogenolysis of polyolefins [59] and alkanes [60], direct transformation of ethylene into propylene [61], etc. These topics are considered in detail in subsequent chapters. [Pg.17]

In the presence of an acyclic alkane, 3 catalyzes at moderate temperature (25-200 °C) the metathesis reaction, leading to the formation of heavier and lower homolog alkanes by simultaneous breaking and formation of C-H and C-C bonds. For example, propane is transformed, even at 25 °C into a quasi-equimolar mixture of ethane and butanes (n- and iso-mixture) as well as methane and pentanes, in lower quantities. Lower and heavier homologs are also obtained starting from... [Pg.87]

Alkane metathesis can also formally appear as the breaking and reformation of one C-H and one C-C bonds. Scheme 3.7 shows, for example, the case of ethane where methane and propane are produced ... [Pg.88]

The most important difference between Chauvin s mechanism for olefin metathesis and the mechanism for alkane metathesis is that the latter applies itself to the reverse reaction of cleavage of alkanes by methane (which has no single C-C bond, see below) and, especially, it is based on a metal hydrido-carbene in equi-Ubrium with a metal-alkyl. [Pg.91]

Methane-Propane Cross-Metathesis ( Alkane Methane-olysis )... [Pg.93]

Reaction between methane and propane requires the right conditions. Firstly, it has a positive free energy of AG° = -1- 2kcalmoT at 150 °C for amethane/propane ratio of 1 but this can be overcome by increasing this ratio, which for a value of 1250 allows 98% propane conversion at 250°C. Secondly, it has to be separated from other reactions catalyzed by tantalum hydride, such as propane hydrogenoly-sis, leading to 1 equiv. of methane and 1 equiv. of ethane, or propane metathesis, leading to 0.5 equiv. of ethane ... [Pg.94]


See other pages where Methane metathesis is mentioned: [Pg.7]    [Pg.10]    [Pg.35]    [Pg.7]    [Pg.10]    [Pg.35]    [Pg.477]    [Pg.215]    [Pg.418]    [Pg.4]    [Pg.230]    [Pg.316]    [Pg.151]    [Pg.180]    [Pg.184]    [Pg.151]    [Pg.102]    [Pg.288]    [Pg.289]    [Pg.323]    [Pg.136]    [Pg.99]    [Pg.140]    [Pg.79]    [Pg.86]    [Pg.92]    [Pg.93]   
See also in sourсe #XX -- [ Pg.10 ]




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