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Gaseous reagent

Polymerizations were generally carried out as follows Gaseous reagents, i.e.,isobutylene, methyl chloride, were passed through drying columns and condensed in the bath and collected in culture tubes. [Pg.4]

Polymerizations were carried out in Pyrex test tubes in a stainless steel enclosure equipped with a cooling bath, inlets for gaseous reagents and a water analyzer. Nitrogen gas was flushed continuously to maintain a moisture level below 30 ppm. [Pg.90]

The gaseous reagents were distilled and collected inside the enclosure. The 10 vol.% alkylaluminum and 1 vol.% f-butyl halide solutions were freshly prepared. The reaction mixtures were stored manually or by a vortex stirrer. Since PIB tended to precipitate out of solution in highly swollen form, relative rates could thus be established by visual observation. [Pg.90]

We used a similar approach in aprotic solvents and produced bromonium-bromide type intermediates by reacting stilbene bromohydrins with hydrogen bromide using a vigorous stream of the gaseous reagent to strip the Br2 generated by attack of Br to Br+ of the bromonium ion, as shown is Scheme 6 for erythro-2-bromo-1,2-diphenylethanol. [Pg.139]

When the partial pressure of each gaseous reagent is 1 bar and the concentration of each species in solution is 1 M, the conditions are defined to be standard. Under these conditions, the enthalpy change in a formation reaction is the standard enthalpy of formation (A... [Pg.405]

Figure 6.30. Schematic diagram of a reactor used continuously for up to 500 h for fluorous biphasic reactions without gaseous reagents. [81] (A. Yoshidaetal, Development of the continuous-flow reaction system based on the Lewis acid-catalysed reactions in a fluorous biphasic system, Green Chemisty, 5, (2003), 555) Reproduced by permission of The Royal Society of Chemistry. Figure 6.30. Schematic diagram of a reactor used continuously for up to 500 h for fluorous biphasic reactions without gaseous reagents. [81] (A. Yoshidaetal, Development of the continuous-flow reaction system based on the Lewis acid-catalysed reactions in a fluorous biphasic system, Green Chemisty, 5, (2003), 555) Reproduced by permission of The Royal Society of Chemistry.
Multiphase catalytic reactions, such as catalytic hydrogenations and oxidations are important in academic research laboratories and chemical and pharmaceutical industries alike. The reaction times are often long because of poor mixing and interactions between the different phases. The use of gaseous reagents itself may cause various additional problems (see above). As mentioned previously, continuous-flow microreactors ensure higher reaction rates due to an increased surface-to-volume ratio and allow for the careful control of temperature and residence time. [Pg.11]

Hence, in a broader-sense TT may be utilized in a number of reactions with greater efficacy, for instance complexation, precipitation, redox, neutralization. Further, TT can be used to titrate gases against other gases devoid of a liquid-phase and to titrate liquid solutions with gaseous reagents. [Pg.200]

However, if a gaseous reagent or product is involved, the task of homogenisation becomes much more difficult, as the uptake and release of gases from solution are very slow processes. Generally, special designs of agitator are required. [Pg.112]

Carbonylation reactions with microwave irradiation have been investigated in connection with solid-state combinatorial chemistry.Since reactions requiring gaseous reagents cannot use microwave irradiation, metal carbonyl complexes, such as Mo(CO)6, Cr(CO)6, W(CO)6, and Co2(CO)8 have been employed as source of carbon monoxide. " Examples of aminocarbonylation performed with microwave irradiation are presented in Section 11.15.4.3 (vide supra). [Pg.551]

In an interesting application of a gaseous reagent to solid-phase synthesis, Takahashi and co-workers demonstrated hydroformylation of an unactivated alkene using synthetic gas (1 1 H2-CO) and a Rh(I) catalyst (Scheme 8).22 The reaction was typically performed at 40°C in toluene at a pressure of 75 atm. Conversions of 99% were obtained following careful reaction optimization. Variation in the concentration of catalyst could be used to alter the regioselectivity of the reaction. [Pg.206]

Diels-Alder cycloaddition reactions using gaseous reagents. [Pg.254]

Charge the inner vessel of the condenser with acetone-Cardice, surround the flask with a cooling bath of acetone-Cardice, and allow the gaseous reagent to flow slowly through the condenser inlet from a preparative assembly or from a compressed gas cylinder. [Pg.99]

Some SRN1 reactions can take place in the dark and with no catalyst. For example, the interaction of freons with nucleophiles in dimethylformamide at 20°C proceeds without photoirradiation. The chain process begins when the system pressure reaches 2 atm, in other words, when the concentration of the gaseous reagent becomes sufficient (Waksel-man Tordeux 1984) (Scheme 8-7). [Pg.401]


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See also in sourсe #XX -- [ Pg.104 , Pg.188 , Pg.339 ]




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Gaseous reagents, diffusion into liquids

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