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Polyol conversion

The catalytic properties of copper during polyols conversion in aqueous phase may be drastically modified by some additives. Metals having a standard oxido-reduction potential higher than that of copper (Ir, Rh, Ru, Pd, Pt, Au) can be deposited on it by oxido-reduction reaction. The first atoms of second metal deposited exchange with hydroxylated... [Pg.229]

Scheme 13.1 Polyol conversion to blocked isocyanates without using either phosgene or isocyanate. CBC = carbonylbisca-prolactam. Scheme 13.1 Polyol conversion to blocked isocyanates without using either phosgene or isocyanate. CBC = carbonylbisca-prolactam.
Montassier C, Menezo JC, Hoang LC, Renaud C, Barbier J (1991) Aqueous polyol conversions on ruthenium and on sulfur-modified ruthenium. J Mol Catal 70 99-110... [Pg.162]

Finally, these compounds may function as osmoregulators as they frequently accumulate in large amounts in plants subject to desiccation or living in environments of high osmotic pressure. Polyols are nonpolar and relatively inert and so may be preferable to other substances such as hexoses. The various roles of polyols in plants and symbiotic associations are discussed in detail by Lewis and Smith (1967) and Smith etal (1969). In lichens experiments have yet to show whether sugar alcohols have all these functions. In particular, the biochemistry and enzymology of the glucose to polyol conversion, or polyol to polyol conversion have yet to be examined. The final fate of much of the transferred carbohydrate in lichens is as protein and polysaccharides such as lichenin. These form the structural com-... [Pg.284]

Soybean oils (SBO) is the main vegetable oil considered for polyol conversion [61, 62]. However, SBO oil is relatively unreactive in typical polymer formulations and, thus, it must be functionalized. For instance, epoxidized soybean oil (ESBO) has received increased attention for the development of ESBO-based PU [62,63] since the presence of epoxy groups has also a strong effect on the thermal stability of PU [46]. [Pg.172]

The boric and sulfuric acids are recycled to a HBF solution by reaction with CaF2. As a strong acid, fluoroboric acid is frequently used as an acid catalyst, eg, in synthesizing mixed polyol esters (29). This process provides an inexpensive route to confectioner s hard-butter compositions which are substitutes for cocoa butter in chocolate candies (see Chocolate and cocoa). Epichlorohydrin is polymerized in the presence of HBF for eventual conversion to polyglycidyl ethers (30) (see Chlorohydrins). A more concentrated solution, 61—71% HBF, catalyzes the addition of CO and water to olefins under pressure to form neo acids (31) (see Carboxylic acids). [Pg.165]

Conversion to acetates, trifluoroacetates (178), butyl boronates (179) trimethylsilyl derivatives, or cycHc acetals offers a means both for identifying individual compounds and for separating mixtures of polyols, chiefly by gas—Hquid chromatography (glc). Thus, sorbitol in bakery products is converted to the hexaacetate, separated, and determined by glc using a flame ionisation detector (180) aqueous solutions of sorbitol and mannitol are similarly separated and determined (181). Sorbitol may be identified by formation of its monobensylidene derivative (182) and mannitol by conversion to its hexaacetate (183). [Pg.52]

The epoxidation is generally conducted in two steps (/) the polyol is added to epichlorohydrin in the presence of a Lewis acid catalyst (stannic chloride, boron triduoride) to produce the chlorohydrin intermediate, and (2) the intermediate is dehydrohalogenated with sodium hydroxide to yield the aliphatic glycidyl ether. A prominent side-reaction is the conversion of aliphatic hydroxyl groups (formed by the initial reaction) into chloromethyl groups by epichlorohydrin. The aliphatic glycidyl ether resins are used as flexibilizers for aromatic resins and as reactive diluents to reduce viscosities in resin systems. [Pg.366]

This reaction is reported to proceed at a rapid rate, with over 25% conversion in less than 0.001 s [3]. It can also proceed at very low temperatures, as in the middle of winter. Most primary substituted urea linkages, referred to as urea bonds, are more thermally stable than urethane bonds, by 20-30°C, but not in all cases. Polyamines based on aromatic amines are normally somewhat slower, especially if there are additional electron withdrawing moieties on the aromatic ring, such as chlorine or ester linkages [4]. Use of aliphatic isocyanates, such as methylene bis-4,4 -(cyclohexylisocyanate) (HnMDI), in place of MDI, has been shown to slow the gelation rate to about 60 s, with an amine chain extender present. Sterically hindered secondary amine-terminated polyols, in conjunction with certain aliphatic isocyanates, are reported to have slower gelation times, in some cases as long as 24 h [4]. [Pg.763]

These results have been fit to experimental data obtained for the reaction between a diisocyanate and a trifunctional polyester polyol, catalyzed by dibutyltindilaurate, in our laboratory RIM machine (Figure 2). No phase separation occurs during this reaction. Reaction order, n, activation energy, Ea, and the preexponential factor. A, were taken as adjustable parameters to fit adiabatic temperature rise data. Typical comparison between the experimental and numerical results are shown in Figure 7. The fit is quite satisfactory and gives reasonable values for the fit parameters. Figure 8 shows how fractional conversion of diisocyanate is predicted to vary as a function of time at the centerline and at the mold wall (remember that molecular diffusion has been assumed to be negligible). [Pg.157]

Schemes 14 and 15 outline the polyol chain assembly. Alkylation of cyanohydrin 93 with iodide 94 provided the chlorocyanohydrin 95, which was converted to the required iodide (96). A second alkylation of 93, this time with 96, provided bisacetonide 97 in 70-80% yield. Conversion of 97 to iodide 87 completed the synthesis of the C6-C15 fragment. Schemes 14 and 15 outline the polyol chain assembly. Alkylation of cyanohydrin 93 with iodide 94 provided the chlorocyanohydrin 95, which was converted to the required iodide (96). A second alkylation of 93, this time with 96, provided bisacetonide 97 in 70-80% yield. Conversion of 97 to iodide 87 completed the synthesis of the C6-C15 fragment.
The slow water removal is obvious within the synthesis of, for example, myristyl myristate determining the total reaction time. In a stirred-tank reactor it takes 24 h to reach a conversion of 99.6% and in a fixed-bed reactor 14 h. Therefore, a new synthesis platform (Figure 4.11) which also enables conversion of highly viscous polyols and fatty acids from renewable resources to ester-based surfactants was designed. It is used by Evonik on a pilot scale, outperforming conventional methods, such as stirred-tank or fixed-bed reactors. In contrast to the setups introduced before, conversion of >99.6% is already obtained after 5.5 h in the bubble column reactor [44-47]. [Pg.90]

The above observations provide a clear demonstration that cosolvents in selected ranges of concentration create reversible perturbations of protein similar to those induced by other modifiers. The reversibility of the cosolvent effect is a prerequisite to cosolvent use and will depend on the concentration of cosolvent, which in turn will vary markedly with the type of solvent used. For instance, polyols can be used at concentrations up to 8 Af while methanol at 3 M causes the appearance of a new absorption band (410 nm) and, after further increases in concentration, an irreversible conversion of cytochrome P-450 into P-420. Other aliphatic alcohols cause denaturation at much lower concentrations. [Pg.270]

Due to the necessity for aromatic structure in the commodity isocyanates, and the intensive chemical conversions required to derive the isocyanate reactant, no high-carbon frameworks derived principally from plant sources have been developed into isocyanates. The majority of the derivation of raw materials from high carbon conjugates has been focused on the development of polyols, for which the structural demands are a better fit for available renewable feedstocks. Although there are some notable exceptions [1], as a general rule modification of the... [Pg.317]

The isoxazoline-furanose intermediate derived from h/i(hydroxylation) was also submitted to direct hydrogenation. The reduction proceeded in a highly diaster-eoselective manner at the C=N double bond. In the gluco series starting with 150, several deoxynojirimycin analogues with extended side chains at C-5 (carbohydrate numbering) such as 151 were obtained by this method (23,313,314). Eurther conversion of 151 led to indolizidine polyols (1,4,8-trideoxyimino polyols), which... [Pg.434]

Another catalyst which may also involve a homogeneous catalysis mechanism is barium hydroxide. Barium hydroxide has been reported to catalyze the methanolysis of rapeseed oil at 65°C with over 80% of oil conversion in less than an hour. " However, Ba(OH)2 shows non-negligible solubility in water, methanol and polyols. " For instance, in alcohols Ba(OH)2 can form barium alcoholates (RO Ba OH and RO Ba-OR). A barium alcoholate of formula... [Pg.80]


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See also in sourсe #XX -- [ Pg.296 ]




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