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Acid continued oxidative degradation

Sealants obtained by curing polysulfide liquid polymers with aryl bis(nitrile oxides) possess stmctural feature of thiohydroximic acid ester. These materials exhibit poor thermal stability when heated at 60°C they soften within days and liquefy in 3 weeks. Products obtained with excess nitrile oxide degrade faster than those produced with equimolar amounts of reagents. Spectroscopic studies demonstrate that, after an initial rapid addition between nitrile oxide and thiol, a second slower reaction occurs which consumes additional nitrile oxide. Thiohydroximic acid derivatives have been shown to react with nitrile oxides at ambient temperature to form 1,2,4-oxadiazole 4-oxides and alkyl thiol. In the case of a polysulfide sealant, the rupture of a C-S bond to form the thiol involves cleavage of the polymer backbone. Continuation of the process leads to degradation of the sealant. These observations have been supported by thermal analysis studies on the poly sulfide sealants and model polymers (511). [Pg.104]

Although interesterification will occur in the absence of added catalysts at sufficiently high temperatures, catalysts are employed by industry to speed this reaction, reducing reaction time and the sample degradation that occur at elevated temperatures. The most commonly used inorganic catalysts are alkaline ones such as sodium methoxide, sodium ethoxide, sodium or potassium metal, and alloys of sodium and potassium. Catalyst concentrations of 0.05% to 0.1% are employed. As the catalysts will react with water, free fatty acids, and oxidized compounds, it is important to use clean, dry feedstocks. Reaction temperatures are generally kept below 100°C. The reactions can be mn in batch or continuous formats. In batch mode, the reaction times are typically less than an hour. [Pg.232]

The continuing oxidation of gluconic acid to glucaric acid is hindered by the degradation of the oxidized species that occurs during the more prolonged oxidation reaction. The best yields of glucaric acid have been in the 55%-60%... [Pg.562]

The series of four reacdons of j8-oxidation then repeats on the shortened fatty acyl-CoA chain and continues until the entire fatty acid chain is degraded to acetyl-CoA. Seven cycles... [Pg.716]

In general, acetic acid production via acetaldehyde oxidation takes place continuously in a bubble column at 50-80 °C with pressures of 1-10 bar. The construction material of choice for the reactor is austenitic Cr-Ni-steel. The acetic acid product serves as process solvent and the concentration of acetaldehyde is kept at 3%. It is necessary to keep the temperature over 50 °C to obtain a sufficient peroxide decomposition and oxidation rate. To remove the heat of the exothermic reaction, the reaction mixture is circulated through an external heat exchanger. Accurate temperature control is important to decrease oxidative degradation of acetic acid to formic acid, CO2, and water. The reaction mixture is separated by several distillation units. The process yields are typically in the range of 90-97% and the purity of acetic acid is higher than 99%. Typical by-products are CO2, formic acid, methyl acetate, methanol, methyl formate, and formaldehyde. [Pg.742]

Regeneration of the reduced metal ion by redox reaction during catalysis is essential to continue PO degradation. Fe is the thermodynamically favored oxidation state for iron under aerobic and alkaline conditions, whereas Fe is favored under anaerobic and acidic conditions. Under most disposal and environmental conditions Mn " is favored. It is therefore unlikely that a particular metal catalyst will perform equally well in a wide range of disposal situations. Due to environmental pH values it is difficult for such catalysts to be recycled for further free radical generation. Both Fe and Fe " salts can precipitate as insoluble oxides or sulfides under environmental conditions, reducing the polymer degradation potential. [Pg.498]

Polyarylamide has good resistance to most common solvents, aqueous solutions and engine oils. However, it is degraded by strong and concentrated mineral acids, powerful oxidants and strong bases. It is sensitive to certain organic acids and to some solutions of metallic salts. Also, it is recommended that their use should be carefully considered where the product is continuously in contact with water. [Pg.31]


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Acid degradation

Acidity continued

Acids continued

Continuous oxidation

OXIDATION OXIDATIVE DEGRADATION

Oxidations degradative oxidation

Oxidation—continued

Oxidative degradation

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