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Oxidation during

Note. (1) Most sulphur compounds are completely oxidised if the tube is heated under the conditions described for the estimation of halogens. Sul-phonic acids and sulphones are more difficult to oxidise completely and the tube should be slowly heated to 300 and maintained at this temperature for at least 6 hours. The oxidation may be facilitated by adding a few crystals of sodium or potassium bromide to the organic material in the small tube, so that bromine shall be present to intensify the oxidation during the heating. [Pg.424]

Further evidence pointing in the same direction was provided by Pierce, Wiley and Smith, who found that on steam activation of a particular char at 900°C the saturation uptake increased three-fold, yet the isotherm was still of Type I. They argued that even if the width of the pores was only two molecular diameters before activation, it would increase, by removal of oxides, during the activation so that the second Type I isotherm would correspond to pores more than two molecular diameters wide. (The alternative explanation, that activation produced new pores of the same width as the old, seems unlikely.)... [Pg.200]

DRI can be produced in pellet, lump, or briquette form. When produced in pellets or lumps, DRI retains the shape and form of the iron oxide material fed to the DR process. The removal of oxygen from the iron oxide during direct reduction leaves voids, giving the DRI a spongy appearance when viewed through a microscope. Thus, DRI in these forms tends to have lower apparent density, greater porosity, and more specific surface area than iron ore. In the hot briquetted form it is known as hot briquetted iron (HBI). Typical physical properties of DRI forms are shown in Table 1. [Pg.424]

The electrolyte is prepared by dipping granulated lead, suspended in a basket, into and out of the fluosUicic acid. The lead oxidizes during the operation and lead fluosUicate is formed ... [Pg.47]

The tendency of aliphatic ethers toward oxidation requires the use of antioxidants such as hindered phenoHcs (eg, BHT), secondary aromatic amines, and phosphites. This is especially tme in polyether polyols used in making polyurethanes (PUR) because they may become discolored and the increase in acid number affects PUR production. The antioxidants also reduce oxidation during PUR production where the temperature could reach 230°C. A number of new antioxidant products and combinations have become available (115,120,124—139) (see Antioxidants). [Pg.353]

A small but important use of ammonium nitrate is in the production of nitrous oxide during the 1980s consumption for this purpose averaged about 30,000 t. The gas is generated by controlled heating of ammonium nitrate above 200°C. Nitrous oxide is used primarily as an anesthetic and as an aerosol propellant for food products (see Anesthetics Aerosols). [Pg.367]

Flaws in the anodic oxide film are usually the primary source of electronic conduction. These flaws are either stmctural or chemical in nature. The stmctural flaws include thermal crystalline oxide, nitrides, carbides, inclusion of foreign phases, and oxide recrystaUi2ed by an appHed electric field. The roughness of the tantalum surface affects the electronic conduction and should be classified as a stmctural flaw (58) the correlation between electronic conduction and roughness, however, was not observed (59). Chemical impurities arise from metals alloyed with the tantalum, inclusions in the oxide of material from the formation electrolyte, and impurities on the surface of the tantalum substrate that are incorporated in the oxide during formation. [Pg.331]

Because nitrile rubber is an unsaturated copolymer it is sensitive to oxidative attack and addition of an antioxidant is necessary. The most common practice is to add an emulsion or dispersion of antioxidant or stabilizer to the latex before coagulation. This is sometimes done batchwise to the latex in the blend tank, and sometimes is added continuously to the latex as it is pumped toward further processing. PhenoHc, amine, and organic phosphite materials are used. Examples are di-Z fZ-butylcatechol, octylated diphenylamine, and tris(nonylphenyl) phosphite [26523-78-4]. All are meant to protect the product from oxidation during drying at elevated temperature and during storage until final use. Most mbber processors add additional antioxidant to their compounds when the NBR is mixed with fillers and curatives in order to extend the life of the final mbber part. [Pg.521]

The near-surface region is partially oxidized during OJ bombardment. During the sputter process the chemical bonding of the oxides is broken. Because the binding... [Pg.111]

The advantages of thermal incineration are that it is simple in concept, has a wide application, and results in almost complete destruction of pollutants with no liquid or solid residue. Thermal incineration provides an opportunity for heat recovery and has low maintenance requirements and low capital cost. Thermal incineration units for small or moderate exhaust streams are generally compact and light. Such units can be installed on a roof when the plant area is limited. = The main disadvantage is the auxiliary fuel cost, which is partly offset with an efficient heat-recovery system. The formation of nitric oxides during the combustion processes must be reduced by control of excess air temperature, fuel supply, and combustion air distribution at the burner inlet, The formation of thermal NO increases dramatically above 980 Table 13.10)... [Pg.1256]

Romijn, J. A., Coyle, E. R, Sidossis, L. S., et al., 1996. Relationship between fatty acid delivery and fatty acid oxidation during strenuous exercise. Journal of Applied Physiology 79 1939—1945. [Pg.801]

Biodiesel does not present any special safety concerns. Pure biodiesel or biodiesel and petroleum diesel blends have a higher flash point than conventional diesel, making them safer to store and handle. Problems can occur with biodiesels in cold weather due to their high viscosity. Biodiesel has a higher degree of unsaturation in the fuel, which can make it vulnerable to oxidation during storage. [Pg.162]


See other pages where Oxidation during is mentioned: [Pg.95]    [Pg.263]    [Pg.32]    [Pg.115]    [Pg.56]    [Pg.328]    [Pg.34]    [Pg.498]    [Pg.501]    [Pg.530]    [Pg.452]    [Pg.143]    [Pg.158]    [Pg.241]    [Pg.246]    [Pg.246]    [Pg.372]    [Pg.171]    [Pg.73]    [Pg.578]    [Pg.40]    [Pg.465]    [Pg.167]    [Pg.323]    [Pg.1238]    [Pg.2229]    [Pg.911]    [Pg.130]    [Pg.139]    [Pg.176]    [Pg.37]    [Pg.374]    [Pg.638]    [Pg.728]    [Pg.700]    [Pg.1230]    [Pg.325]    [Pg.171]    [Pg.1015]   
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Absorption oxidation during

Allylic alcohols rearrangement during oxidation

Assumptions in SO2 oxidation calculations 100% SO3 utilization during

Catalysts changes during partial oxidation

Characterization of surface processes during oxide CMP by in situ FTIR spectroscopy

Chemical Composition of Sherry Wines During the Biological and Oxidative Aging

Control of polymer oxidation during processing and use

Deformation and failure of oxide scale during hot rolling

Energy during glucose oxidation

Formation of Nitrogen Oxides during Fuel Combustion in Power Plants

Formation of nitrogen oxides during coal combustion

Free radical reactions during oxidation

Heat transfers during catalytic oxidation

Hydrocarbons activation during oxidation

Isomerization during oxidation, selectivity

Mechanisms involved in the photolysis of thermally oxidized polyolefins during processing

Nitric oxide during adsorption

Nitric oxide radical production during

Nitrogen SO2 oxidation, no reaction during

Oscillations during formaldehyde oxidation

Oscillations during methanol oxidation

Oxidation Level Changes During Reactions

Oxidation absorbance changes’ phases during

Oxidation behaviour of Fe-Cr-AI alloys during resistance and furnace heating

Oxidation during drying

Oxidation during long-term storage

Oxidation during meat storage

Oxidation of Encapsulated Flavor During Storage

Oxidation preventing during extraction

Oxidation state during reaction

Oxidation steady state multiplicity during

Oxidation, during sample preparation

Oxidation, radical species present during

Oxidative aging chemical changes during

Oxidative phosphorylation during exercise

Oxidative stress during aging

Oxide surfaces during catalytic reactions

Production during char oxidation

Production during methane oxidation

Proteins, changes during lipid oxidation

Reactions Performed in situ During Oxidation with IBX

Reactions Performed in situ During an Oppenauer Oxidation

Reactive oxidant production during the respiratory burst

Release and Oxidation of the Encapsulated Flavor During Storage

Shelf storage, oxidation during

Standing during formic acid oxidation

Structural during formic acid oxidation

The Morphological Stability of Boundaries During Metal Oxidation

Viscosity increase during oxidation

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