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Composite decomposition

Sample Entry Coblock type Coblock Composition Decomposition temperature, °C Isothermal wt. Thermal Ex-Loss 400 °C pansion Coef-(N2), wt% ficient, ppm ... [Pg.77]

Write a word equation for the chemical changes that produced the two whiting compounds CaC03 (calcium carbonate), sometimes called precipitated chalk, and Ca(OH)2 (calcium hydroxide), sometimes called slaked lime. After writing the equations, find for each equation the correct classification composition, decomposition, single displacement, or double displacement (see the next subsection, An Artist s Materials and Chemical Change ). [Pg.124]

Chemistry plays an important role on earth. Life is actually all just chemistry and consists in large part of natural chemical substances and processes that allow for life and continued existence on Earth. Every being plays host to all kinds of natural chemical processes in all vital parts of the body. Composition, decomposition and the circulation of matter in the body are all chemical processes. [Pg.22]

If there is no constant influx of fluid of a certain composition, decomposition of magnetite ceases. The limiting case is a dry system closed to CO2. By analogy with systems closed to water, in such a system with constant pressure P — Pf = const) the fluid phase disappears entirely, and the Mgt + Sid + Hem association (system Fe-C-O) becomes bivariant and can exist stably below the P-T curve (see Fig. 77) in the stability field of the Sid -1- Hem (+ fluid) association. From these considerations the Mgt -I- Sid + Hem association cannot be used to judge the low-temperature limit of mineral formation the upper limit is fixed quite definitely inasmuch as removal of CO2 begins at P P and the reaction proceeds irreversibly to the right. The extensive occurrence of magnetite in oxide-carbonate iron-formations of low-rank metamorphism apparently indicates the absence of equilibrium or even a deficiency of COj and special dry conditions. [Pg.222]

Gas composition Decomposition on heating AC Perovskite formation on heatingAC Decomposition on cooUngAC Equilibrium 3-phase field rangeAC... [Pg.90]

Composition Decomposition on heating/OsJ mol ) Perovskite formation on heating/QnJ moF )... [Pg.93]

Since various motions mentioned occur on various time scales, it is worthwhile to cover a wide range of frequencies. An important advantage of DRS over other spectroscopic techniques is the capability to explore a range of timescales from as slow as 10" s to as fast as 10 " s. Therefore, this single technique allows to study a broad spectrum of motions as a function of temperature, pressure, or composition. Decomposition of DRS spectra into constituents corresponding to various processes is needed. A procedure for doing this which handles also the temperature dependencies of relaxational processes has been devised by Schlosser and his colleagues [91]. [Pg.664]

TGA Weight loss measurement Moisture content Thermal stability QC testing Chemical stability Chemical composition Decomposition kinetics Catalyst activity... [Pg.306]

Chemical stability Chemical composition Decomposition kinetics Catalyst activity Chemical stability Chemical composition Decomposition kinetics Extent of rate of resin cure Catalyst activity Chemical stability Chemical composition Decomposition kinetics Extent of rate of resin cure Resin cure kinetics Catalyst activity Polymer decomposition Identification of volatiles Polymer decomposition Identification of volatiles... [Pg.155]

If the light and heavy key components form an azeotrope, then something more sophisticated than simple distillation is required. The first option to consider when separating an azeotrope is exploiting change in azeotropic composition with pressure. If the composition of the azeotrope is sensitive to pressure and it is possible to operate the distillation over a range of pressures without any material decomposition occurring, then this property can be used to... [Pg.78]

The Beckstead-Derr-Price model (Fig. 1) considers both the gas-phase and condensed-phase reactions. It assumes heat release from the condensed phase, an oxidizer flame, a primary diffusion flame between the fuel and oxidizer decomposition products, and a final diffusion flame between the fuel decomposition products and the products of the oxidizer flame. Examination of the physical phenomena reveals an irregular surface on top of the unheated bulk of the propellant that consists of the binder undergoing pyrolysis, decomposing oxidizer particles, and an agglomeration of metallic particles. The oxidizer and fuel decomposition products mix and react exothermically in the three-dimensional zone above the surface for a distance that depends on the propellant composition, its microstmcture, and the ambient pressure and gas velocity. If aluminum is present, additional heat is subsequently produced at a comparatively large distance from the surface. Only small aluminum particles ignite and bum close enough to the surface to influence the propellant bum rate. The temperature of the surface is ca 500 to 1000°C compared to ca 300°C for double-base propellants. [Pg.36]

Fig. 1. The postulated flame stmcture for an AP composite propellant, showing A, the primary flame, where gases are from AP decomposition and fuel pyrolysis, the temperature is presumably the propellant flame temperature, and heat transfer is three-dimensional followed by B, the final diffusion flame, where gases are O2 from the AP flame reacting with products from fuel pyrolysis, the temperature is the propellant flame temperature, and heat transfer is three-dimensional and C, the AP monopropellant flame where gases are products from the AP surface decomposition, the temperature is the adiabatic flame temperature for pure AP, and heat transfer is approximately one-dimensional. AP = ammonium perchlorate. Fig. 1. The postulated flame stmcture for an AP composite propellant, showing A, the primary flame, where gases are from AP decomposition and fuel pyrolysis, the temperature is presumably the propellant flame temperature, and heat transfer is three-dimensional followed by B, the final diffusion flame, where gases are O2 from the AP flame reacting with products from fuel pyrolysis, the temperature is the propellant flame temperature, and heat transfer is three-dimensional and C, the AP monopropellant flame where gases are products from the AP surface decomposition, the temperature is the adiabatic flame temperature for pure AP, and heat transfer is approximately one-dimensional. AP = ammonium perchlorate.
Aromatic diacyl peroxides such as dibenzoyl peroxide (BPO) [94-36-0] may be used with promoters to lower the usehil decomposition temperatures of the peroxides, although usually with some sacrifice to radical generation efficiency. The most widely used promoter is dimethylaniline (DMA). The BPO—DMA combination is used for hardening (curing) of unsaturated polyester resin compositions, eg, body putty in auto repair kits. Here, the aromatic amine promoter attacks the BPO to initially form W-benzoyloxydimethylanilinium benzoate (ion pair) which subsequentiy decomposes at room temperature to form a benzoate ion, a dimethylaniline radical cation, and a benzoyloxy radical that, in turn, initiates the curing reaction (33) ... [Pg.223]

Some of the composition adjustments in the Alnicos result in a high Curie temperature so that the decomposition reaction can take place relatively rapidly below This is particularly tme for Co, which is 24 wt % or greater for the anisotropic magnets. Another important consideration is the suppression of nonmagnetic fee y-phase which may appear at 1000—1100°C in this regard, the amount of Al, which is a y-suppressor, is critical. The formation of y is pronounced if the Al content falls much below 7—8 wt %. [Pg.380]

Basic oxides of metals such as Co, Mn, Fe, and Cu catalyze the decomposition of chlorate by lowering the decomposition temperature. Consequendy, less fuel is needed and the reaction continues at a lower temperature. Cobalt metal, which forms the basic oxide in situ, lowers the decomposition of pure sodium chlorate from 478 to 280°C while serving as fuel (6,7). Composition of a cobalt-fueled system, compared with an iron-fueled system, is 90 wt % NaClO, 4 wt % Co, and 6 wt % glass fiber vs 86% NaClO, 4% Fe, 6% glass fiber, and 4% BaO. Initiation of the former is at 270°C, compared to 370°C for the iron-fueled candle. Cobalt hydroxide produces a more pronounced lowering of the decomposition temperature than the metal alone, although the water produced by decomposition of the hydroxide to form the oxide is thought to increase chlorine contaminate levels. Alkaline earths and transition-metal ferrates also have catalytic activity and improve chlorine retention (8). [Pg.485]


See other pages where Composite decomposition is mentioned: [Pg.123]    [Pg.126]    [Pg.212]    [Pg.254]    [Pg.613]    [Pg.1126]    [Pg.261]    [Pg.123]    [Pg.126]    [Pg.212]    [Pg.254]    [Pg.613]    [Pg.1126]    [Pg.261]    [Pg.357]    [Pg.2525]    [Pg.24]    [Pg.270]    [Pg.6]    [Pg.318]    [Pg.322]    [Pg.34]    [Pg.284]    [Pg.304]    [Pg.66]    [Pg.288]    [Pg.382]    [Pg.225]    [Pg.515]    [Pg.44]    [Pg.236]    [Pg.15]    [Pg.43]    [Pg.133]    [Pg.166]    [Pg.301]   


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