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C thermal

Compare and contrast the following pairs of compounds as regards (a) methods of preparation, (b) important properties including hydrolysis, (c) thermal stability ... [Pg.255]

Polymer T,°C TJC Softening temperature,°C Thermal degradation temperature,°C... [Pg.314]

PVDE is not hazardous under typical processing conditions. If the polymer is accidentaky exposed to temperatures exceeding 350°C, thermal decomposition occurs with evolution of toxic hydrogen fluoride (HE). [Pg.388]

Metal Crystal 22° C stmeture 1000° c Melting point, °C Density, g/cm Thermal expansion coefficient at RT, ioV°c Thermal conductivity at RT, W/(m-K)" Young s modulus, GPa "... [Pg.109]

Operating parameters of this German plant, on the basis of one cubic meter of raw gas, iaclude 0.139 m O2, 0.9 kg briquettes, 1.15 kg steam, 1.10 kg feed water, 0.016 kWh, and 1.30 kg gas Hquor produced. Gasifier output is 1850 m /h and gas yield is 1465 m /t dry, ash-free coal. The coal briquettes have a 19% moisture content, 7.8% ash content (dry basis), and ash melting poiat of 1270°C. Thermal efficiency of the gas production process is about 60%, limited by the quaHty and ash melting characteristics of the coal. Overall efficiency from raw coal to finished products is less than 50%. [Pg.159]

Material CAS Registry Number Formula Mp, °C Tme specific gravity, g/cm Mean J/(kg-K)" specific heat Temp range, °C Thermal conductivity, W/(m-K) 500° 1000° C C Linear thermal expansion coefficient peTC X 10 from 20-1000°C... [Pg.26]

Fig. 8. Blackbody and furnace A, furnace shell B, furnace tube C, thermal insulation D, heater winding E, outer wall of graphite cmcible F, pure metal... Fig. 8. Blackbody and furnace A, furnace shell B, furnace tube C, thermal insulation D, heater winding E, outer wall of graphite cmcible F, pure metal...
AUoy Constituents, wt % Be Co Density, g/mL Elastic modulus GPa Thermal expansion coefficient, ppm/°C Thermal conductivity, W/(m-K) Melting range, °C... [Pg.70]

As chlorination proceeds from methyl chloride to carbon tetrachloride, the length of the C—Cl bond is decreased from 0.1786 nm in the former to 0.1755 nm in the latter (3). At ca 400°C, thermal decomposition of carbon tetrachloride occurs very slowly, whereas at 900—1300°C dissociation is extensive, forming perchloroethylene and hexachloroethane and Hberating some chlorine. Subjecting the vapor to an electric arc also forms perchloroethylene and hexachloroethane, as well as hexachlorobenzene, elementary carbon, and chlorine. [Pg.530]

Fig. 6. Catalyst inhibition mechanisms where ( ) are active catalyst sites the catalyst carrier and the catalytic support (a) masking of catalyst (b) poisoning of catalyst (c) thermal aging of catalyst and (d) attrition of ceramic oxide metal substrate monolith system, which causes the loss of active catalytic material resulting in less catalyst in the reactor unit and eventual loss in performance. Fig. 6. Catalyst inhibition mechanisms where ( ) are active catalyst sites the catalyst carrier and the catalytic support (a) masking of catalyst (b) poisoning of catalyst (c) thermal aging of catalyst and (d) attrition of ceramic oxide metal substrate monolith system, which causes the loss of active catalytic material resulting in less catalyst in the reactor unit and eventual loss in performance.
Density (g/cm2) Melting Point (°C) Coefficient of Expansion X IQ-6 (°C) Thermal Conductivity (W/m °C) Vield Tensile Strength Modulus (N/mm2) (N/mm2) Hardness (DPN)... [Pg.93]

Material >ensity (kg/m ) Specific heat (kJ/kg K) Thermal conductivity (W/m/K) Coeff. of therm exp (/Am/m/ C) Thermal dififusivity (m /s) X 10" Glass transition Temp, TgCO Max. operating, Temp (°C)... [Pg.31]

Polyfluoroparafins, fluorocarbons, and other perfluoro denvatives show remarkable heat stability They are usually stable at temperatures below 300 C Thermal decomposition at 500-800 °C, however, causes all possible splits in the molecules and produces complex mixtures that are difficult to separate For preparative purposes, only pyrolyses that do not yield complicated mixtures of products are of interest [7] The pyrolytic reacpons of polyfluoro and perfluoro derivatives, when carried out at 500-11 Ofl °C, represent the most useful route to preparative generation of perfluoroolefins on the laboratory scale [7]... [Pg.918]

Melting point, °C Thermal expansion, 10 in./in. Specific volume, cm /lb... [Pg.332]

Melting point (°C) Boiling point (°C) Density (g/cm ) Specific heat (J/g°C) Thermal conductivity (W/cm C) Resistivity (jiQ/cm at 20°C) Co cient of thermal expansion (xl0-V C) Cross section thermal neutrons (barns/atom)... [Pg.853]

Density (g/cm Melting point ( Q Boiling point (°C) Thermal neutron absorption cross section (barn/atom) Linear , Thermal coeff. of conductivity 7 7 (W/cm C) Specific heat (J/g°C) Electrical resistivity (ufl/cm) Temperature coeff. of resistivity (°C)... [Pg.891]

Metal A lomic number Atomic weight Lattice structure Density at 20°C (g/em ) Melting point (°C) Thermal conductivity at 0-l00°C (W/m°C) Specific heat at 0°C (J/kg C) Coefficient of linear expansion at 20-iOO°C X 70 Thermal neutron cross-section (barns) (10-- m ) Resistivity at 0°C (fiil em) Temperature coefficient of resistance o-ioo°c X 10 ... [Pg.924]

Harris, S. J., Green, P. D. and Cobb, R. C., Thermally Sprayed Al-Zn-In-Sn Alloys in 3rd Int. Conf. on Advances in Surface Engineering for Corrosion and Wear Resistance, Newcastle-upon-Tyne, 1-10(1992)... [Pg.479]

Loop Tests Loop test installations vary widely in size and complexity, but they may be divided into two major categories (c) thermal-convection loops and (b) forced-convection loops. In both types, the liquid medium flows through a continuous loop or harp mounted vertically, one leg being heated whilst the other is cooled to maintain a constant temperature across the system. In the former type, flow is induced by thermal convection, and the flow rate is dependent on the relative heights of the heated and cooled sections, on the temperature gradient and on the physical properties of the liquid. The principle of the thermal convective loop is illustrated in Fig. 19.26. This method was used by De Van and Sessions to study mass transfer of niobium-based alloys in flowing lithium, and by De Van and Jansen to determine the transport rates of nitrogen and carbon between vanadium alloys and stainless steels in liquid sodium. [Pg.1062]

C. Thermal degradation of polyazines of this type occurs with marked exothermal effects, accompanied by a practically complete evolution of nitrogen as N2 from the polymer. [Pg.27]

NMP is most commonly used for S polymerization. For S polymerizations carried out at temperatures greater than 100 °C, thermal initiation provides some rate enhancement and a mechanism for controlling the excess of nitroxide that is formed as a consequence of radical-radical termination and the persistent radical... [Pg.480]

RAFT end groups are known to be unstable at very high temperatures (>200 °C). Thermal elimination has been used as a means of trithiocarbonate end group removal. For ps430,4W direct elimination is observed (Scheme 9.54). For poly(butyl acrylate)464 the major product suggests a hoinolysis/backbiting/ i-scission reaction is involved (Scheme 9.55). [Pg.538]


See other pages where C thermal is mentioned: [Pg.203]    [Pg.359]    [Pg.375]    [Pg.410]    [Pg.320]    [Pg.481]    [Pg.499]    [Pg.536]    [Pg.26]    [Pg.343]    [Pg.350]    [Pg.381]    [Pg.429]    [Pg.529]    [Pg.371]    [Pg.509]    [Pg.402]    [Pg.549]    [Pg.5]    [Pg.3]    [Pg.77]    [Pg.86]    [Pg.98]    [Pg.102]    [Pg.511]    [Pg.546]    [Pg.546]    [Pg.23]   


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