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Untitled - Sciencemadness Dot Org

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THERMAL PROPERTIES<br />

Fig. 2.02. Pyrolysis apparatus.<br />

A. Carrier gas supply<br />

B. Pressure regulator<br />

C. Flow control needle valve<br />

D. Reference thermal conductivity cell<br />

E. Pyrolysis chamber<br />

F. Combustion tube<br />

G. Active cell<br />

H. Manometer<br />

I. Pressure control needle valve<br />

J. Rotameter<br />

I H<br />

Fig. 2.03. Pyrolysis block.<br />

A. Pyrolysis chamber<br />

B. Nickel plug<br />

C. Carrier gas inlet<br />

D. Carrier gas outlet<br />

E. Cartridge heater wells (2)<br />

F. Helical threads cut in inner body<br />

of block<br />

G. Outer shell of block<br />

H. Cooling jacket inlet<br />

I. Cooling jacket outlet<br />

test material is weighed into a small combustion boat and placed in the pyrolysis<br />

chamber, initially at room temperature. A lo- to lSml/min flow of helium is then<br />

started, and when the air has been swept out, the pyrolysis chamber temperature is<br />

raised at a constant rate, usually lO”C/min. The helium stream carries gases<br />

evolved from the sample through the combustion tube and into the thermal conduc-<br />

tivity cell, G. The two cells, D and G, form two arms of a Wheatstone bridge whose<br />

output varies with the concentration of impurities (decomposition products, etc.) in<br />

the effluent helium stream. The bridge output is fed to one axis of an X-Y recorder,<br />

and the pyrolysis chamber temperature is fed to the other. In this manner, the rate<br />

of gas evolution from the sample as a function of chamber temperature is deter-<br />

mined.<br />

The combustion chamber converts the more complex products, such as undecom-<br />

posed but vaporized explosive, to simple molecules. This increases the bridge sen-<br />

sitivity and also keeps these products from condensing in the cooler parts of the ap-<br />

paratus.<br />

Data Presentation. All the DTA curves were determined at a heating rate of<br />

ll”C/min with granular NaCl as the reference sample. All the pyrolysis curves were<br />

determined at a heating rate of lO”C/min. Gas-solid interactions were minimimized<br />

because gaseous products were swept away from the sample in the pyrolysis ap-<br />

paratus as rapidly as they were formed,<br />

Any possible contribution to the reaction from atmospheric oxygen also was<br />

eliminated, because the carrier gas was helium.<br />

224

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