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Reactivity ratios tubular

Additional complications peculiar to the analysis of copolymerization data obtained in continuous tubular processes are associated with the fact that such reaches never operate isothermally and often with a substantial axial pressure drop. In addition, there often exists a substantial reridence time distribution, accompanied by a radial concentration gradient, as already pointed out. Data obtained in such reactors are induded in Table 10, but it can be seen readily how the copol3mer compositions reported — and hence the reactivity ratios calculated — could depend not only on feed composition, pressure, entrance and exit temperature and average residence time, but also on residence time distribution, pipe diameter and flow rate. Again, such S3 tems are usually very inadequately defined, but data obtained in tubular reactors must not be rejected a priori for the reasons already cited. [Pg.441]

Low levels of D-limonene in the diet have not been reported to cause adverse effects in humans. D-Limonene can be a dermal sensitizer (see above for discussion about D-limonene oxidation products) however, an 8% solution of D-limonene in petrolatum did not cause an allergic skin response in any of 25 volunteers tested. D-limonene is also a recommended quencher in that it can decrease the sensitizing effect of cinnamic aldehyde when used at a 1 1 ratio with cinnamic aldehyde (International Fragrance Association, that is, IFRA, guidelines developed and used by the fragrance and consumer product industries). There is inadequate evidence in humans for the carcinogenicity of D-limonene, and the overall conclusion by experts is that, as discussed above, D-limonene produces renal tubular tumors in male rats by a non-DNA reactive a-2-globulin-asso-ciated response. Therefore, the mechanism by which D-limonene increased the incidence of renal tubular tumors in male rats is not relevant to humans. [Pg.1534]

For the catalytic tests, lOOmg of the bimetallic catalyst Pt-Rh/Al203 were placed in a tubular flow reactor and fed with a complex gas mixture containing CO, NO, C3Hg and O2 with N2 as the diluent. The flow composition oscillated between two values of Sn which represented the ratio between oxidising and reducing species in the reactive medium and can be defined as ... [Pg.148]

Figure 4-5 Sensitivity of reactant conversion to changes in flow rate ratio for nonisother-mal plug-flow tubular reactors with exothermic chemical reaction and cocurrent cooling in a concentric double-pipe configuration with radius ratio k = 0.5. The inlet tempoatures are 340 K for the reactive fluid and 335 K for the cooling fluid. Figure 4-5 Sensitivity of reactant conversion to changes in flow rate ratio for nonisother-mal plug-flow tubular reactors with exothermic chemical reaction and cocurrent cooling in a concentric double-pipe configuration with radius ratio k = 0.5. The inlet tempoatures are 340 K for the reactive fluid and 335 K for the cooling fluid.
Reactant A is converted irreversibly and exothermically to products in a 2-in.-inner-diameter tubular reactor via first-order chemical kinetics. The reactive mixture in the inner pipe is cooled using a concentric double-pipe heat exchanger. The nonreactive cooling fluid in the annular region flows countercurrently with respect to the reactive fluid. The radius ratio of the double-pipe configuration is If = Rinside/ outside = 0.5, the inlet temperature of the reactive fluid is 340 K,... [Pg.97]

The Los Alamos critical assembly known as Honeycomb in intended to supplement metal assemblies as a source of effective neutron cross sections in the 0.1-MeV region. It is a 48-ln. cube of Interleaved U(93.1S) foil and graphite plates in a tubular aluminum matrix (78 X 78 X 72 in.), for Which the C/ "tJ atomic ratio is 182. An arrangement for remotely Introducing central samples facilitates precision measurement of effective absorption cross sections (centoal reactivity coefficients). [Pg.337]


See other pages where Reactivity ratios tubular is mentioned: [Pg.302]    [Pg.153]    [Pg.496]    [Pg.81]    [Pg.84]    [Pg.89]    [Pg.289]    [Pg.277]    [Pg.141]    [Pg.211]   
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