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0 C6H3. Temperature dependence of p . Magnetism fitted according to Ising model using J hc -225cm, g 2.15 .

0 crystallization. melting point, T, glass transition point. The lower part of the figure shows the DSC curve .

0 for homopolymers and copolymers of metaphosphates and

0 nullclines of tliis system along witli trajectories corresponding to sub-and super-tlireshold excitations. The trajectory arising from tire sub-tlireshold perturbation quickly relaxes back to tire stable fixed point. Three stages can be identified in tire trajectory resulting from tire super-tlireshold perturbation

0 open circles

0 phase I. T melting point. The lower part of the figure shows the DSC curve .

0-junction with n ports

0C H3 CH N CHCCHjIjij. Temperature dependence of for supercooled liquid state. T, glass transition point, T melting point. The lower part of the figure shows the DSC curve .

0S- -Temperature dependence of Xm and 1 Zm curves calculated by

0SCH3 Cl3. Temperature dependence of Xm and i Xm- Pill curves fitted according to Bleaney-Bowers

1 contains plots of the data obtained in n-butanol dehydration trials conducted with each of these batches of catalyst at 600 F and 1 atm. Figure PI2.8-2 contains cross plots of the smoothed data in Figure P12.8-1 that indicate the dependence of the observed rate on the diameter of the catalyst beads at conversions of 7, 14, and 21 . The experimental conditions are such that the catalyst beads are at the same temperature throughout and that there are no significant temperature gradients within the fixed bed.

1 Dependence of reaction rate on the mass of catalyst present.

1 Gradient of dimensionless concentration dc at the stationary planar electrode surface in a calm solution, and 2 the dependence of the ratio c c on the dimensionless distance jc 5,

1 Graphical illustration of the trapezoidal rule.

1 has been developed based on

1 Initial rate versus mass velocity. Reprinted with permission fmm AIChE J., 12,292 .

1 is an important record-keeping document for HAZID analysis. This hazard register is same as the risk register discussed in Clause 3.2 of Chapter I, and details of the risk register are shown in

1 Points in the complex plane, Polar system.

1 REMPI and UV absorption spectra of 1,3-DMU . The 1 1 REMPI spectrum was obtained by scanning the pump laser and setting the probe laser at 220 nm with a delay time of 10 ns. Neither REMPI spectrum was normalized by the laser power, and at the short wavelength side of the figure, the low output power of the OPO laser resulted in the missing S3 feature in the 1 1 spectrum. The absorption spectrum was taken at 140 C, the same temperature as that of the pulsed valve during the REMPI experiments.

1 shows another way, where various system requirements and SIF requirements in conjunction with SRS inputs form SRS to get an SRS output. Now we shall look deeper into SRS and discuss how various inputs and requirements form SRS to establish details in the form of SRS output.

1 shows general risk categorization process, in which Fig. I 3.4.3-1A can be considered as general standard model, whereas Fig. I 3.4.3-1B and C show how scenario changes when categorization changes. Keeping this in mind, it is better to understand the same with the help some examples of various risk categories encountered in industrial process plants. These have been shown in Fig. I 3.4.3-2, to

1 shows the safety life cycle phases as per lEC 61508.

1 Typical concentration versus time plot for experimental trials. Temperature, 26 C pressure, 746 torr hydrogen flow rate, 30.7 X 10 moFs catalyst weight, 0.975 g stirrer speed, 1100 rpm slope, 13.7 X 10 moF.

1 —7 curves for pure Pb as a Type I and the Pb—Inl5 alloy as a Type II superconductor

10 M, in dmso solution.


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