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1B shows how one after another, IPL reduces the chances of risk and the system is brought back to ALARP region. A typical actual process example has been presented in Clause 1.1.2 of Chapter Vll.

1C and D Authorizes each packet for each protocol differently. Follows specific rules and may allow some commands to a server hut not others, OR limits access to certain types based on authenticated user. Setup is quite complex every client program needs to be set up. Also each protocol must have a proxy in it. True proxy is much safer.

1H-1H DQF-COSY spectrum of the sugar region of 15 showing

1H-1H TOCSY spectrum of the sugar region of 19 showing all the 1H

2 Composition dependence of Tc in Pb solid solution alloys

2 Dependence of reaction rate on the presumed dependence of the rate law on the concentration of benzoic acid and hydrogen pressure.

2 Dependence of W F on the diameter of the catalyst particles for dehydration of n-butanol at 1 titm and 600 F. Reprinted with permission from the contribution of D. N. Miller and R. S. Kirk to

2 Effect of pressure on the reaction rate. Temperature, 25 to 26 C hydrogen flow rate, 27.6 x 10 mol s catalyst weight, 0.976 g stirrer speed, 1500 rpm.

2 Initial rate versus pressure of dimethylamine.

2 is a plot of the reaction rate per unit mass of catalyst versus the product The data correspond to reaction at 130 C at a catalyst loading of 0.5 g. The data in the figure represent two types of experiments

2 Large LOCA as a Function Event Tri

20 BaTiOs. Ps versus T below 20 C, where f siooi is the component of the spontaneous polarization parallel to the c axis in the tetragonal phase

21 BaTiOs. k versus v. Parameter

26 PbTiOs. Pg versus T

26 PbTiOs. versus T

29 Lattice parameters of ABa2Cu306 at T 10 K, ionic radii according to Shannon

2A Schematic illustration of the formation of the nanocrystalline structure in Fe—Cu—Nb—Si—B alloys, based on atom probe analysis results and transmission electron microscopy observations by Mono et al. 3.23,

3 Chamley acetabular cup design showing grooves on exterior for bone cement, and the stainless-steel wire for wear assessment by X-ray.

3 Effect of catalyst weight on the rate of reaction. Temperature, 25 C pressure, 748 torr hydrogen flow rate, 31.3 x 10 mol s stirrer speed, 1000 rpm.

3 The anti-toxin malaria CPI vaccine candidate 9.

3-D image of CANDU-reactor fuel channel with bundle. Based on data from AECL.

36 SrTeOs. k versus T. f lOkHz

3D liquid water distributions in a hydrophobic and a mixed wettability GDL from the two-phase LBM simulations .

3D-UV-visible Differential Reflectance Spectra recorded in 0,5 M H2SO4 of a PAni film

4 Effect of hydrogen flow rate on the reaction rate. Temperature, 25 to 2TC pressure, 534 torr, catalyst weight, 0.974 g stirrer speed, 1500 rpm.



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