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All of the details about when one value or another is used are far beyond the scope of this book. But 0x4C-80 is used when the Layer 2 protocol is IEEE 802.2 Logical Link Control (LLC) frames, which can be the contents of the LAN MAC frames. A value of 0x50-indicates the absence of the Layer 2 protocol altogether. When Layer 2 is 0x4C-80 (LLC used), then the value of the first 8 bits (first octet) of the Layer 3 field is 0x70. The 0x70 value means that the protocol is user specified, the user being IBM in all these cases. SNA was discussed in the previous chapter. APPN is Advanced Peer-to-Peer Networking, a sort of router-based version of hierarchical SNA. NetBIOS is IBM s (and Microsoft s) implementation of the middle layers of the OSI RM (most of layers 5--3). Finally, HPR is High Performance Routing, a kind of extension to APPN designed for fast packet networks such as ATM. Purists might cringe at these brief descriptions, but this is enough to know about IBM protocols for frame relay encapsulation purposes. The details on how SNA traffic is carried inside frame relay frames are quite complex and require a much deeper understanding of SNA than has been presented in this chapter and the previous one. Those interested in the deeper levels of SNA, APPN, and other IBM protocols with regard to frame relay are referred to the sources listed in the bibliography. Before moving on to the related topic on Ether-type encapsulation, a comparison of the NLPID, SNAP, and Q.933 encapsulation header formats is shown in Figure 11.9.

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21-2.2.1 High Viscosity Mixers. While turbine mixers can handle low to moderate viscosities, high viscosity uids [100 000 cP (100 Pa s) and greater] usually require some type of close-clearance impeller design. The diameter of a typical turbine-style impeller is less than 70% of the tank diameter. Closeclearance impellers for high viscosity applications are 85 to 95% of the tank diameter. Some close-clearance impellers even have exible scrapers, which are effectively 100% of the tank diameter. Important mechanical features of high viscosity mixers are the low speed and high torque required to rotate large impellers in viscous uids. Equally important, but more subtle, are requirements for the tank to have a very round cross-section. The tank must be round so that the clearance between the impeller and the wall remain nearly constant, and the shaft must be centered for the same reason. Shaft and impeller designs are primarily for strength and based on the hydraulic forces caused by viscous drag. Although high viscosity impellers can take many forms, two of the more common varieties are the helical-ribbon (Figure 21-7) and anchor-style (Figure 21-8) impellers. 21-2.2.2 High-Shear Mixers. High-shear mixers have many features opposite to those of high viscosity mixers. Typical high-shear mixers have small impellers, 10 to 20% of the tank diameter, and operate at high speeds, 1000 rpm (16.7 rps) to 3600 rpm (60 rps). To operate at high speeds, without requiring excessive power, high-shear impellers usually have small blades. The blades

You can also specifically design a star by clicking with the Star tool to display the Star dialog box, as shown in Figure 5.13, where you can type the number of points and both the first and second radius of the points.

For links to more information on analog formats, including manufacturers and suppliers, see the Formats section of Appendix D.

Plot Area, and they were positioned over the bordered range. The title is actually text entered into in a cell.

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