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Data lines sometimes require additional work to be done on installation and can be harder to troubleshoot, so the cost of provisioning a data line has been traditionally higher than a voice line of the same length Therefore, a voice line works for modem data most of the time, but when it fails or degrades, there is a different process of troubleshooting and repair One of the reasons for this voice and data separation was regulatory, both within and without the United States Most voice service providers could process voice calls (eg, switch them, provide caller identification, etc), but could not do anything with data bits (or voice bits either, for that matter) except pass them unchanged and unprocessed through the PSTN.



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create table ch11 (entityid int auto_increment not null primary key, lat float, lng float, type varchar(80), title varchar(80), tel varchar(80), adda varchar(80), addb varchar(80))





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This was called raw bit transport or basic transport services and all the service provider could supply in this regulated environment was a leased private line provisioned for the user s data bits This was certainly true until the service providers received permission to offer their own public data network services But this is a topic for the next chapter In addition to regulatory issues, there were technical reasons as well The PSTN was designed for constant bit rate voice calls, not bursty data packets Putting bursty data packets on all-thebandwidth circuits was extremely wasteful of network resources, but it worked Perhaps it would be better to try to put voice calls on the data networks as a stream of packets In fact, it was just this quest for packetized voice that culminated in frame relay But this is also a topic for the next chapter.

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Cr203 coverage and selectivity were also found for other catalyst combinations 62-364 High activities and selectivities are due to well-dispersed Cr6+-Ox species,363 however, Cr3+ dominates after reaction 364 Metal phosphates such as Ni 2P 20 7 (82% selectivity at 550 C),365 as well as CeP04 and LaP04 (higher than 80% selectivity),366 were found to be active in the dehydrogenation of isobutane to isobutylene Strong acidic sites were suggested to playa key role in the process Magnesium-cobalt phosphate with a composition of C0 2Mg(P04h is highly selective (77% at 500 C) in the oxidative dehydrogenation of propane when calcined at 550 c.

For now, it is enough to point out that trying to put voice traffic on data networks is the classic example of mixed traffic types It made less and less sense to have two circuits going everywhere, one for voice and one for data Even data was no longer just pure text There were graphical data with engineering drawings, image data with photographs, moving picture data with action content, audio data with the soundtrack, and so forth It became harder and harder to give the correct quality of service to each of these traffic types on the same network Some of the differences in the quality of service needed by these different traffic types are listed in Table 11 They are all so different in their needs that separate networks have been built just to carry each type of traffic, as shown in parentheses Table 1.

1 Different Networks, Different Quality of Service Trafffic Type Error Sensitivity Low Low Medium High Delay Sensitivity High High High Low Bandwidth Need Low High Very High Low/Medium Burstiness.

367 High activities in the dehydrogenation of propane to propylene were reported for supporting submonolayer or monolayer VOP04 on Ti02 or Ah03 which ensures the formation of highly dispersed VOP04 giving the best catalytic performance 68,369 Very high olefin yields were reported in the oxidative dehydrogenation of ethane,37o propane and butanes,37! and isobutane,372,373 as well as C5 and C6 alkanes 374 over Pt-coated cx-A1203 foam monoliths operating adiabatically at very short contact time (a few milliseconds) In the case of ethane and propane selectivities exceeding 60% were obtained at almost complete conversion According to the latest report, ethylene can be produced with about 85% selectivity at about 70% conversion using a Pt-Sn bimetallic catalyst and by adding large amounts of hydrogen to the reaction mixture at 950 c.

Figure 20-1 Simpli ed overview of a typical kraft process showing chemical pulping, oxygen deligni cation, pulp bleaching, and chemical recovery systems. Important mixing operations are indicated by the NAMF mixing icon.

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