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may be damaged. This could be due to an Ethernet equipment problem or the bridge becoming overloaded. Normally, this counter should display 0 or remain static. Another set of counters collects information on frames being sent out of the bridge s the wireless port:
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Bytes 0x00 0x0A are the jump instruction and the OEM ID (shown in bold print). Bytes 0x0B 0x53 are the BPB and the extended BPB. The remaining code is the bootstrap code and the end of sector marker (shown in bold print).
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When we discussed the sampling distribution of x in 8, we assumed that we knew the population standard deviation. This is a big and questionable assumption because if we know the population standard deviation, we would probably also know the population mean and, if so, why are we calculating sample estimates of What saves us, of course, is the central limit theorem, which tells us that the sampling distribution of x is approximately normal when the sample size, n, is large enough (roughly, n 30). If the original population is approximately normal, or the sample size is large, there are techniques similar to z-procedures for analyzing sampling distributions of sample means. In fact, some texts simply use z-procedures in this situation even though the population standard deviation is unknown. However, the resulting distribution is not normal and it s best to employ other procedures. In order to do this, we use the sample standard deviation s as an estimate of the population standard deviation . That is, sx = s n x =
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If the study wasn t double-blind, it would be because the psychologists were aware of which subjects had which therapy. In this case, the attitudes of the psychologists toward the different therapies might influence their evaluations probably because they might read more improvement into a therapy of which they approve. 17. Group A favors a dress code, group B does not. Both groups are hoping to bias the response in favor of their position by the way they have worded the question. 18. You probably want to block by community since it is felt that economic status influences attitudes toward advertising. That is, you will have three blocks: Upper Middle, Middle, and Lower Middle. Within each, you have four billboards. Randomly select two of the billboards within each block to receive the Type I ads, and put the Type II ads on the other two. After a few weeks, compare the differences in reaction to each type of advertising within each block. 19. With only 3000 of 100,000 surveys returned, voluntary response bias is most likely operating. That is, the 3000 women represented those who felt strongly enough (negatively) about men and were the most likely to respond. We have no way of knowing if the 3% who returned the survey were representative of the 100,000 who received it, but they most likely were not. 20. Assign each of the 26 women a two-digit number, say 01, 02, . . ., 26. Then enter the table at a random location and note two-digit numbers. Ignore numbers outside of the 01 26 range. The first number chosen assigns the corresponding woman to the first group, the second to the second group, etc. until all 26 have been assigned. This method roughly equalizes the numbers in the group (not quite because 4 doesn t go evenly into 26), but does not assign them independently. If you wanted to assign the women independently, you would consider only the digits 1, 2, 3, or 4, which correspond to the four groups. As one of the women steps forward, one of the random digits is identified, and that woman goes into the group that corresponds to the chosen number. Proceed in this fashion until all 26 women are assigned a group. This procedure yields independent assignments to groups, but the groups most likely will be somewhat unequal in size. In fact, with only 26 women, group sizes might be quite unequal (a TI-83/84 simulation of this produced 4 1s, 11 2s, 4 3s, and 7 4s).
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Don t get me wrong. These can be great questions. And if you could get an honest answer out of them, I might say toss one or two out there and see what happens. But if you ask questions such as these before you get an offer, it has the effect of raising the ante too high. No one wants to work that hard. The interviewer will simply fold and hope the next candidate is less challenging.
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6.7 Procedures
Before you can have offline access to the files on a shared network folder, you must specify how the files in the folder are stored in a cache on the client computer in this case, the user s portable computer. For nonexecutable files, such as word processing documents, spreadsheets, and bitmaps, there are two options for storing files: automatic caching, and manual caching.
The greatest potential for ethanol production from biomass, however, lies in enzymatic hydrolysis of cellulose. The enzyme cellulase, now used in the textile industry to stone wash denim and in detergents, simply replaces the sulfuric acid in the hydrolysis step. The cellulase can be used at lower temperatures, 30 to 50 C, which reduces the degradation of the sugar. In addition, process improvements now allow simultaneous saccharification and fermentation (SSF). In the SSF process, cellulase and fermenting yeast are combined, so that as sugars are produced, the fermentative organisms convert them to ethanol in the same step. Once the hydrolysis of the cellulose is achieved, the resulting sugars must be fermented to produce ethanol. In addition to glucose, hydrolysis produces other six-carbon sugars from cellulose and five-carbon sugars from hemicellulose that are not readily fermented to ethanol by naturally occurring organisms. They can be converted to ethanol by genetically engineered yeasts that are currently available, but the ethanol yields are not sufficient to make the process economically attractive. It also remains to be seen whether the yeasts can be made hardy enough for production of ethanol on a commercial scale. A large variety of feedstocks is currently available for producing ethanol from cellulosic biomass. The materials being considered can be categorized as agricultural waste, forest residue, and energy crops. Agricultural waste available for ethanol conversion includes crop residues such as wheat straw, corn stover (leaves, stalks, and cobs), rice straw, and bagasse (sugar cane waste). Forestry waste includes underutilized wood and logging residues; rough, rotten, and salvable dead wood; and excess saplings and small trees. Energy crops, developed and grown specifically for fuel, include fast-growing trees, shrubs, and grasses such as hybrid poplars, willows, and switchgrass. Although the choice of feedstock for ethanol conversion is largely a cost issue, feedstock selection has also focused on environmental issues. Materials normally targeted for disposal include forest thinnings collected as part of an effort to improve forest health, and certain agricultural residues, such as rice straw. Although forest residues are not large in volume, they represent an opportunity to decrease the fire hazard associated with the dead wood present in many forests. Small quantities of forest thinnings can be collected at relatively low cost, but collection costs rise rapidly as quantities increase. Agricultural residues, in particular corn stover, represent a tremendous resource base for biomass ethanol production. Agricultural residues, in the long-term, would be the sources of biomass that could support substantial growth of the ethanol industry. At conversion yields of around 60 to 100 gal/dry ton, the available corn stover inventory would be sufficient to support 7 to 12 billion gallons of ethanol production per year. The cost of agricultural residues is not nearly as sensitive to supply as is the cost of forest residues, although the availability of corn stover could be affected by a poor crop year. The relatively low rise in cost as a function of feedstock use is due to the relatively high density of material available that does not involve competition for farmland. In addition, the feedstock is located in the corn-processing belt, an area that has an established infrastructure for collecting and transporting agricultural materials. It is also located near existing grain ethanol plants, which could be expanded to produce ethanol from stover. Initially, locally available labor and residue collection equipment might have to be supplemented with labor and equipment brought in from other locations for residue harvesting and storage operations, if the plants involved are of sufficient scale. Eventually, however, when the local collection infrastructure has been built up, costs would come down. Dedicated energy crops such as switchgrass, hybrid willow, and hybrid poplar are another long-term feedstock option. Switchgrass is grown on a 10-year crop rotation basis, and harvest can begin in the first year in some locations and the second year in others. Willows require a 22-year rotation, with the first harvest in the fourth year and subsequent harvests every 3 years thereafter. Hybrid poplar requires 6 years to reach harvest age in the Pacific Northwest, 8 years in the Southeast, Southern Plains, and South Central regions,
3 When the Add Printer Wizard appears, click Next. 4 On the Local Or Network Printer page, select the option labeled A Network
hydrogenation or hydrocracking processes may be operated on a strictly thermal basis or in the presence of a catalyst. Thermodynamically speaking, larger hydrocarbon molecules are broken into lighter species when subjected to heat. The hydrogen/carbon atomic ratio of such molecules is lower than that of saturated hydrocarbons, and abundantly supplied hydrogen improves this ratio by saturating reactions, thus producing liquid species. These two steps may occur simultaneously. However, the application of hydrocracking process has been hampered by the presence of certain contaminants in such hydrocarbons. The presence of sulfur- and nitrogen-containing compounds along with organometallic compounds in crude shale oils and various refined petroleum products has long been considered undesirable. Desulfurization and denitrification processes have been developed for this purpose. The thermal cracking process is directed toward the recovery of gaseous olefins as the primarily desired cracked product, in preference to gasoline range liquids. By this process, it is claimed that at least 15 to 20 percent of the feed shale oil is converted to ethylene, which is the most common gaseous product. Most of the feed shale oil is converted to other gaseous and liquid products. Other important gaseous products are propylene, l,3-butadiene, ethane, and butanes. Hydrogen is also recovered as a valuable non-hydrocarbon gaseous product. Liquid products can comprise 40 to 50 weight percent or more of the total product. Recovered liquid products include benzene, toluene, xylene, gasoline-boiling-range liquids, and light and heavy oils. Coke is a solid product of the process and is produced by polymerization of unsaturated materials. Coke is typically formed in an oxygen-deficient environment via dehydrogenation and aromatization. Most of the formed coke is removed from the process as a deposit on the entrained inert heat carrier solids. The thermal cracking reactor does not require a gaseous hydrogen feed. In the reactor, entrained solids flow concurrently through the thermal riser at an average riser temperature of 700 to 1400 C. The preferred high length-to-diameter (L-to-D) ratio is in the range of a high 4:1 to 40:1, or 5:1 to 20:1 preferably. The moving bed hydroprocessing reactor is used to produce crude oil from oil shale or tar sands containing large amounts of highly abrasive particulate matter, such as rock dust and ash. The hydroprocessing takes place in a dual-function moving bed reactor, which simultaneously removes particulate matter by the filter action of the catalyst bed. The effluent from the moving bed reactor is then separated and further hydroprocessed in fixed bed reactors with fresh hydrogen added to the heavier hydrocarbon fraction to promote desulfurization. A preferred way of treating the shale oil involves using a moving bed reactor followed by a fractionation step to divide the wide-boiling-range crude oil produced from the shale oil into two separate fractions. The lighter fraction is hydrotreated for the removal of residual metals, sulfur, and nitrogen, whereas the heavier fraction is cracked in a second fixed bed reactor normally operated under high-severity conditions. The fluidized bed hydroretort process eliminates the retorting stage of conventional shale upgrading, by directly subjecting crushed oil shale to a hydroretorting treatment in an upflow, fluidized bed reactor such as that used for the hydrocracking of heavy petroleum residues. This process is a single stage retorting and upgrading process. Therefore, the process involves: (a) crushing oil shale, (b) mixing the crushed oil shale with a hydrocarbon liquid to provide a pumpable slurry, (c) introducing the slurry along with a hydrogen-containing gas into an upflow, fluidized bed reactor at a superficial fluid velocity sufficient to move the mixture upwardly through the reactor, (d) hydroretorting the oil shale, (e) removing the reaction mixture from the reactor, and (f ) separating the reactor effluent into several components. The mineral carbonate decomposition is minimized, as the process operating temperature is lower than that used in retorting. Therefore, the gaseous product of this process has a greater heating value than that of other conventional methods. In addition, owing to the
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