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To request computer and user certificates for client computers, first create a console on the client computer that displays the Certificates (Local Computer) and Certificates (Current User) snap-ins. To do so, complete the following steps: 1. On a client computer, click Start, choose Run, type mmc in the Open box and then click OK. This opens a blank Microsoft Management Console (MMC). 2. Choose Add/Remove Snap-In from the File menu. The Add/Remove Snap-In dialog box appears. 3. Click Add, and select Certificates in the Add Standalone Snap-In dialog box, and then click Add again. 4. In the Certificates Snap-In dialog box (Figure 15-11), select Computer Account, click Next, select Local Computer, and then click Finish.

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include hydrogen consumption that may be 20 to 100 percent higher than that for fixed bed resid desulfurization process, and loss of liquid and hydrogen to high gas yields. The distillate products require further hydrotreating and conversion to produce transportation fuels. Thus, the options for refiners processing heavy high sulfur will be a combination of upgrading schemes and by-product utilization. Other heavy oil upgrading options include: (a) deep cut vacuum distillation, (b) solvent deasphalting prior to conversion, and (c) hydrogenation prior to conversion. For the present, using a schematic refinery operation (Fig. 3.1), new processes for the conversion of residua and heavy oils will probably be used in concert with visbreaking with some degree of hydroprocessing as a primary conversion step. Other processes may replace or augment the deasphalting units in many refineries. Depending on the properties, an option for heavy oil, like tar sand bitumen, is to subject the feedstock to either delayed coking or fluid coking as the primary upgrading step with some prior distillation or topping (Speight, 2007). After primary upgrading, the product streams are hydrotreated and combined to form a synthetic crude oil that is shipped to a conventional refinery for further processing to liquid fuels. The product qualities resulting from the various heavy oil upgrading technologies are quite variable and are strongly dependent on feed type, process type, and processing conditions. However, producing fuels of acceptable properties is possible (in all cases) with existing petroleum processing technology, although the economics vary with a given refinery. However, there is not one single heavy-oil-upgrading solution that will fit all refineries. Heavy feedstock properties, existing refinery configuration, and desired product slate all can have a significant effect on the final configuration. Furthermore, a proper evaluation however is not a simple undertaking for an existing refinery. The evaluation starts with an accurate understanding of the nature of the feedstock; along with corresponding conversion chemistry need to be assessed. Once the options have been defined, development of the optimal configuration for refining the incoming feedstocks can be designed.

FAT volumes smaller than 16 MB are formatted as FAT12. FAT16 volumes larger than 2 GB are not accessible from computers running MS-DOS, Windows 95, Windows 98, Windows Me, and many other operating systems. This limitation occurs because these operating systems do not support cluster sizes larger than 32 KB, which results in the 2 GB limit. In theory, FAT32 volumes can be about 8 terabytes; however, the maximum FAT32 volume size that Windows XP Professional can format is 32 GB. Therefore, you must use NTFS to format volumes larger than 32 GB. However, Windows XP Professional can read and write to larger FAT32 volumes formatted by other operating systems.