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A text file that you can use to provide automated input for unattended installation of Windows XP and Windows 2000. This input includes parameters to answer the questions included in Setup for specific installations. In some cases, you can use this text file to provide input to wizards, such as the Active Directory Installation Wizard, which is used to add Active Directory to Windows 2000 Server through Setup. The default answer file for Setup is known as Unattend.txt. See also Active Directory.
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of bitumen with a lease operating life of 22 years. Expended production of the in situ projects at Foster Creek, MacKay River, and Christina Lake will provide a further 200,000 bbl/day of bitumen at the time of completion. The Scotford Upgrader is located next to Shell Canada s Scotford Refinery near Fort Saskatchewan, Alberta where bitumen from the Muskeg River Mine is upgraded into synthetic crude oil. A significant portion of the output is sold to the Scotford Refinery for further processing. In addition to the coking options, the LC-Fining ebullated-bed hydroconversion process is used at both the Syncrude Mildred Lake upgrader and the Shell Scotford Upgrader. The H-Oil ebullated-bed hydroconversion process is used at the Husky Lloydminster Upgrader. 4.6.2 Secondary Upgrading Catalytic hydrotreating is used for secondary upgrading to remove impurities and enhance the quality of the final synthetic crude oil product. In a typical catalytic hydrotreating unit, the feedstock is mixed with hydrogen, preheated in a fired heater, and then charged under high pressure to a fixed-bed catalytic reactor. Hydrotreating converts sulfur and nitrogen compounds present in the feedstock to hydrogen sulfide and ammonia. Sour gases from the hydrotreater(s) are treated for use as plant fuel. Hydrocracking may also be employed at this stage to improve product yield and quality. Thus the primary liquid product (synthetic crude oil) is hydrotreated (secondary upgrading) to remove sulfur and nitrogen (as hydrogen sulfide and ammonia, respectively) and to hydrogenate the unsaturated sites exposed by the conversion process. It may be necessary to employ separate hydrotreaters for light distillates and mediumto-heavy fractions; for example, the heavier fractions require higher hydrogen partial pressures and higher operating temperatures to achieve the desired degree of sulfur and nitrogen removal. Commercial applications have therefore been based on the separate treatment of two or three distillate fractions at the appropriate severity to achieve the required product quality and process efficiency. Hydrotreating is generally carried out in down-flow reactors containing a fixed bed of cobalt-molybdate catalysts. The reactor effluents are stripped of the produced hydrogen sulfide and ammonia. Any light ends are sent to the fuel gas system and the liquid products are recombined to form synthetic crude oil. Finishing and stabilisation (hydrodesulfurization and saturation) of the liquid products is achieved by hydrotreating the liquid streams, as two or three separate streams (Speight, 1999 and references cited therein). This is necessary because of the variation in conditions and catalysts necessary for treatment of a naphtha fraction relative to the conditions necessary for treatment of gas oil. It is more efficient to treat the liquid product streams separately and then to blend the finished liquids to a synthetic crude oil. In order to take advantage of optimum operating conditions for various distillate fractions, the Suncor coker distillate is treated as three separate fractions: naphtha, kerosene, and gas oil. In the operation used by Syncrude, the bitumen products are separated into two distinct fractions: naphtha and mixed gas oils. Each plant combines the hydrotreated fractions to form synthetic crude oil that is then shipped by pipeline to a refinery. 4.6.3 Other Processes Other processes which have also received some attention for bitumen upgrading include partial upgrading (a form of thermal deasphalting), flexicoking, the Eureka process, and various hydrocracking processes.
Part V:
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