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Water high-pressure boiler specifications

Table 3.7 Typical make-up water specifications for high-pressure boilers... Table 3.7 Typical make-up water specifications for high-pressure boilers...
TABLE 13.3 Typical Makeup Water Specification for High-Pressure Boilers... [Pg.376]

Normally, the reaction occurs at 350°C and 3000 kPa (the reaction is not really isothermal see item 3 below). Heat evolved by the reaction is removed by producing high-pressure steam (4237 kPa, 254°C) from boiler feed water in the reactor shell. Propylene is the limiting reactant, with benzene present in excess. The feed propylene is a raw cut, and contains 5 wt% propane impurity. Recendy, the propane supplier has been having difficulty meeting specifications, and the propane impurity exceeds 5 wt%. The reduced feed concentration of propylene is causing a decrease in cumene production. In order to maintain the desired cumene production rate, it has been suggested that the reaction temperature be raised to compensate. [Pg.621]

Motor-driven, multistage reciprocating compressors have reportedly been the most popular choice for aeroderivatives. Motor-driven, oil-fiooded screw compressors are also used in some cases. High horsepower, multistage centrifugal compressors, similar to those used at many pipeline compressor stations, may be required for the newer heavy-duty units if the distribution pipeline pressure is insufficient (see Pipelines). Gas turbines have more stringent fuel-gas specifications in terms of cleanliness than do gas-fired boilers. Thus oil- and water-knockout systems, coalescing filters, and fine-mesh filters are used. [Pg.17]

Table 93 Specification for grades of high-quality water suitable for higher pressure WT boilers. Table 93 Specification for grades of high-quality water suitable for higher pressure WT boilers.
These facts have led to the review and finally the development of an alternative approach and in particular the possibilities of recovering vanadium for metallurgical use. Figure 100 illustrates the principles of the soot ash removal unit. The carbon slurry from the SGP unit is flashed to atmospheric pressure in the slurry tank (a). The slurry is then filtered on an automatic filter (b) to recover a filter cake with about 80% residual moisture and a clear water filtrate. The filter cake is subjected to a controlled oxidation process in a multiple-hearth furnace (c). This type of furnace, which is well established in many industries and specifically in the vanadium industry, allows combustion of the carbon to occur under conditions where the vanadium oxides neither melt nor corrode. This is not an easy task if one considers the problems of burning a high-vanadium fuel oil in a conventional boiler. The product is a vanadium concentrate, which contains about 75% V2O5. Compared to the old naphtha extraction-based recycle system, the new once-through process consists of only two proces-... [Pg.140]


See other pages where Water high-pressure boiler specifications is mentioned: [Pg.247]    [Pg.243]    [Pg.375]    [Pg.314]    [Pg.838]    [Pg.118]    [Pg.27]    [Pg.867]    [Pg.388]    [Pg.233]    [Pg.56]    [Pg.105]    [Pg.85]    [Pg.889]    [Pg.295]   
See also in sourсe #XX -- [ Pg.376 ]




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