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Condensers, waste reduction

As with the electrical load profile, it is also necessary to analyze the heat load over the daily and annual cycles. Ideally, the heat load will match the available heat from the electrical generator (however, this is rarely the case). There will be periods when supplementary output will be necessary which can be achieved by, say, supplementary firing the waste heat gases of a gas turbine, or heat output reduction is necessary by the introduction of bypass stacks. For a steam turbine installation bypass pressure-reducing valves will be necessary to supplement steam output, while a dump condenser may be needed at low-process steam demands. The nature of the electrical and heat load will obviously have significant influence in the development of the scheme and scope of equipment. [Pg.188]

Because systems are normally not designed for use with this type of fluid, certain aspects should be reviewed with the equipment and fluid suppliers before a decision to use such fluids can be taken. These are compatibility with filters, seals, gaskets, hoses, paints and any non-ferrous metals used in the equipment. Condensation corrosion effect on ferrous metals, fluid-mixing equipment needed, control of microbial infection together with overall maintaining and control of fluid dilution and the disposal of waste fluid must also be considered. Provided such attention is paid to these designs and operating features, the cost reductions have proved very beneficial to the overall plant cost effectiveness. [Pg.864]

The electric furnace process (Fig. 11) for the conversion of phosphate rock into phosphorus was described by Horton et al. [15] in a paper that also presented the results of a pilot plant study of treating the wastes produced. The process, as well as the handling of the various waste streams for pollution control, are discussed in Section 9.5.2. In processing the phosphate, the major source of wastewater is the condenser water bleedoff from the reduction furnace, the flow of which varies from 10 to 100 gpm (2.3-22.7 m /hour) and its quality characteristics are presented in Table 7. [Pg.438]

Barometric condenser systems can be a major source of contamination in plant effluents and can cause a particularly difficult problem by producing a high-volume, dilute waste stream [8]. Water reduction can be achieved by replacing barometric condensers with surface condensers. Vacuum pumps can replace steam jet eductors. Reboilers can be used instead of live steam reactor and floor washwater, surface runoff, scrubber effluents, and vacuum seal water can be reused. [Pg.524]

Fig. 2.3 Flow diagram ofTi02 production by the k) Evaporator I) TiCU superheater m) O2 su-chloride process, a) Mill b) Silo c) Fluidized- perheater n) Burner o) Cooling coil p) Filter bed reactor d) Cooling tower e) Separation of q) Ti02 purification r) Silo s) Gas purification metal chlorides f) TiCU condensation g) Tank t) Waste-gas cleaning u) CI2 liquefaction, h) Cooler i) Vanadium reduction j) Distillation ... Fig. 2.3 Flow diagram ofTi02 production by the k) Evaporator I) TiCU superheater m) O2 su-chloride process, a) Mill b) Silo c) Fluidized- perheater n) Burner o) Cooling coil p) Filter bed reactor d) Cooling tower e) Separation of q) Ti02 purification r) Silo s) Gas purification metal chlorides f) TiCU condensation g) Tank t) Waste-gas cleaning u) CI2 liquefaction, h) Cooler i) Vanadium reduction j) Distillation ...
High-temperature thermal treatment of hazardous waste offers a reduction in volume as well as a conversion of toxic organic constituents to harmless or less harmful forms [1]. However, hazardous metals can neither be generated nor destroyed in the waste thermal process, but they can be transformed both chemically and physically [2]. There is therefore a potential for hazardous metals to emit if they vaporize at high temperatures [3]. Many matals and their salts will form vapors at temperatures reached by flame and post-flame zones of a combustion chamber. When the vapors cool, they condense to form submicron particles, which tend to be relatively difficult to capture in air polution control equipments. These emissions of submicron metallic particles have been identified as one of the greatest health risks associated with waste incineration [4]. [Pg.559]

Although steam is the carrier vapour most used, on account of its low molecular weight, its high heat of evaporation and the ease with which it is condensed, other gases also find application in industry for effective pressure reduction. In the production of hard coal tar pitch, for instance, waste gases containing COj, N2 and water... [Pg.309]


See other pages where Condensers, waste reduction is mentioned: [Pg.410]    [Pg.293]    [Pg.298]    [Pg.79]    [Pg.483]    [Pg.237]    [Pg.1593]    [Pg.237]    [Pg.40]    [Pg.75]    [Pg.366]    [Pg.65]    [Pg.573]    [Pg.1012]    [Pg.56]    [Pg.172]    [Pg.66]    [Pg.146]    [Pg.468]    [Pg.154]    [Pg.1415]    [Pg.617]    [Pg.713]    [Pg.483]    [Pg.3223]    [Pg.362]    [Pg.1698]    [Pg.1908]    [Pg.360]    [Pg.528]    [Pg.2599]    [Pg.93]    [Pg.135]    [Pg.12]    [Pg.414]    [Pg.483]    [Pg.414]    [Pg.711]    [Pg.200]    [Pg.1692]    [Pg.1898]    [Pg.1597]    [Pg.67]   
See also in sourсe #XX -- [ Pg.286 , Pg.287 , Pg.288 ]




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WASTE REDUCTION

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