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Sulfur, absorption factor

The above calculation is quite tedious and gets complicated by the fact that the properties which ultimately control the magnitude of these fourteen unknown quantities further depend on the physical and chemical parameters of the system such as reaction rate constants, initial size distribution of the feed, bed temperature, elutriation constants, heat and mass transfer coefficients, particle growth factors for char and limestone particles, flow rates of solid and gaseous reactants. In a complete analysis of a fluidized bed combustor with sulfur absorption by limestone, the influence of all the above parameters must be evaluated to enable us to optimize the system. In the present report we have limited the scope of our calculations by considering only the initial size of the limestone particles and the reaction rate constant for the sulfation reaction. [Pg.141]

More recentiy, sulfuric acid mists have been satisfactorily controlled by passing gas streams through equipment containing beds or mats of small-diameter glass or Teflon fibers. Such units are called mist eliminators (see Airpollution control methods). Use of this type of equipment has been a significant factor in making the double absorption process economical and in reducing stack emissions of acid mist to tolerably low levels. [Pg.183]

To determine of Ce(IV) in acid soluble single crystals, a simple and sensitive method is proposed. The method is based on the reaction of tropeoline 00 oxidation by cerium(IV) in sulfuric acid solution with subsequent measurement of the light absorption decrease of the solution. The influence of the reagent concentration on the analysis precision is studied. The procedure for Ce(IV) determination in ammonium dihydrophosphate doped by cerium is elaborated. The minimal determined concentration of cerium equal to 0.04 p.g/ml is lower than that of analogous methods by a factor of several dozens. The relative standard deviation does not exceed 0.1. [Pg.198]

Licht et al. [17] developed a method of numerical analysis to describe the above-quoted equilibria of the 11 participating species (including alkali metal cations) in aqueous polysulfide solution, upon simple input to the algorithm of the temperature and initial concentration of sulfur, alkali metal hydroxide, and alkali metal hydrosulfide in solution. The equilibria constants were evaluated by compensation of the polysulfide absorption spectrum for the effects of H8 absorption and by computer analysis of the resultant spectra. Results from these calculations were used to demonstrate that the electrolyte is unstable, and that gradual degradation of polysulfide-based PECs (in the long term) can be attributed to this factor (Chap. 5). [Pg.16]

The absorption process in the bed is affected, as with all mass transfer processes, by the surface. If no other factors have any strong limiting effect on the process, an increase in mass transfer surface leads to a reduced sulfur dioxide concentration (Fig. 16.8). [Pg.483]

Leather dressing serves a number of important purposes. It can sometimes soften hard leather and help to prevent pieces breaking off, it consolidates powdering, and to some extent prevents absorption of sulfur dioxide. The last factor is an important one in the case of new leathers which have not started to rot. [Pg.24]


See other pages where Sulfur, absorption factor is mentioned: [Pg.142]    [Pg.284]    [Pg.124]    [Pg.286]    [Pg.708]    [Pg.117]    [Pg.233]    [Pg.65]    [Pg.197]    [Pg.117]    [Pg.153]    [Pg.286]    [Pg.31]    [Pg.921]    [Pg.286]    [Pg.63]    [Pg.87]    [Pg.41]    [Pg.124]    [Pg.187]    [Pg.75]    [Pg.359]    [Pg.129]    [Pg.149]    [Pg.106]    [Pg.570]    [Pg.486]    [Pg.15]    [Pg.409]    [Pg.772]    [Pg.271]    [Pg.19]    [Pg.287]    [Pg.124]    [Pg.156]    [Pg.281]    [Pg.898]    [Pg.93]    [Pg.207]    [Pg.3228]    [Pg.41]   
See also in sourсe #XX -- [ Pg.219 ]




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