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Recovery inorganic acid

Older hydrolysis processes applied concentrated inorganic acids such as H2SO4 and mild temperature (100-120 °C) to minimize the undesired consecutive reactions [49]. The recovery and reconcentration of the acid catalyst from the product mixture turned out to be difficult and expensive. Modern processes are therefore based on diluted acid and higher temperatures (180-220 °C) [49]. [Pg.38]

Figure 6.24 Flotation recovery of lime-depressed pyrite activated by inorganic acids vs. concentration of activators... Figure 6.24 Flotation recovery of lime-depressed pyrite activated by inorganic acids vs. concentration of activators...
As an example of the application of the aforementioned sequence, Table XYI lists the main engineering parameters necessary to design or optimize ED stacks equipped with AMV and CMV electromembranes (Table II) and committed to the recovery of the sodium salts of some weak monocarboxylic acids of microbial origin (i.e., acetic, propionic, and lactic acid) and of a strong inorganic acid (i.e., chloride acid), as estimated by Fidaleo and Moresi (2005a,b, 2006). [Pg.345]

On the other hand, the capability of sample preconcentration for instruments such as AAS, ICP-AES, ICP-MS, and so forth was studied [3]. After metal ions were enriched, they were eluted almost simultaneously by inorganic acid at low pH, because of their diffusion in the column is at a disadvantage for improvement of the detection limits. It has been demonstrated that metal ions such as Ca, Cd, Mg, Mn, Pb, and Zn were enriched with a good recovery at a concentration of 10 ppb each in 500 mL of the sample solution. However, the final enriched sample volume eluted from the CCC column was as large as several milliliters, due to longitudinal diffusion of the sample band in the retained stationary phase [1,3]. Additional band spreading occurred in the flow tube when the concentrated solution was eluted with an acid solution for subsequent analysis. [Pg.977]

Contaminated MEG from textile uses may contain antimony and from vehicle fleet operation it may be contaminated with inorganic acid inhibitors so that from both sources the residues arising from MEG recovery is liable to foul heat exchanger surfaces and may be very toxic. [Pg.384]

This chapter focuses on the advantages achieved with different procedures and makes comparative analyses of the synthetic results. Furthermore, despite utility at small scale, the use of Lewis acid/acyl chlorides reagents on an industrial scale is frequently discouraged due to the large amounts of waste produced. Practically, the use of homogeneous Lewis acids in combination with acyl chlorides or anhydrides poses a serious problem for the efficient recovery and disposal of metal oxides and protic inorganic acid by-products. [Pg.60]

Miscellaneous. Hydrochloric acid is used for the recovery of semiprecious metals from used catalysts, as a catalyst in synthesis, for catalyst regeneration (see Catalysts, regeneration), and for pH control (see Hydrogen-ION activity), regeneration of ion-exchange (qv) resins used in wastewater treatment, electric utiUties, and for neutralization of alkaline products or waste materials. In addition, hydrochloric acid is also utilized in many production processes for organic and inorganic chemicals. [Pg.451]

Problems of removal of mercury from aqueous effluents are more comphcated in plants that manufacture a variety of inorganic and organic mercury compounds it is generally best to separate the effluent streams of inorganic and organic mercurials. When phenyhnercuric acetate is precipitated from its solution in acetic acid by addition of water, the filtrate is collected and reused for the next precipitation. This type of recycling is necessary not only for economic reasons but also to minimise recovery operations. [Pg.117]

Solvent Extraction Reagents. Solvent extraction is a solution purification process that is used extensively in the metallurgical and chemical industries. Both inorganic (34,35) and organic (36) solutes are recovered. The large commercial uses of phosphine derivatives in this area involve the separation of cobalt [7440-48-4] from nickel [7440-02-0] and the recovery of acetic acid [61-19-7] and uranium [7440-61-1]. [Pg.320]

A method [62] has been described for the determination of down to 2.5pg kg-1 alkylmercury compounds and inorganic mercury in river sediments. This method uses steam distillation to separate methylmercury in the distillate and inorganic mercury in the residue. The methylmercury is then determined by flameless atomic absorption spectrophotometry and the inorganic mercury by the same technique after wet digestion with nitric acid and potassium permanganate [63]. The well known adsorptive properties of clays for alkylmercury compounds does not cause a problem in the above method. The presence of humic acid in the sediment did not depress the recovery of alkylmercury compounds by more than 20%. In the presence of metallic sulphides in the sediment sample the recovery of alkylmercury compounds decreased when more than lmg of sulphur was present in the distillate. The addition of 4M hydrochloric acid, instead of 2M hydrochloric acid before distillation completely, eliminated this effect giving a recovery of 90-100%. [Pg.409]


See other pages where Recovery inorganic acid is mentioned: [Pg.497]    [Pg.401]    [Pg.369]    [Pg.268]    [Pg.222]    [Pg.125]    [Pg.4919]    [Pg.617]    [Pg.248]    [Pg.116]    [Pg.271]    [Pg.1439]    [Pg.380]    [Pg.200]    [Pg.296]    [Pg.359]    [Pg.149]    [Pg.150]    [Pg.12]    [Pg.49]    [Pg.2382]    [Pg.349]    [Pg.550]    [Pg.16]    [Pg.908]    [Pg.244]    [Pg.221]    [Pg.138]    [Pg.367]    [Pg.500]    [Pg.371]    [Pg.49]    [Pg.9]    [Pg.480]    [Pg.320]    [Pg.322]    [Pg.334]   
See also in sourсe #XX -- [ Pg.144 ]




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