Abstract
Total reduced sulfurs (TRS) include hydrogen sulfide (H2S), methyl mercaptan (methanethiol, CH3SH), di- methyl sulfide (CH3SCH3) and dimethyl disulfide (CH3S2CH3) and are referred to as noncondensible gases. They are part of a well-known environmental problem afflicting pulp mills exploiting the Kraft pulp mill process. These sulfur com- pounds are formed in the Kraft pulping process and come in contact with different waters and liquors, contributing to the odor problems of Kraft mills. Because of their toxic and corrosive characters, they must be removed down to very low concentration levels. The olfactory threshold of TRS for human beings is four orders of magnitudes below the regulated emission level which is approximately 5-10 ppm in Canada and the US, giving rise to strict regulations in order to reduce their emissions from specific sulfate pulp process equipments. Among several approaches proposed to remove or at least reduce these airborne pollutants, the utilization of ferric chelate complex of trans-1,2-cyclohexane diaminetetraacetic acid (CDTA) for the oxidative scrubbing of hydrogen sulfide and methyl mercaptan in Kraft mill streams is beneficial from the standpoints of iron protection against precipitation and oxygen-mediated regenerative oxidation of the ferrous chelate CDTA. The remaining (unreactive) two sulfur-bearing compounds, dimethyl sulfide and dimethyl disulfide undergo only physical absorption in such solutions. The physical solubility of these four compounds in aqueous CDTA-Fe(III) alkaline solutions is therefore a crucial parameter for designing the complete scrubbing-absorption process. The aim of this review is to highlight several aspects related to the solubility of TRS compounds in Fe-chelate aqueous solutions (experimental methods, solubility dependence on temperature, chelate concentration, and solution pH).
Talk to us
Join us for a 30 min session where you can share your feedback and ask us any queries you have