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... total number of eleven pH controlled batch experiments were conducted for bioleaching of a pyrite concentrate using a mixed microbial culture (Figure 9). Ten different oxidic by-products and slaked lime as reference material were used to control the pH in the bioreactor during the experiment. ...
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... the maintenance coefficient was much higher when no chloride was added ( Figure 9 and Table IV Modeling studies suggested a probability of inhibition of specific Fe 2+ utilization rate due to chloride at lower growth rates, whereas a higher dilution rates specific ferrous utilization is stimulated ( Figure 8, Paper VII). Similarly the effect of chloride would also be more pronounced at lower substrate level as the growth rate will decrease with the increment of the chloride concentration at a given residual substrate concentration ( Figure 3, Paper VII). ...
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... phenomenon of growth uncoupled Fe 2þ oxidation has been previously reported in At. ferrooxidans batch growth ( Breed et al., 1999;Kelly and Jones, 1978). In Figure 9 the biomass yield was plotted versus the logarithm of the Fe 3þ /Fe 2þ ratio. The figure shows that for different total iron concentrations the biomass yields were at the same level until the dilution neared the critical rate. ...
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... per the Pirt theory, the biomass yield increased with increasing dilution rate (Figure 7), as growth uncoupled Fe 2+ oxidation cannot be ignored (Equations 3 and 7), and was in agreement with previous studies (Sundkvist et al., 2008, Becker andMärkl, 2000). The plots of specific Fe 2+ oxidation rate versus dilution rate (Equation 8; Figure 8) and specific Fe 2+ oxidation rate versus the log of the Fe 3+ to Fe 2+ ratio (Equations 8 and 9; Figure 9) showed that the specific Fe 2+ oxidation rate was relatively constant and insensitive to both dilution rate and the Fe 3+ to Fe 2+ ratio. When working under chemostat conditions, the true maintenance coefficient was the intercept in figure 8 and was valid in the entire range where the chemostat conditions were fulfilled. ...
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... the maintenance coefficient was much higher when no chloride was added ( Figure 8 and Table V). The contribution from maintenance activities to the calculated maximum specific Fe 2+ utilization rate in the experiments with 0 g L -1 , 2 g L -1 , and 3 g L -1 chloride was 93%, 24%, and 23%, respectively ( Figure 9). The calculated maintenance coefficient based on the Pirt theory (Table V) showed that the introduction of 2-3 g L -1 chloride into the growth medium in the feed to the bioreactor decreased the maintenance coefficient by 70% when compared to the experiment without chloride. ...

Citations

... Under the indirect mechanism, bacteria oxidize the ferrous ion to the ferric ion state, regenerating the ferric ion, which is necessary for the chemical oxidation of the sulfide mineral [9]. Figure 3 shows the contact, contactless and cooperative mechanisms of the bio-leaching process. a b c Figure 3 -Patterns of direct and indirect interaction of the bacteria with pyrite: acontact leaching; bnon-contact leaching; ccooperative leaching [12] Sulfuric acid is the main inorganic acid that is found in leaching conditions. Many organic acids are formed by bacterial (and fungal) metabolism that leads to organic acidosis, the complexes and chelates formation [13]. ...
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This paper deals with theoretical research of the biochemical features of low rank coals (LRC) treatment. The biochemical bases of the organic component degradation of LRC and the biochemical principles of bioleaching of sulfur compounds and metals from LRC are presented. The analysis of microorganisms' groups was carried out and the optimal conditions of their cultivation were determined. Electronic databases such as KEGG, BacDive, and EAWAG-BBD were used to identify the necessary ecological and trophic groups of microorganisms and to realize the patterns of trophic interactions in associations of different groups of microorganisms both under anaerobic and aerobic conditions. The methodological approach was applied and principle diagram of biochemical research of LRC processing was formed in order to develop the environmentally friendly direction of biogas and humic products production.