Abstract:Bubble size is of fundamental importance in the flotation process, as it provides the surface area for particle collection. Typically, weak surfactants (frothers) are added to process water to reduce bubble coalescence. Certain inorganic electrolytes, which occur naturally in some flotation process water, have been shown to mimic the role of frothers. The concentration at which bubble coalescence is inhibited, the critical coalescence concentration, was determined in a 5.5-L mechanical flotation cell for a ser… Show more
“…In general the bubble size decreased as a result of the higher electrolyte content in the water. The results corroborated those of Sovechles and Waters (2015) who showed a critical coalescence ionic strength ranging from 0.22 to 0.28 (dimensionless in Sovechles and Waters). Craig et al (1993) clearly demonstrated that it is not a particular ion which prevents bubble coalescence but a combination of ions, which in its simplest form is made of a cation and an anion.…”
“…In general the bubble size decreased as a result of the higher electrolyte content in the water. The results corroborated those of Sovechles and Waters (2015) who showed a critical coalescence ionic strength ranging from 0.22 to 0.28 (dimensionless in Sovechles and Waters). Craig et al (1993) clearly demonstrated that it is not a particular ion which prevents bubble coalescence but a combination of ions, which in its simplest form is made of a cation and an anion.…”
“…Salt addition can decrease the bubble size for the possible reason that bubble coalescence is inhibited by charge repulsion 40 . In our earlier work, microbubbles were produced successfully in the salt solution and exhibited great mass transfer characteristics, 41 which is consistent with previous finding that the bubble size correlated well with ionic strength 42 . However, the ionic strength needed for the formation of microbubble system requires further determination.…”
Section: Introductionsupporting
confidence: 87%
“…However, the ionic strength needed for the formation of microbubble system requires further determination. Additionally, for the effect of ionic strength on multiphase flow characteristics, more attention has been paid to the bubble size and gas holdup rather than interfacial area 39,42 . With the development of process industry, techniques based on microbubble generation will be applied widely in the mineral flotation, which requires a systematic investigation on multiphase flow characteristics of the salt solution.…”
With enormous interfacial area for particle collection, microbubbles exhibit great application prospect in the mineral flotation. Under certain ionic strength, microbubbles can be produced continuously in the microbubble column without extra reagent addition. In this work, multiphase flow characteristics (Sauter mean diameter, bubble size distribution, gas holdup & interfacial area) were studied systematically with variables including the salt type, salt concentration, and operating conditions. Based on mathematical model, critical coalescence concentration was determined for each investigated salt. According to experimental results, a mathematical correlation was established between the Sauter mean diameter and ionic strength. For the formation of microbubble system, the lowest ionic strength was approximately 0.5 mol/L. Multiphase flow characteristics in the microbubble column depended highly on the ionic strength. The interfacial area and gas holdup increased by 38 times and more than 3 times respectively, with the ionic strength of Al2(SO4)3 rising from 0 to 1.5 mol/L. The critical coalescence concentration ranged from 0.037 mol/L (Al2(SO4)3) to 0.517 mol/L (NaCl), which correlated with the ionic strength of each salt.
“…However, this increase in the cultivation medium pumped into the biogas scrubbing unit resulted in increased in N2 and O2 concentrations regardless of the type of diffuser tested. This can be explained by the superior dissolved gas stripping at higher liquid flowrates, which negatively impacted on the final concentration of CH4 in the upgraded biogas [20]. The biogas quality at a L/G ratios of 1 and 2 fulfilled with the current European biomethane standard regardless of the diffuser configuration [2,18,19] Overall, the results herein obtained confirmed that the metallic diffuser was the best system to purify biogas at the L/G ratios typically implemented in photosynthetic biogas upgrading processes in open photobioreactors.…”
Four different types of biogas diffusers (metallic of 2 µm, porous stone, and two ceramic membranes of 0.2 and 0.4 µm) were evaluated to improve the quality of biomethane in an outdoor pilot scale photobioreactor interconnected to an external biogas absorption unit. Each type of diffuser was tested independently using three different liquid to biogas (L/G) ratios (0.5, 1 and 2). No significant difference was recorded in the CH4 concentrations of biomethane (i.e. > 93.0%) working with the different types of diffusers at L/G ratios > 1. Only the metallic biogas diffuser supported CH4 concentrations higher than 94.0% at a L/G ratio of 0.5. The increase in L/G ratio induced the stripping of the dissolved N2 and O2 into the biogas, which compensated the decrease in CO2 concentration mediated by the higher pH value of the scrubbing solution. The ANOVA of the results here obtained confirmed that both the type of biogas diffuser and the L/G ratio significantly determined the quality of the upgraded biogas.
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