Continuous Foam Fractionation Column Research Articles

Prediction of foaming and surface tension of lean MDEA solutions with corrosion inhibitor (bis(2-hydroxyethyl)cocoalkylamine) in continuous foam fractionation column

ABSTRACTAmine foaming is a common problem in gas sweetening unit. Prediction of foaming behavior will help in unraveling the operational challenges faced by the gas industry. This study was performed with the aim of predicting the foam volume and surface tension of lean methyldiethanolamine solutions in presence of bis(2-hydroxyethyl)cocoalkylamine (BHCL) corrosion inhibitor using continuous foam fractionation technique. The effect of BHCL as a model foam creators on foaming tendency was explored. The obtained experimental results were used to determine the empirical parameters k and n of the power law relation previously derived for high viscous fluid (i.e., ), both and are dimensionless parameters. The prediction model gave a good agreement with the experimentally observed results (<6% deviation). The foam height model helped in envisaging the surface tension profile and in turn the separation performance and efficiency of foam creators. The foam height increased with increasing superficial gas velocity and BHCL concentration. For low BHCL concentrations, the minimum surface tension was noticed at superficial gas velocity of 0.02 m/s.

Process intensification of foam fractionation by successive contraction and expansion

Enrichment in foam fractionation is enhanced by reducing the liquid flux while maintaining the flux of bubble surfaces. We show that it is possible to do so in a continuous foam fractionation column by inserting a plate into the foam layer and forcing the foam through a narrower tube (foam riser) mounted at the centre of the plate. A 35% reduction in liquid flux was observed by using a single plate-foam riser assembly in a foam stabilised by 0.52 g/L sodium dodecyl sulphate solution, and the liquid rejected from the foam due to the presence of the foam riser had the same concentration as the feed solution. However, due to the nature of the adsorption isotherm of SDS, the enrichment enhancement measured in the experiments hererin was modest. The mechanism of the foam riser plate was explained by invoking recent theoretical studies on pneumatic foam. It was demonstrated that the reduction in liquid flux was affected by sudden expansion of the flow area causing a rejection of interstitial liquid to the top of the plate and extracted, whence it was recycled back to the feed. Preliminary experiments on the effect of liquid pool depth and foam height on interfacial adsorption were also carried out to demonstrate that the insertion of the plate does not affect the adsorption of the target substance to the bubble surface in the current system. It was found that equilibrium could be achieved within 0.2 m of liquid pool depth or foam height, however the equilibrium surface excess on a rising bubble in the liquid pool is roughly 51% of the equilibrium value on a quiescent interface, while that in the foam layer is roughly 73% of the equilibrium value on a quiescent interface.

Polarized light based scheme to monitor column performance in a continuous foam fractionation column

BackgroundA polarized light scattering technique was used to monitor the performance of a continuously operated foam fractionation process. The S11 and S12 parameters, elements of the light scattering matrix, combined together (S11+S12) have been correlated with the bubble size and liquid content for the case of a freely draining foam. The performance of a foam fractionation column is known to have a strong dependence on the bubble size distribution and liquid hold up in foam. In this study the enrichment is used as a metric, representative of foam properties and column performance, and correlated to the S11+S12 parameter.ResultsThree different superficial gas velocities (6.9, 7.5, and 10.6 cm/min) and four different pH values (4.8, 5.5, 6.5, and 7.5) are tested for the foam fractionation of a dilute solution of bovine serum albumin (0.1 mg/ml). As a result, at scattering angle of 125° the magnitude of S11+S12 is higher as the pH increases. When the bubble sizes are small with a larger liquid content, the foam is strongly back scattering resulting in lower values of S11+S12 (at 125°) at pH = 4.8. The light scattering data and the enrichment values are measured over a period of 90 minutes and correlated using a linear model. The predictive power of the model was found to be statistically significant.ConclusionThe time average S11+S12 shows a direct proportionality with the enrichment value, indicating that polarized light should be a valuable technique for monitoring foam fractionation columns. Additional knowledge of the nature of dependence between foam properties and S11+S12 combined with models relating the enrichment to the bubble size and liquid hold up is needed to develop an accurate diagnostics tool for monitoring enrichment utilizing S11+S12 measurements.

Modelling continuous foam fractionation with reflux

An equilibrium stage approach is taken to modelling the performance of a continuous foam fractionation column with reflux. Such an approach has been facilitated by recent developments in the understanding of pneumatic columns of foam that allow liquid rates within the rising column of foam to be predicted with confidence. It is shown that the recovery of surfactant into the product stream increases monotonically with increasing reflux ratio but this is at the expense of reduced product rate.

Effect of pH on the Startup of a Continuous Foam Fractionation Process Containing Ovalbumin

The effect of pH on the bubble size distribution, void fraction, and enrichment ratio of a continuous foam fractionation column containing ovalbumin was investigated. The bubble size and void fraction were measured using a photoelectric capillary probe for different solution pHs (3.5, 4.5, 6.5, and 9.7). The bubble diameters for pH 3.5 and 4.5 were the largest of the four pHs studied. At these two pHs, the foam was less stable and formed aggregates, leading to lower enrichment and mass recovery. For the nearly neutral pH 6.5 or the more basic pH 9.7, the bubble size was smaller and the foam was more stable, resulting in both high enrichment and high mass recovery. The void fraction was smallest for pH 6.5, but the effect of pH on void fraction was not significant. In the lower foam phase, the calculated specific area increased as the pH increased from 3.5 to 9.7, which may partially contribute to the higher enrichments at pH 6.5 and 9.7.

Effect of bubble size on foam fractionation of ovalbumin.

The bubble size distribution and void fraction (epsilong) (at two bulk liquid pool positions below the bulk liquid-foam interface and one lower foam phase position) in a continuous foam fractionation column containing ovalbumin were obtained using a photoelectric capillary probe. The bubble size and epsilong data were gathered for different operating conditions (including the changes in the superficial gas velocity and feed flow rate) at a feed solution of pH 6.5 and used to calculate the specific area, a, of the bubbles. Thus, local enrichment (ERl), values of ovalbumin could be estimated and compared with directly obtained experimental results. The ERl results were also correlated with the bubble size and epsilong to understand better the concentration mechanisms of foam fractionation. The high ERl in the lower foam phase was largely attributable to the abrupt increase in epsilong (from 0.25 to 0.75), or the a (from about 12 to 25 cm2/cm3) from the bulk liquid to the foam phase. These changes correspond with enhanced gravity drainage. With an increase in the superficial gas velocity, the bubble size increased and the a decreased in both the bulk liquid and lower foam phases, resulting in a decrease in the local experimentally determined enrichments at high superficial gas velocities. At intermediate feed flow rates, the bubble size reached the maximum. The epsilong and a, on the other hand, were the largest for the largest feed flow rate. The ERl in the lower foam phase was maximized at the lowest feed flow rate. It follows, therefore, that a alone is not sufficient to determine the magnitude of the ERl in the foam phase.

A Model for Continuous Foam Concentration of Proteins: Effects of Kinetics of Adsorption of Proteins and Coalescence of Foam

Abstract A model for concentration of proteins from dilute solutions in a continuous foam fractionation column is proposed. This model accounts for (1) kinetics of adsorption of proteins in the liquid pool as well as in the foam, (2) liquid drainage from thin films due to Plateau border suction and disjoining pressure, (3) gravity drainage of liquid from Plateau borders, and (4) bubble coalescence in the foam. Protein enrichment and recovery were found to increase as the liquid pool height increased, eventually attaining constant values (corresponding to adsorption equilibrium), thus demonstrating the strong dependence of protein separation on adsorption kinetics. Higher enrichments and lower recoveries were obtained for smaller gas velocities, larger bubble sizes, and higher feed flow rates. Enrichments as well as recoveries were higher at lower feed concentrations. Coalescence was found to lead to higher enrichments and lower recoveries, this dependence being stronger for larger inlet bubble sizes.

Effect of Coalescence on the Performance of a Continuous Foam Fractionation Column

Abstract A model for the hydrodynamics of coalescing foam bed is proposed which accounts for liquid drainage through thin films and plateau borders, bubble coalescence, and mixing of liquid between thin films and plateau borders. Foam bed is assumed to consist of equal sized dodecahedral bubbles at any cross section, and the variation of bubble size with foam height due to coalescence is described through phenomenological models. This model is employed to investigate the effect of coalescence on enrichment and recovery for the nonanol-water system in a continuous foam fractionation column for different inlet bubble sizes, superficial gas velocities, and inlet concentrations. Coalescence is found to yield higher enrichments and lower recoveries, possibly because of the predominant effect of increased liquid drainage due to larger bubble sizes resulting in a significant decrease in liquid holdup with foam height. Larger bubble sizes and lower superficial gas velocities were found to result in higher enrichm...

Foam fractionation of globular proteins

Foam fractionation of bovine serum albumin (BSA) was studied as a model system for potato wastewater. The effects of feed concentration, superficial gas velocity, feed flow rate, bubble size, pH, and ionic strength on the enrichment and recovery of BSA were investigated in a single-stage continuous foam fractionation column. Enrichments ranged from 1.5 to 6.0 and recoveries from 5 to 85%. The feed concentrations were varied from 0.01 to 0.2 wt %, and enrichments were found to increase with lower feed concentrations. Enrichments also increased with lower superficial gas velocities and larger bubble sizes. At sufficiently low feed flow rates, enrichment was found to increase with an increase in the flow rate, eventually becoming insensitive to the feed flow rate at higher values. The pH was varied from 3.5 to 7.0 and ionic strength from 0.001M to 0.2M. The effects of pH and ionic strength were found to be coupled with bubble size. A minimum bubble size was found at pH 4.8, the isoelectric point of BSA, resulting in a minimum in the enrichment. Bubble size, and thus enrichment, was found to increase as the ionic strength decreased from 0.2M to 0.01M. Previous models(1,2) for the hydrodynamics of foam column were extended for a singlestage continuous foam fractionation column for the prediction of enrichment and recovery. The model assumed adsorption equilibrium, infinite surface viscosity, and bubbles of the same size. Though coalescence was formally accounted for in the model by considering bubble size as a function of foam height, calculations for the experimental runs were performed only for the case of no coalescence. Quantitative predictions of enrichment and recovery could not be made with a single representative bubble size because of the broad inlet bubble size distribution as well as broadening of the distribution as a result of coalescence. The experimental enrichments were higher and recoveries were lower than the model predictions, the discrepancy being more pronounced at lower feed concentrations because of increased coalescence. The higher enrichments are due to the predominant effect of internal reflux as a result of coalescence whereas the lower recoveries are a result of detrimental effects of broadening bubble size distributions.

Separation of a surface active solute by foam fractionation

A continuous foam fractionation column in the simple mode is used to treat the dilute aqueous solutions of a surface active solute, benzyl-dimethyl-cetylammonium chloride. The drainage of the interstitial liquid makes the foam column more effective. This is because it not only serves as the internal reflux but also reduces the amount of bulk solution carried in the overflowing foam. Higher feed concentration and higher gas flow rate reduce the drainage of the interstitial liquid and thus are unfavorable to the separation capability of the foam fractionation column.