首页> 外文会议>10th Gothenburg Symposium on Chemical Water and Wastewater Treatment VII 2002, Jun 17-19, 2002, Gothenburg, Sweden >Break-up and Re-formation of Floes Formed by Hydrolyzing Coagulants and Polymeric Flocculants
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Break-up and Re-formation of Floes Formed by Hydrolyzing Coagulants and Polymeric Flocculants

机译:水解混凝剂和高分子絮凝剂形成的浮球的分解和重整

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The results presented here highlight very significant aspects of floc formation, breakage and re-growth. Under the conditions used, the metal-based coagulants showed a more rapid onset of flocculation, but significantly smaller floes than with the polyelectrolytes. The lag time in the latter case is due to the relatively slow adsorption of these materials on the clay particles. With the dilute suspensions used and the low polymer concentrations it is expected that adsorption of sufficient polymer to give particle destabilization can be quite long compared to the particle collision rate (Gregory, 1988). The low molecular weight polyDADMAC shows a shorter lag time, which may be a result of its more rapid diffusion than the much larger molecules of the other two polymers. For the hydrolyzing coagulants, hydroxide precipitation occurs quite rapidly and so flocculation begins soon after coagulant dosing. It is noticeable that the pre-hydrolyzed products show an earlier onset of flocculation than with alum and ferric sulphate, most likely because of a more rapid precipitation. The experiments revealed that iron-based coagulants give larger floes than those based on aluminium. The behaviour of iron (III) is similar to that of aluminium in that sweep flocculation by the hydroxide is fast and dominates at around neutral pH. Because of the much lower solubility of ferric hydroxide, rather more precipitate would be expected than with alum for equimolar dosages (as in the present case). For both aluminium and iron, the pre-hydrolyzed product gave significantly increased floc size, but only marginal differences in residual turbidity before floc breakage. However, the re-formed floes showed better removal by sedimentation. The similar form of the FI curves in Figures 1 and 2 strongly suggests that floes are of broadly similar nature for all the metal-based coagulants, but are significantly stronger with the pre-hydrolyzed products. The underlying mechanisms are not well understood and it is unlikely that simple charge effects can explain the results. The polymeric flocculants gave significant differences in floc size, with polyDADMAC giving larger FI values. This finding is difficult to explain in terms of the different molecular weights, since it is expected that higher molecular weight polymers should give stronger floes, either as a result of polymer bridging or 'electrostatic patch' effects (Gregory, 1996). For the dilute suspensions used here and the relatively low particle collision rates, it is expected that adsorbed polymers would adopt a rather flat configuration, which makes bridging unlikely. It has been shown (Kam and Gregory, 2001) that high charge density poly electrolytes are more effective in removing humic substances from water. Since the suspensions used are stabilized by humic acid and polyDADMAC has a much higher charge density than Zetag 64, charge effects may partly explain the observed behaviour. The fact that an anionic polyelectrolyte (Magnafloc 156) gives similar results is surprising. The high level of calcium in the tap water used may play a significant part. Although there have been previous reports of the irreversible nature of floc breakage with hydrolysing coagulants, the reasons remain unclear. Irreversible breakage suggests that chemical bonds are broken. When particle interaction is of a physical nature (such as van der Waals or electrostatic attraction) there is no obvious reason why aggregates should not re-form after breakage. With polymeric flocculants, irreversible floc breakage is well known, but it is usually associated with bridging interactions (Ditter et al, 1982). High shear rates (especially with turbulence) may cause scission of polymer chains (Horn and Merrill, 1984) and adsorbed polymer could adopt a more flat configuration during the breakage phase. However, these considerations do not apply when charge neutralization or 'electrostatic patch' effects are responsible for flocculation, so tha
机译:这里介绍的结果突出了絮凝物形成,破裂和重新生长的非常重要的方面。在所使用的条件下,基于金属的凝结剂显示出更快的絮凝开始,但是与聚电解质相比,絮凝剂明显更小。在后一种情况下的滞后时间是由于这些材料在粘土颗粒上的吸附相对较慢。使用稀释的悬浮液和低的聚合物浓度,与颗粒碰撞速率相比,可以预期足够的聚合物吸附使颗粒不稳定,可能会很长(Gregory,1988)。低分子量的polyDADMAC显示出更短的滞后时间,这可能是由于它比其他两种聚合物的大得多的分子更快地扩散的结果。对于水解凝结剂,氢氧化物沉淀相当迅速地发生,因此在凝结剂投配后不久就开始絮凝。值得注意的是,与用明矾和硫酸铁相比,预水解产品显示出更早的絮凝开始,这很可能是因为沉淀更快。实验表明,铁基凝结剂比铝基凝结剂产生更大的絮凝物。铁(III)的行为与铝类似,因为氢氧化物的快速絮凝很快,并且在中性pH左右占主导地位。由于氢氧化铁的溶解度低得多,对于等摩尔剂量(与目前的情况一样),预计会比明矾有更多的沉淀。对于铝和铁,预水解产物的絮凝物尺寸均显着增加,但絮凝物断裂前残留浊度仅略有差异。然而,重新形成的絮凝物显示出通过沉降的更好去除。图1和2中FI曲线的相似形式强烈表明,絮凝物对于所有基于金属的凝结剂具有大致相似的性质,但对于预水解产物则明显更强。潜在的机制尚不完全清楚,简单的电荷效应不可能解释结果。聚合絮凝剂的絮凝度差异显着,而聚DADMAC的絮凝度值较大。很难用不同的分子量来解释这一发现,因为人们期望较高分子量的聚合物应产生更强的絮凝物,这是由于聚合物桥接或“静电贴片”效应所致(Gregory,1996)。对于此处使用的稀释悬浮液和相对较低的颗粒碰撞率,预计吸附的聚合物将采用相当平坦的构造,这使得桥接不太可能。已经显示出(Kam和Gregory,2001),高电荷密度的聚电解质对于从水中去除腐殖质更有效。由于所用的悬浮液被腐殖酸稳定,并且聚DADMAC具有比Zetag 64高得多的电荷密度,因此电荷效应可以部分解释所观察到的行为。阴离子聚电解质(Magnafloc 156)给出类似结果的事实令人惊讶。自来水中所含的高钙可能起重要作用。尽管以前有关于使用水解混凝剂的絮凝破损具有不可逆性的报道,但原因尚不清楚。不可逆的断裂表明化学键断裂。当颗粒相互作用具有物理性质(例如范德华力或静电吸引)时,没有明显的理由说明破碎后不应重新形成聚集体。对于聚合物絮凝剂,不可逆的絮凝破坏是众所周知的,但它通常与桥接相互作用有关(Ditter等,1982)。高剪切速率(特别是湍流)可能会导致聚合物链断裂(Horn和Merrill,1984),并且在断裂阶段,吸附的聚合物可能会采用更扁平的形态。但是,当电荷中和或“静电补丁”效应导致絮凝时,这些考虑因素将不适用,因此

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