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Alternative Ultrafiltration Membrane Testing for the SRS Baseline Process

机译:SRS基线过程的替代超滤膜测试

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The ability to more rapidly process high-level waste sludge and supernate, without sacrificing cost savings, continues to be a crucial challenge facing the Savannah River Site (SRS). There has, to date, not been any extensive investigation of alternative filter technologies for the SRS baseline process. To address this problem, a focused investigation into alternative, state-of-the art filtration technologies to facilitate the strontium and actinide removal process, which can be cost effectively implemented in existing facilities and current equipment designs, was completed. Filter technologies manufactured by Mott (0.1 micron and 0.5 micron) Graver (0.07 micron), Pall (0.1 micron and 0.8 micron) and GKN (0.1 micron) were evaluated. Membranes had a nominal inside diameter of 3/8 inches and an active membrane length of 2 feet. The investigation was performed in two phases. The first phase of testing evaluated the consistency or variability in flux through the different membranes using water and a standard 5.0 wt percent strontium carbonate slurry. The second phase of testing evaluated the achievable permeate flux and clarity through the various membranes using the SRS average salt supernate simulant at solids loadings of 0.06, 0.29 and 4.5 wt percent. Membrane variation data indicate that membranes having an asymmetric ceramic coating (Pall 0.1 micron and Graver 0.07 micron), typically displayed the lowest variability with water. Membranes without a ceramic asymmetric coating (Mott 0.5 micron and GKN 0.1 micron) displayed the highest variability. This is most likely associated with the experimental uncertainties in measuring large volumes of permeate in a short amount of time and to the impact of impurities in the water. In general, variability ranging from 4-56 percent was observed when using water for all membranes. In the case of variation testing using strontium carbonate, variability decreased to 3-12 percent. In addition, membrane structure or composition had little effect on the variability. Data obtained from SRS simulant testing, indicate that membranes having a ceramic asymmetric coating (Graver 0.07 micron, Pall 0.1 micron), typically achieved the highest average steady state fluxes for all solution concentrations evaluated. In general, the Graver 0.07 micron and Pall 0.1 micron membranes achieved fluxes approximately 13 to 21 percent higher than those observed with the baseline Mott 0.1 micron membrane using the SRS simulant at solids loadings of 0.29 and 4.5 wt percent. Membranes without a ceramic asymmetric coating (GKN, Mott) achieved the lowest average steady state fluxes. It is postulated that small particles present in solution were unable to penetrate the ceramic layer, thus producing surface filtration where the filter cake acts as the filter medium. Conversely, membranes without the asymmetric ceramic coating were susceptible to the small particles present in solution penetrating into the internal pore structure of the membrane, thus producing depth filtration where the porosity is greatly reduced by particles trapped within the interstices of the internal structure. Turbidity data indicate that permeate from the alternative membranes provided reduced or equivalent turbidity measurements when compared to the baseline 0.1 micron Mott membrane.
机译:更快速地处理高放射性废物的污泥和上清液,在不牺牲成本节约的能力,仍然是面临的萨凡纳河站点(SRS)的一个关键挑战。有先后,到今天为止,没有得到的替代性过滤器技术,为SRS基线过程中的任何广泛的调查。为了解决这个问题,有重点调查的替代,国家的最先进的过滤技术,以促进锶和锕系元素去除过程,这在现有的设施和现有设备的设计有效的执行成本,已经完成。通过莫特(0.1微米和0.5微米)格拉弗(0.07微米),帕尔(0.1微米和0.8微米)和GKN(0.1微米)。制造过滤器技术进行了评价。膜具有3/8英寸的标称内径和2英尺的有效膜长度。分两个阶段进行调查。的第一阶段通过使用水和标准5.0重量%的碳酸锶浆料中的不同的膜进行评价的测试在焊剂中的一致性或变性。的第二阶段测试评价可达到的渗透通量和清晰度通过使用SRS在0.06,0.29和4.5重量%的固体加载量平均盐上清液模拟的各种膜。膜变化的数据表明,具有不对称的陶瓷涂层(帕尔0.1微米和0.07格拉弗微米)的膜,典型地显示与水的最低可变性。不含陶瓷不对称涂层(莫特0.5微米和GKN 0.1微米)的膜表现出最高的可变性。这是最有可能与在测量很短的时间量和杂质在水流的冲击大量渗透实验的不确定性有关。一般情况下,可变性范围从使用水对所有膜时观察到4-56%的。在使用碳酸锶变异测试的情况下,可变性减小到百分之3-12。此外,膜的结构或组合物对可变性的影响不大。从SRS模拟测试数据获得的,表明具有陶瓷涂层的非对称膜(雕刻刀0.07微米,帕尔0.1微米),通常达到的最高的平均稳态通量为所有的溶液浓度进行评价。一般而言,雕刻刀0.07微米和0.1帕尔微米膜实现通量比那些使用SRS基线莫特0.1微米的膜观察到的高约13至21%在0.29和4.5重量%的固体加载量模拟物。不含陶瓷不对称涂层(GKN,莫特)膜达到的最低平均稳态通量。据推测,存在于溶液中的小颗粒无法穿透陶瓷层,从而产生表面过滤,其中滤饼作为过滤介质。相反地​​,如果没有非对称陶瓷涂层膜易受到小颗粒存在于溶液渗透到膜的内部孔结构,从而产生深度过滤,其中孔隙率在很大程度上受到截留在内部结构的空隙内的颗粒减少。相比于基线0.1微米莫特膜时的浊度数据指示来自提供减少或等效浊度测量的替代膜的是渗透物。

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