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首页> 外文期刊>The Korean journal of chemical engineering >Ultrafiltration behaviors of pectin-containing solution extracted from citrus peel on a ZrO_2 ceramic membrane pilot unit
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Ultrafiltration behaviors of pectin-containing solution extracted from citrus peel on a ZrO_2 ceramic membrane pilot unit

机译:ZrO_2陶瓷膜中试装置从柑桔皮中提取的含果胶溶液的超滤行为

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摘要

Ultrafiltration experiments on a solution of pectin, hesperidin, and other mixtures extracted from citrus peels have been performed on a 500 l/min pilot scale crossflow ceramic membrane unit. A 30,000 molecular weight cut-off (MWCO) zirconia (ZrO_2) ceramic membrane with a total effective flow area of 0.5 m~2 was used in the process. The permeate flux for pure water and hesperidin showed linear relationship with transmembrane pressure (AP), but the flux for pectin solutions showed a curvilinear relationship with AP and represented a rapid increase with increasing AP before leveling-off. Similar behavior was observed by adding different amounts of hesperidin to these pectin solutions, but with much lower permeate flows. The formation of gel layers on the membrane surface is mainly responsible for the lower permeate fluxes. In addition, the permeate flux decrease faster at higher AP, since higher AP brought bigger flux at lower pectin concentration. Compared with the more than 90% retention rate of macromolecu-lar pectin, pigment and other component have less than 20% retention rate. So, the decolorization, the separation and purification of pectin preparations could be achieved simultaneously through ultrafiltration with a ceramic membrane.
机译:对果胶,橙皮苷和从柑桔皮中提取的其他混合物的溶液进行超滤实验已在500升/分钟的中试规模错流陶瓷膜装置上进行。该工艺中使用了总截留面积为0.5 m〜2的30,000截留分子量(MWCO)的氧化锆(ZrO_2)陶瓷膜。纯水和橙皮苷的渗透通量与跨膜压(AP)呈线性关系,而果胶溶液的通量与AP呈曲线关系,并且在稳定前随AP的增加而迅速增加。通过向这些果胶溶液中添加不同量的橙皮苷观察到相似的行为,但渗透流量要低得多。膜表面上凝胶层的形成主要是导致较低的渗透通量的原因。此外,较高的AP会导致渗透通量下降更快,因为较高的AP在较低的果胶浓度下会带来较大的通量。与高分子果胶的90%以上的保留率相比,颜料和其他成分的保留率不到20%。因此,果胶制剂的脱色,分离和纯化可通过陶瓷膜超滤同时实现。

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