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The wash-off of dyeings using interstitial water: Part 3. Disperse dyes on polyester

机译:使用间隙水冲洗染料:第3部分。将染料分散在聚酯上

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Poly(ethylene terephthalate), which had been dyed at 0.5,1.0 and 2.0% omf depths of shade using three disperse dyes, was reduction cleared using a traditional, four-stage process that comprised two water rinses at 40 °C, treatment with aq Na2CO3/Na2S2O4 at 60 °C and one cold water rinse. A novel, two-stage wash-off method was also employed that consisted of treatment with damp nylon beads and surfactant at 70 °C and one cold water rinse. In terms of fastness to repeated washing at 60 °C and colorimetric characteristics, the traditional, four-stage reduction clearing treatment using aq., alkaline Na2S2O4 could be replaced by the two-stage, bead wash-off with detergent at 70 °C. As the detergent-based, bead wash-off process used lower amounts of water than reduction clearing and did not employ sodium dithionite, it avoided the environmentally unacceptable generation of aromatic amines in the case of the reduction clearing of azo dyes. Calculations indicated that considerably less heat energy was consumed in bead wash-off than reduction clearing not only because two, rather than four stages were involved but also since the bead process used only a 2:1 water: fibre ratio rather than the 20:1 liquor ratio employed in the reduction clear process; also, the much lower specific heat capacity of nylon than water meant that much less heat was required to heat the beads. The beads adsorbed vagrant disperse dye during wash-off, thereby offering the potential of a lower effluent load compared to a traditional reduction clearing treatment for disperse dyes on polyester.
机译:聚对苯二甲酸乙二醇酯,已使用三种分散染料分别在0.5、1.0和2.0%omf的阴影深度进行染色,使用传统的四阶段方法进行还原清除,该方法包括在40°C下进行两次水漂洗,并用无水硫酸处理。在60°C下用Na2CO3 / Na2S2O4冲洗一次。还采用了一种新颖的两阶段冲洗方法,该方法包括在70°C下用湿尼龙珠和表面活性剂进行处理,然后用冷水冲洗一次。就在60°C下重复洗涤的牢度和比色特性而言,使用碱性Na2S2O4水溶液进行的传统四步还原清除处理可以用在70°C下用洗涤剂进行的两步珠洗来代替。由于以洗涤剂为基础的珠粒冲洗工艺比还原透明胶使用的水量少,并且不使用连二亚硫酸钠,因此在偶氮染料还原透明胶的情况下,避免了环境上无法接受的芳香胺的生成。计算表明,洗珠过程比还原清除过程消耗的热能少得多,这不仅是因为涉及两个阶段,而不是四个阶段,而且因为珠过程仅使用2:1的水:纤维比,而不是20:1的比例。还原澄清过程中使用的液比;同样,尼龙的比热容比水低得多,这意味着加热珠粒所需的热量少得多。珠粒在冲洗过程中吸附了游走的分散染料,因此与传统的分散澄清方法在聚酯上进行还原处理相比,可以提供较低的出水量。

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