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Decolourization of dye-containing effluent using mineral coagulants produced by electrocoagulation

机译:使用电凝产生的矿物凝结剂对含染料废水进行脱色

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The colour and colour causing-compounds has always been undesirable in water for any use, be it industrial or domestic wastewaters. The discharge of such effluents causes excessive oxygen demand in the receiving water and then a treatment is required before discharge into ecosystems. This study examined the possibility to remove colour causing-compounds from effluent by chemical coagulation, in comparison with direct electrocoagulation. The inorganic coagulants (C|, C_2 and C_3) in the form of dry powder tested, were respectively produced from electrolysis of S_1 = [NaOH (7.5 × 10~(-3) M)], S_2 = [NaCl (10~(2) M)], and S_3 = [NaOH (7.5 × 10~(-3) M) + NaCl (10~(-2) M)] solutions, using sacrificial aluminium electrodes operated at an electrical potential of 12 V. Reactive textile dye (CI Reactive Red 141) was used as model of colour-causing compound prepared at a concentration of 50 mg l~(-1). The best performances of dye removal were obtained with C_2 having a chemical structure comprised of a mixture of polymeric specie (Al_(45)(OH)_(45)Cl) and monomeric species (ArCl(OH)_2·2H_2O and Al(OH)_3). The removal efficiency (R_A) evaluated by measuring the yields of 540 nm-absorbance removal varied from 41 to 96% through 60 min of treatment by imposing a concentration of C_2 ranging from 100 to 400 mg l~(-1). The effectiveness of the treatment increased and the effluent became more and more transparent while increasing C_2 concentration. The comparison of chemical treatment using C_2 coagulant and direct electrocoagulation of CI Reactive Red 141 containing synthetic solution demonstrated the advantage of chemical treatment during the first few minutes of treatment. A yield of 88% of absorbance removal was recorded using C_2 coagulant (400 mg l~(-1)) over the first 10 min of treatment, compared to 60% measured using direct electrocoagulation while imposing either 10 or 15 V of electrical potential close to the value (12 V) required during C_2 production. However, at the end of the treatment (after 60 min of treatment), CI Reactive Red 141 pollutant was completely removed from solution (540 nm-absorbance removal of 100%) using direct electrochemical treatment, compared to 96.4% of absorbance removed while treating dye-containing synthetic solution by means of C_2 coagulant.
机译:在任何用途中,无论是工业废水还是家庭废水,这种颜色和引起颜色的化合物一直是人们所不希望的。此类废水的排放会导致接收水中过量的氧气需求,然后在排放到生态系统之前需要进行处理。这项研究与直接电凝相比,研究了通过化学凝结从废水中去除发色化合物的可能性。电解S_1 = [NaOH(7.5×10〜(-3)M)],S_2 = [NaCl(10〜( 2)M)],S_3 = [NaOH(7.5×10〜(-3)M)+ NaCl(10〜(-2)M)]溶液,使用在12 V电势下工作的牺牲铝电极。以纺织染料(CI活性红141)为模型,制备了浓度为50 mg l〜(-1)的发色化合物。使用具有由高分子物质(Al_(45)(OH)_(45)Cl)和单体物质(ArCl(OH)_2·2H_2O和Al(OH)的混合物组成的化学结构的C_2可获得最佳的染料去除性能)_3)。通过测量540 nm的C_2浓度范围为100到400 mg l〜(-1),通过测量540 nm吸光度的去除率来评估去除效率(R_A)从41%到96%。在增加C_2浓度的同时,处理的有效性提高了,出水变得越来越透明。使用C_2混凝剂进行化学处理和对包含合成溶液的CI Reactive Red 141进行直接电凝的比较证明了在处理的前几分钟内化学处理的优势。在处理的前10分钟,使用C_2凝结剂(400 mg l〜(-1))记录的吸光度去除率为88%,相比之下,在施加10或15 V电位的情况下使用直接电凝法测得的吸收率为60%到C_2生产期间所需的值(12 V)。但是,在处理结束时(处理60分钟后),使用直接电化学处理从溶液中完全去除了CI Reactive Red 141污染物(540 nm吸光度去除了100%),而处理时去除了96.4%的吸光度通过C_2混凝剂制成的含染料的合成溶液。

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