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Separation of Ni(II) from Nickel-containing Wastewater in an Emulsion Liquid Membrane System with P507 as Carrier

机译:用P507作为载体将Ni(II)从乳液液膜系统中的含镍废水分离

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An effective emulsion liquid membrane system with P507 as carrier, Span-80 as surfactant and H_2SO_4 as internal aqueous phase was established to treat Ni( II )-containing wastewater. The effects of volume fraction of Span-80 in the oil phase(Φ(Span-80)), emulsifying siirring speed(v_1), separation stirring speed(v_2), volume fraction of P507(Φ(P507)), volume ratio of oil phase to internal phase(i?0;), milk phase to water phase(R_(ew)) and concentration of H_2SO_4 in internal aqueous phase on Ni( II) migrating rate have been investigated in the course of migrating of nickel ions in the system. The optimal operation conditions were determined to be: Φ(Span-80)=8.5%,v_1 =3600 r-min~(-1),v_2 =320 r-min~(-1), Φ(P507)=6.5%, R_(oi) =1:1, R_(ew) =2:5 and c (H_2SO_4) =1.6 molL~(-1) ,under which the migrating rate of nickel ions reached above 97%.
机译:建立具有P507的有效乳液液膜系统作为载体,作为表面活性剂和作为内水相的H_2SO_4,以治疗Ni(II)废水。跨度-80体积分数在油相中的影响(φ(寿命-80)),乳化瞬间(V_1),分离搅拌速度(V_2),P507的体积分数(φ(p507)),体积比在镍离子迁移过程中研究了内相(I→0;),对水相(R_(ew))和内部水相中的H_2SO_4浓度的乳液相系统。确定最佳操作条件是:φ(跨度-80)= 8.5%,V_1 = 3600 r-min〜(-1),V_2 = 320 r-min〜(-1),φ(p507)= 6.5% ,R_(OI)= 1:1,R_(EW)= 2:5和C(H_2SO_4)= 1.6莫尔〜(-1),镍离子的迁移率达到97%以上。

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