工业用水与废水
工業用水與廢水
공업용수여폐수
INDUSTRIAL WATER & WASTEWATER
2015年
3期
26-29,50
,共5页
规整型电极%苯酚废水%·OH%三维电极
規整型電極%苯酚廢水%·OH%三維電極
규정형전겁%분분폐수%·OH%삼유전겁
structured electrode%phenol wastewater%·OH%three dimension electrodes
采用自制的长方体蜂窝状规整型第三电极和乱堆型粒子电极为填充电极的三维电极体系处理苯酚废水,比较了规整型第三电极、乱堆型粒子电极对苯酚废水的处理效果,以及降解过程中·OH、 H2O2、苯酚浓度、CODCr浓度的变化情况,探讨了苯酚降解的反应动力学,并运用红外光谱初步研究了苯酚的降解机理。结果表明,在电解质投加量为5 g/L,电压为7 V, pH值为5,极板间距为4 cm的条件下,与乱堆型粒子电极相比,规整型第三电极对苯酚去除率提高了22.50%,并且苯酚在三维电极反应器内的降解反应符合拟一级反应动力学模型,反应速率常数为0.014 min-1。
採用自製的長方體蜂窩狀規整型第三電極和亂堆型粒子電極為填充電極的三維電極體繫處理苯酚廢水,比較瞭規整型第三電極、亂堆型粒子電極對苯酚廢水的處理效果,以及降解過程中·OH、 H2O2、苯酚濃度、CODCr濃度的變化情況,探討瞭苯酚降解的反應動力學,併運用紅外光譜初步研究瞭苯酚的降解機理。結果錶明,在電解質投加量為5 g/L,電壓為7 V, pH值為5,極闆間距為4 cm的條件下,與亂堆型粒子電極相比,規整型第三電極對苯酚去除率提高瞭22.50%,併且苯酚在三維電極反應器內的降解反應符閤擬一級反應動力學模型,反應速率常數為0.014 min-1。
채용자제적장방체봉와상규정형제삼전겁화란퇴형입자전겁위전충전겁적삼유전겁체계처리분분폐수,비교료규정형제삼전겁、란퇴형입자전겁대분분폐수적처리효과,이급강해과정중·OH、 H2O2、분분농도、CODCr농도적변화정황,탐토료분분강해적반응동역학,병운용홍외광보초보연구료분분적강해궤리。결과표명,재전해질투가량위5 g/L,전압위7 V, pH치위5,겁판간거위4 cm적조건하,여란퇴형입자전겁상비,규정형제삼전겁대분분거제솔제고료22.50%,병차분분재삼유전겁반응기내적강해반응부합의일급반응동역학모형,반응속솔상수위0.014 min-1。
Using three dimension electrodes systems filled with home-made cuboid honeycomb structured third electrode and disorderly particle electrode respectively to treat phenol wastewater, the treatment effect by the said two systems was compared with the variation of ·OH, H2O2, phenol and CODCr concentration during the degradation process investigated. The reaction kinetics of phenol degradation was discussed; besides, the mecha-nism of degradation was primarily studied by infrared spectroscopy also. The results showed that, under the con-dition that, the electrolyte dosage was 5 g/L, the voltage was 7 V, the pH value was 5, and the distance between plates was 4 cm, the removal rate of phenol by structured third electrode was 22.50% higher than that by disor-derly particle electrode, the phenol degradation reaction in the three dimension electrode reactor fit pseudo-first order kinetics model, the reaction rate constant was 0.014 min-1.