1) iron-carbon aeration microelectrolysis
铁炭曝气微电解
1.
The pretreatment of cellulose zymolytic wastewater with iron-carbon aeration microelectrolysis method was researched by orthogonal experiment.
采用正交实验法对铁炭曝气微电解预处理纤维素发酵废水进行了研究,最佳工艺条件为pH4—5,铁屑用量150g·l-1,铁炭比1∶2,反应时间1h,曝气量30ml·min-1。
2) aerate ferric-carbon micro-electrolysis
曝气铁炭微电解
1.
The results indicated that process of aerate ferric-carbon micro-electrolysis method and hydrolysis acidification and aerobic biological treatment and ozone oxidization were effective and practical for fluorescent whitening agent wastewater,by which when the COD concentration of the influent was about 5 620 mg·L-1,the TOC lowered 68.
采用"曝气铁炭微电解-水解酸化-好氧生物处理-臭氧氧化"工艺对荧光增白剂生产废水进行了处理。
3) aerated and catalyzed ferric-carbon micro-electrolysis
曝气催化铁炭微电解工艺
1.
The technique of aerated and catalyzed ferric-carbon micro-electrolysis which treated tetrahydrofuran wastewater were studied.
结果表明,普通铁炭微电解工艺的处理效果与Fe/C质量比、pH值、反应时间等因素有关;采用曝气催化铁炭微电解工艺预处理四氢呋喃废水,在反应时间为120 m in、进水COD为10 000 mg/L左右、pH<4时,对COD的去除率>70%,较普通铁炭微电解工艺有明显的提高,且不易发生板结。
4) Fe-C aeration
铁炭曝气
1.
The air flotation/Fe-C aeration/Fenton oxidation/UASB/bio-contact oxidation process was used to treat the high-concentration petrochemical wastewater.
采用气浮/铁炭曝气/芬顿氧化/UASB/生物接触氧化工艺处理高浓度石化废水,介绍了系统的启动与运行情况。
5) Aerated micro-electrolysis
曝气微电解
1.
Pretreatment of pyrimidine wastewater by aerated micro-electrolysis and flocculation technique;
曝气微电解-絮凝工艺预处理嘧啶废水
2.
The results show that the optimal pH value for removing strong organic solvents by aerated micro-electrolysis and catalytic electro-oxidation technology are 2 to 3 and 5 to 6 respectively,and the optimal hydraulic retention times(HRT) are 120 min and 90 to 120 min respectively.
结果表明,曝气微电解和催化电氧化技术去除强有机溶剂的最佳pH值分别为(2~3)、(5~6),最佳水力停留时间分别为120、(90~120)m in;高级氧化技术可大大提高废水的可生化性,将B/C值从0。
6) micro-electrolysis
铁炭微电解
1.
Pulp and paper effluent tertiary treatment by micro-electrolysis technology;
铁炭微电解法深度处理制浆造纸废水的研究
补充资料：微气泡曝气
分子式：
CAS号：
性质：气泡曝气方法之一。活性污泥法废水生物处理过程中，在曝气池底部或邻近底部设置多孔陶质扩散器进行曝气，扩散器上微孔孔径约为50μm，可产生直径0.2～0.3mm的微小气泡。操作时，输入的空气需先经过滤，以防扩散器发生堵塞。由于产生微气泡的扩散器浸没深度较大，而且扩散器微孔阻力增加，因此，所需鼓风压力较大。其充氧效率一般为10％～30％。
CAS号：
性质：气泡曝气方法之一。活性污泥法废水生物处理过程中，在曝气池底部或邻近底部设置多孔陶质扩散器进行曝气，扩散器上微孔孔径约为50μm，可产生直径0.2～0.3mm的微小气泡。操作时，输入的空气需先经过滤，以防扩散器发生堵塞。由于产生微气泡的扩散器浸没深度较大，而且扩散器微孔阻力增加，因此，所需鼓风压力较大。其充氧效率一般为10％～30％。
说明：补充资料仅用于学习参考，请勿用于其它任何用途。
参考词条