陕西科技大学学报(自然科学版)
陝西科技大學學報(自然科學版)
협서과기대학학보(자연과학판)
JOURNAL OF SHAANXI UNIVERSITY OF SCIENCE & TECHNOLOGY
2014年
2期
20-25
,共6页
孙根行%路建萍%孙绪博%郝新宇%白琴%谢萍
孫根行%路建萍%孫緒博%郝新宇%白琴%謝萍
손근행%로건평%손서박%학신우%백금%사평
炼油厂“三泥”%酸化氧化%调理及离心%脱水%污泥离心上清液
煉油廠“三泥”%痠化氧化%調理及離心%脫水%汙泥離心上清液
련유엄“삼니”%산화양화%조리급리심%탈수%오니리심상청액
refinery sludge%acidification and oxidation%thermal refining and centrifugation%dehydration%sludge centrifugal supernatant
对西北某炼油厂废水处理系统的“三泥”样品,采用酸化氧化及调理的污泥脱水工艺进行优化研究,获得了良好的污泥脱水效果,为污泥减量化技术改造提供依据.结果表明,当反应pH=4、H2 O2投加量为2.0 g/L、m(H2 O2)∶ m(Fe2+)=4∶1、反应温度为35℃、反应时间为60 min、CaO投加量为7.0 g/L、离心转速为3000 r/min ,离心时间5 min时,得到的泥饼含水率为70%~73%、石油类含量<2%;同时,测得调理后污泥比阻(SRF)在0.3×108 s2/g左右.在一定范围内,“三泥”离心上清液中的SS、COD、石油类含量,以及浊度等,随着H2 O2投加量的增加而降低.
對西北某煉油廠廢水處理繫統的“三泥”樣品,採用痠化氧化及調理的汙泥脫水工藝進行優化研究,穫得瞭良好的汙泥脫水效果,為汙泥減量化技術改造提供依據.結果錶明,噹反應pH=4、H2 O2投加量為2.0 g/L、m(H2 O2)∶ m(Fe2+)=4∶1、反應溫度為35℃、反應時間為60 min、CaO投加量為7.0 g/L、離心轉速為3000 r/min ,離心時間5 min時,得到的泥餅含水率為70%~73%、石油類含量<2%;同時,測得調理後汙泥比阻(SRF)在0.3×108 s2/g左右.在一定範圍內,“三泥”離心上清液中的SS、COD、石油類含量,以及濁度等,隨著H2 O2投加量的增加而降低.
대서북모련유엄폐수처리계통적“삼니”양품,채용산화양화급조리적오니탈수공예진행우화연구,획득료량호적오니탈수효과,위오니감양화기술개조제공의거.결과표명,당반응pH=4、H2 O2투가량위2.0 g/L、m(H2 O2)∶ m(Fe2+)=4∶1、반응온도위35℃、반응시간위60 min、CaO투가량위7.0 g/L、리심전속위3000 r/min ,리심시간5 min시,득도적니병함수솔위70%~73%、석유류함량<2%;동시,측득조리후오니비조(SRF)재0.3×108 s2/g좌우.재일정범위내,“삼니”리심상청액중적SS、COD、석유류함량,이급탁도등,수착H2 O2투가량적증가이강저.
In this paper ,using oil refining sludge of wastewater treatment system from a refin-ery in the northwest as the sample ,the sludge dehydration process of acidification oxidation and thermal refining is put forward .It obtains good effect of sludge dewatering and provides the basis for reform of sludge reduction technology .The results show that moisture and oil content of the mud cake are respectively 70% ~73% and under 2% ,w hen pH is to 4 ,reac-tion temperature is 35 ℃ , the dosing quantity of H2 O2 is 2 .0 g/L ,the best value of m (H2 O2 )∶m(Fe2+ ) is 4∶1 ,reaction time is 60 min ,the dosing quantity of CaO is 7 .0 g/L , centrifugal speed is 3 000 r/min and centrifugal time is 5 min .After centrifugation ,at the same time ,specific resistance to filtration (SRF )is around 0 .3 × 108 s2/g .Within a certain range ,the content of SS ,COD ,oil and turbidity are decreased with the increase of the dosing quantity of H2 O2 .