有機(jī)硅行業(yè)高濃度COD條件下含鋅廢水處理技術(shù)研究
[Abstract]:A large number of heavy metal wastewater containing high concentrations of organic compounds will be produced in the process of organic silicon production, which will have a significant impact on the ecological environment and human health if the wastewater with strong toxicity is not effectively treated. In this paper, the treatment of zinc-containing wastewater of high concentration organic matter produced by organic silicon production enterprises was studied. The methods of neutralization microfiltration, photocatalytic neutralization and microfiltration, electrocoagulation were compared respectively. The treatment effect of "electrocoagulation neutralization microfiltration" and "microfiltration electrocoagulation neutralization microfiltration" on wastewater was determined, and the optimum scheme and its parameters were determined. The experimental results show that: (1) under the condition of pH 10, the "neutralization microfiltration" method is used to treat wastewater. The COD of treated wastewater decreased from 2000 mg / L to 789 mg / L, and the removal rate was 60.55 mg / L from 40 mg / L to 0.624 mg / L, and the removal rate was 98.44 mg / L; (2) "ozone photocatalytic neutralization and microfiltration" wastewater, controlling initial pH 4, photocatalysis 2 h, ozone dosage 45 mg / min. After treatment, COD can be reduced from 2000 mg / L to 531 mg / L, the removal rate is 73.45 mg / L from 40 mg / L to 0.513 mg / L, and the removal rate is 98.72; (3) the current density is 7.0 Am ~ (2), the electrocoagulation time is 45 min, and the plate spacing is 2 cm 路L ~ (-1). After treatment, the COD of wastewater decreased from 2000mg / L to 454 mg / L, the removal rate was 77.30mg / L, the concentration of Zn2 decreased from 40 mg / L to 6.081mg / L, and the removal rate was 84.80%. (4) the electrocoagulation neutralization microfiltration method was used to treat wastewater. The COD of effluent was reduced from 2000mg / L to 342mg / L, the removal rate was 82.90% and the concentration of Zn2 was reduced from 40 mg / L to 0.162 mg / L, and the removal rate was 99.59; (5) the "microfiltration coagulation neutralization and microfiltration process" was used to treat wastewater. The effluent COD decreased from 2000 mg / L to 265 mg / L, the removal rate was 86.75 mg / L and the concentration of Zn2 decreased from 40 mg / L to 0.034 mg / L, and the removal rate was 99.91%. Through the comparison of the five wastewater treatment schemes mentioned above, although "neutralization microfiltration", "photocatalytic neutralization microfiltration", "electrocoagulation neutralization microfiltration", The concentration of Zn2 in effluent can be up to standard by "microfiltration coagulation and neutralization microfiltration", but the COD and Zn2 concentrations are still high after "neutralizing micro-filtration" and "photocatalytic neutralization microfiltration". The concentration of Zn2 treated by "electrocoagulation neutralization microfiltration" and "microfiltration coagulation neutralization microfiltration method" is much lower, and the removal rate of COD is more than 99.5%. For the complex and changeable wastewater, in order to ensure the lower concentration of Zn2 effluent, the best way to treat this kind of wastewater should be selected, which is "electrocoagulation neutralization microfiltration method" and "microfiltration coagulation neutralization microfiltration method".
【學(xué)位授予單位】:南昌航空大學(xué)
【學(xué)位級(jí)別】:碩士
【學(xué)位授予年份】:2016
【分類(lèi)號(hào)】:X783
【相似文獻(xiàn)】
相關(guān)期刊論文 前10條
1 王三反,王文琴,劉義安,王巖;電凝聚除氟條件的研究[J];水處理技術(shù);1990年04期
2 楊蘊(yùn)哲;胡筱敏;梁吉艷;;鋁陽(yáng)極電凝聚處理活性紅241動(dòng)力學(xué)分析[J];環(huán)境保護(hù)科學(xué);2007年06期
3 陳彬;李彥旭;朱又春;潘碧云;;脈沖電源電凝聚處理廚房廢水的研究[J];環(huán)境污染與防治;2008年01期
4 徐敏;葛建團(tuán);;復(fù)極式電凝聚-電氣浮方法處理洗衣廢水[J];廣東化工;2009年01期
5 劉云根;崔亞偉;王海峰;;電凝聚技術(shù)在水處理中的研究進(jìn)展[J];污染防治技術(shù);2009年02期
6 王孝武;朱又春;宋衛(wèi)鋒;林美強(qiáng);陳彬;;脈沖電源電凝聚處理廢水的研究[J];環(huán)境工程學(xué)報(bào);2009年10期
7 А.Д.斯米爾諾夫;陳世忠;;電凝聚凈化廢水法[J];環(huán)境污染治理譯文集;1980年03期
8 耿亮,余仁煥;赤鐵礦和石英電凝聚行為的研究[J];金屬礦山;2001年09期
9 甘莉,甘光奉;電凝聚水處理技術(shù)的新進(jìn)展[J];工業(yè)水處理;2002年05期
10 吳克明,潘留明,劉紅,馬麗娜;電凝聚處理高濃度乳化油廢水的研究[J];環(huán)境工程;2005年05期
相關(guān)博士學(xué)位論文 前2條
1 謝朝新;水長(zhǎng)期貯存對(duì)水質(zhì)的影響及超聲—電凝聚水處理技術(shù)研究[D];重慶大學(xué);2004年
2 張克強(qiáng);含硫化物(H_2S,S~(2-),HS~-)廢水電凝聚與生物處理的技術(shù)研究[D];天津大學(xué);2004年
相關(guān)碩士學(xué)位論文 前10條
1 劉龍;頁(yè)巖油廢水的預(yù)處理研究[D];東北大學(xué);2014年
2 劉軍平;有機(jī)硅行業(yè)高濃度COD條件下含鋅廢水處理技術(shù)研究[D];南昌航空大學(xué);2016年
3 張艷鳳;電凝聚氣浮技術(shù)處理氣田廢水的試驗(yàn)研究[D];長(zhǎng)安大學(xué);2008年
4 錢(qián)佳燕;超聲輔助電凝聚處理毒死蜱廢水研究[D];南京航空航天大學(xué);2012年
5 徐炳哲;電凝聚處理印染廢水的能耗影響因素及節(jié)能技術(shù)研究[D];東北大學(xué);2013年
6 涂文鋒;含油廢水處理的電凝聚氣浮技術(shù)研究[D];南昌大學(xué);2005年
7 李燕莉;電凝聚對(duì)微污染水中污染物的去除研究[D];武漢科技大學(xué);2004年
8 荊建鳴;預(yù)處理—脈沖電凝聚技術(shù)處理活性染料廢水研究[D];東南大學(xué);2006年
9 唐雷;電凝聚法對(duì)輕度污染水體的處理及殺菌消毒研究[D];武漢紡織大學(xué);2015年
10 朱茂森;混凝—電凝聚—超濾技術(shù)處理三次采油廢水[D];東北大學(xué);2008年
,本文編號(hào):2133832
本文鏈接:http://sikaile.net/kejilunwen/huanjinggongchenglunwen/2133832.html