Carrousel氧化沟工艺处理造纸中段废水

介绍Carrousel氧化沟系统处理某纸厂造纸中段废水设计与运行情况,以及存在问题与建议。     

UASB-生物接触氧化工艺处理鸡爪加工废水实例

鸡爪加工废水含油脂、悬浮物较高,是一种较难处理的有机废水。采用隔油-厌氧(UASB)-生物接触氧化-絮凝联合处理工艺处理鸡爪加工废水,结果表明:工艺是可行的,处理后出水可达标排放。     

纳米TiO2光电催化氧化法测定COD的影响因素

以纳米TiO2为光阳极,利用薄层微型反应器纳米TiO2光电催化氧化的方法测定COD,具有快速、准确、无二次污染的特点。研究了电解质类型、光源种类等对薄层微型反应器中光电催化测定COD的影响。研究结果表明：与NaNO,和KCl比较,NaH2PO4作电解质时的紫外光吸收低、电极表面氧化性能稳定,性能良好;与镓灯、碘镓灯比较,中压汞灯的紫外光谱丰富、辐射照度大,有利于TiO2光电催化反应的进行;通过热重分析,确定电极薄膜的烧结温度为520℃。     

醇酮废水硝酸氧化液分离己二酸的工艺研究

研究了从以醇酮废水为原料生产混合二元酸的硝酸氧化液中分离已二酸的工艺过程和操作条件,采用结晶-活性炭脱色-重结晶的方法,先由醇酮废水硝酸氧化液中结晶分离出粗己二酸,再对粗己二酸进行脱色、重结晶,干燥得到精己二酸。己二酸的结晶条件：结晶时间180min、结晶终温不低于35℃;粗己二酸活性炭脱色条件：脱色温度75℃、活性炭加入量为粗己二酸的8％、脱色时间90min。分离出的己二酸与混合二元酸的质量比为1：2,己二酸产品的纯度为99％以上、熔点151～152℃、Pt—Co色号小于50。     

絮凝-BC法-氧化絮凝工艺处理高浓度印钞废水试验

采用絮凝-BC法-氧化絮凝工艺对高浓度印钞废水的处理进行试验研究。结果表明,该工艺技术可行,处理后COD去除率达到99.9%,出水达到了国家规定的一级排放标准。     

饮用水中内分泌干扰物双酚A的臭氧氧化降解研究

采用臭氧氧化工艺对饮用水中内分泌干扰物双酚A特性进行了研究.研究表明:在原水浓度为1.0mg/L左右,臭氧总投加量为1.0、1.5和2.0mg/L条件下,30min BPA去除率可达70%、82%和90%.通过考察不同臭氧投加量、不同本底条件、不同BPA初始浓度和不同臭氧投加时间对BPA臭氧氧化的影响,分析得出臭氧投加量对BPA的降解占主导地位,而臭氧接触时间对去除效果的影响很小;采用紫外波长扫描确定在臭氧降解BPA的同时生成了在UV₂₅₄上有吸收的产物.通过考察臭氧氧化双酚A过程中UV₂₅₄的变化,提出低臭氧投加量下BPA不能完全被氧化,而采用缩短臭氧投加时间、加大臭氧投加量以及提高水中余臭氧浓度等方法,有利于水中BPA的完全降解.     

管流电氧化杀藻及其影响要素

对藻种类、电流密度、电极材料、细胞密度和流量对电化学氧化杀藻的影响进行了研究.实验结果显示,铜绿微囊藻比水华鱼腥藻对电化学氧化更为敏感,藻的种类和形状对杀藻效果存在影响.使用普通镀锌水管、铜水管和钛管作为阴极进行实验,发现阴极材料对结果影响不大,而阳极对杀藻效果影响较大,钌钛电极效果明显好于钛电极.电流密度对杀藻效果影响很大,电流密度为1mA.cm^-2时,杀藻效果不明显,当电流密度大于2.5mA.cm^-2时,杀藻效果开始非常显著.细胞密度是影响杀藻效果的重要因素,在5mA.cm^-2下,低密度(6×10⁸个/L)水样的光密度值下降明显比高密度(6×10⁹个/L)水样快.水样在反应器中的流量对结果影响不大.     

苯并(a)芘及其代谢产物的连续降解研究

在以驯化过的芽孢杆菌(BA-07)降解BaP的过程中,鉴定出2个BaP的未开环代谢产物顺式-4,5-二氢-4,5-二醇-BaP(cis-BP4,5-dihydrodiol)和顺式-7,8-二氢-7,8-二醇-BaP(cis-BP7,8-dihydrodiol).由于该产物对微生物有一定毒性,所以难于进一步降解.为提高BaP降解的同时,降低cis-BP4,5-dihydrodiol和cis-BP7,8-dihydrodiol的累积,对2种降解方法(即单纯用BA07降解和运用高锰酸钾与BA-07耦合的方法降解)进行了比较,并且优化了连续降解的参数.结果表明,①对BaP及其代谢产物的连续降解,化学氧化与微生物耦合(高锰酸钾与BA-07)的降解效果明显好于单纯利用微生物(细菌BA-07)的降解;②在同一时间取样,cis-BP4,5-dihydrodiol的残留率均高于cis-BP7,8-dihydrodiol;③当BaP的浓度为40μg/mL,培养基的最佳pH为7.0,以琥珀酸钠为共代谢底物,可以显著提高BaP降解率,降低cis-BP 4,5-dihydrodiol和cis-BP7,8-dihydrodiol的累积.同时提出了化学氧化与微生物协同的方法可以有效促进环境中持久有机污染物的连续降解.     

Effect of oxidation treatment on the adsorption and the stability of mercury on activated carbon

Oxidation treatment on the adsorption and the stability of Hg on activated carbon （AC） was inrestigated. Both MnO2-AC and FeCl3-AC were produced during oxidation treatment. The measurement of modified AC＇s mercury adsorption capacity was conducted in a simulated coal-fired flue gas by adsorbing test apparatus. TCLP and column leaching methods were used to test the stability of mercury adsorbed on ACs. The results indicate that the oxidation treatment changed the pore structure of the AC and modified the carbon surface by creating chemical components such as MnO4^-, Mn^4＋, O, NO^3-, Fe^3＋, Cl^-, etc. The Hg sorption capacity on MnO2-AC or FeCl3-AC was about three times higher than that of untreated carbon. In addition, the mercury control cost of each of the formers was about the half cost of the untreated carbon. The stability of Hg absorption was studied, it found that mercury adsorbed on the oxidation treated AC was not better than that of untreated carbon. It could concluded that the insoluble form of Hg is very important to the stability of mercury adsorbed on AC. This study suggests that the FeCl3-AC is the best absorbent for Hg with high adsorption capacity, better Hg adsorption stability in leaching environment, and lower cost among the three ACs tested.     

Decomposition kinetics of dimethyl methylphospate(chemical agent simulant) by supercritical water oxidation

Supercritical water oxidation （SCWO） has been drawing much attention due to effectively destroy a large variety of high-risk wastes resulting from munitions demilitarization and complex industrial chemical. An important design consideration in the development of supercritical water oxidation is the information of decomposition rate. In this paper, the decomposition rate of dimethyl methylphosphonate（DMMP）, which is similar to the nerve agent VX and GB（Sarin） in its structure, was investigated under SCWO conditions. The experiments were performed in an isothermal tubular reactor with a H2O2 as an oxidant. The reaction temperatures were ranged from 398 to 633℃ at a fixed pressure of 24 MPa. The conversion of DMMP was monitored by analyzing total organic carbon （TOC） on the liquid effluent samples. It is found that the oxidative decomposition of DMMP proceeded rapidly and a high TOC decomposition up to 99.99% was obtained within 11 s at 555℃. On the basis of data derived from experiments, a global kinetic equation for the decomposition of DMMP was developed. The model predictions agreed well with the experimental data.