排序方式: 共有47条查询结果,搜索用时 15 毫秒
11.
MBR-RO组合工艺污水回收中试研究 总被引:6,自引:0,他引:6
以A2/O-MBR为预处理工艺,构建了MBR-RO组合系统并用于城市污水的直接处理与回收,考察了MBR工艺作为RO预处理的可行性,评价了RO膜的出水水质,分析了不同操作条件对RO膜的渗透性能及膜污染的影响.研究表明,RO出水平均值为TOC<1.3 mg/L、NH 4-N<0.03 mg/L、TN<0.1 mg/L,TP未检出,电导率和浊度分别小于30μS/cm和0.12 NTU,MBR出水中的无机离子已被RO完全截留,MBR-RO系统具有很高的污染物降解能力和脱盐能力,其出水水质可达饮用水水质标准.MBR作为RO的预处理是完全可行的,连续6个多月的运行中RO膜污染表现不严重. 相似文献
12.
渤海海水淡化反渗透法的预处理工艺 总被引:14,自引:0,他引:14
采用“消毒-混凝-澄清一砂滤”、“消毒-混凝-澄清-砂滤-超滤”以及“消毒-砂滤-超滤”三套海水淡化预处理工艺进行了试验对比。试验的目的在于获取可行的反渗透预处理工艺。表明,采用“消毒-混凝-澄清-砂滤-超滤”工艺或“消毒-砂滤-超滤”工艺是技术可行的反渗透预处理工艺,其中次氯酸钠为可选消毒剂,三氯化铁为较好的混凝剂,而超滤是不可或缺的单元处理工艺。 相似文献
13.
采用混凝-Fenton组合工艺对漳州九龙岭垃圾填埋场的渗滤液经NF+RO处理后膜滤浓缩液进行中试试验,探讨了PAC、PAM、FeSO4·7H2 O和H2 O2的投加量对处理效果的影响及反应机理,并设计各工艺单元参数.结果表明:混凝工艺药剂最佳投加量为PAC 2000 mg/L、PAM 9 mg/L;Fenton工艺的氧化剂最佳投加量为FeSO4·7H2 O 1.6 g/L、H2 O28 mL/L.膜滤浓缩液经处理后,出水COD约300 mg/L,色度约30,平均去除率分别达76.8%和95.4%,处理费35.52元/t,试验结果为同类膜滤浓缩液提供了经济可行的处理方法和工艺设计依据. 相似文献
14.
污水污灌一直是灌区农业灌溉的一种重要形式,但由于系统接纳污水的成分复杂,也常常带来灌溉风险。主要针对污灌水体中的硫离子给水稻带来的危害,提出利用光敏剂快速除硫的可能性。土柱实验发现,光敏剂在土壤中的吸附符合Langmuir等温式Qeq=3.81Ce/(1+1.293Ce),当其加入量为10μmol/L,光照强度为3000lx时,S2-的去除率为87.5%;光照强度为2000lx时,S2-的去除率为78.1%,而完成该过程仅需要30min,并且光敏剂也不会给环境带来二次污染。 相似文献
15.
ZHANG Yejian YAN Li QIAO Xiangli CHI Lin NIU Xiangjun MEI Zhijian ZHANG Zhenjia 《环境科学学报(英文版)》2008,20(5):558-564
Palm oil industry is the most important agro-industry in Malaysia, but its by-product–palm oil mill e uent (POME), posed a great
threat to water environment. In the past decades, several treatment and disposal methods have been proposed and investigated to
solve this problem. A two-stage pilot-scale plant was designed and constructed for POME treatment. Anaerobic digestion and aerobic
biodegradation constituted the first biological stage, while ultrafiltration (UF) and reverse osmosis (RO) membrane units were combined
as the second membrane separation stage. In the anaerobic expanded granular sludge bed (EGSB) reactor, about 43% organic matter
in POME was converted into biogas, and COD reduction e ciency reached 93% and 22% in EGSB and the following aerobic reactor,
respectively.With the treatment in the first biological stage, suspended solids and oil also decreased to a low degree. All these alleviated
the membrane fouling and prolonged the membrane life. In the membrane process unit, almost all the suspended solids were captured
by UF membranes, while RO membrane excluded most of the dissolved solids or inorganic salts from RO permeate. After the whole
treatment processes, organic matter in POME expressed by BOD and COD was removed almost thoroughly. Suspended solids and
color were not detectable in RO permeate any more, and mineral elements only existed in trace amount (except for K and Na). The
high-quality e uent was crystal clear and could be used as the boiler feed water. 相似文献
16.
17.
为了实现微藻培养基的低成本化和废水资源化利用多重目的的耦合,对反渗透浓缩液(RO浓水)作为培养基培养小球藻(Chlorella sp.)的可行性及其影响因素进行了探讨。实验取一级、二级处理出水和消化反应上清液及3种废水与RO浓水混合液制成6种培养基培养小球藻,探究最佳培养基;在此基础上探究浓度与温度对小球藻生长的影响。结果表明,培养15 d后,3种添加了RO浓水的培养基比3种纯废水培养基更有利于小球藻的生长,其中消化反应上清液-RO浓水混合液是最佳培养基;浓水浓度0%~90%的该混合液中小球藻生物量增加315%~780%,且小球藻的生物量表现为随RO浓水浓度的增大先增加后减小的变化趋势,30%是小球藻最佳培养浓度;在10、20和30℃下,浓度0%~90%的培养基中小球藻生物量增加了140%~570%,各浓度中的小球藻均在20℃下生长最好。 相似文献
18.
This study explored the removal of five veterinary pharmaceuticals (VPs) (sulfamethoxazole (SMETOX), trimethoprim (TMP),
ciprofloxacin (CIPRO), dexamethasone (DEXA) and febantel (FEBA)) from different water matrices (Milli-Q water, model water, tap
water and real pharmaceutical wastewater using four types of nanofiltration (NF) membranes (NF90, NF270, NF and HL) and two
reverse osmosis (RO) membranes (LFC-1 and XLE). All VPs were added to different water matrices at a concentration of 10 mg/L.
Rejections of VPs and water flux were measured. The rejection increased with increase of molecular weight. The highest rejections
were obtained with RO membranes (LFC-1, XLE) and tight NF (NF90) membrane. In general, the rejection of VPs was higher in
model water and tap water than in Milli-Q water, but the water flux was lower. This was mainly explained by ion adsorption inside the
membranes pores. Narrower pore size counteracted the effect of presence of low concentration of natural organic matter (NOM) in tap
water. The NOM was assumed to enhance the adsorption of VPs onto membrane surface, increased the size exclusion and electrostatic
repulsion also appeared during the transport. Investigated water matrices had influence on water flux decline due to their complexity. 相似文献
19.
以花生壳活性炭对RO浓水进行吸附处理,利用傅立叶红外光谱(FTIR)和荧光光谱(EEM)研究花生壳活性炭对不同pH的RO浓水的吸附特性.结果表明,花生壳活性炭对溶解性有机碳(DOC)的吸附遵循准二级吸附动力学方程,特别是碱性条件下,DOC的吸附量随着pH的升高而降低.而且pH越高,达到吸附平衡的时间越长.通过FTIR光谱分析发现,活性炭的芳香结构吸收峰在吸附后红移至1630 cm-1,表明被吸附的有机物在该处有明显的特征吸收峰,而C—O和O—H官能团的吸收峰则因为钙离子等物质的吸附而显著降低.由EEM光谱分析可知,RO浓水的荧光物质主要由腐殖酸类腐殖质和富里酸类腐殖质组成,其荧光强度与DOC之间具有较好的线性相关性. 相似文献
20.
ZHANG Yejian YAN Li QIAO Xiangli CHI Lina NIU Xiangjun MEI Zhijian ZHANG Zhenjia 《环境科学学报(英文版)》2008,20(5)
Palm oil industry is the most important agro-industry in Malaysia, but its by-product-palm oil mill effluent (POME), posed a great threat to water environment. In the past decades, several treatment and disposal methods have been proposed and investigated to solve this problem. A two-stage pilot-scale plant was designed and constructed for POME treatment. Anaerobic digestion and aerobic biodegradation constituted the first biological stage, while ultrafiltration (UF) and reverse osmosis (RO) membrane units were combined as the second membrane separation stage. In the anaerobic expanded granular sludge bed (EGSB) reactor, about 43% organic matter in POME was converted into biogas, and COD reduction efficiency reached 93% and 22% in EGSB and the following aerobic reactor, respectively. With the treatment in the first biological stage, suspended solids and oil also decreased to a low degree. All these alleviated the membrane fouling and prolonged the membrane life. In the membrane process unit, almost all the suspended solids were captured by UF membranes, while RO membrane excluded most of the dissolved solids or inorganic salts from RO permeate. After the whole treatment processes, organic matter in POME expressed by BOD and COD was removed almost thoroughly. Suspended solids and color were not detectable in RO permeate any more, and mineral elements only existed in trace amount (except for K and Na). The high-quality effluent was crystal clear and could be used as the boiler feed water. 相似文献