首页 | 本学科首页   官方微博 | 高级检索  
相似文献
 共查询到20条相似文献,搜索用时 156 毫秒
1.
针对油田采出废水的特点,以粘胶基活性炭纤维为原料,经二次炭化和二次活化方式处理制得ACF样品。以ACF为过滤材料,对延长某采油厂经过沉降、分离处理后的采油废水进行动态吸附实验,实验结果表明:经水蒸汽二次活化得到的ACF样品对选用的油田废水处理效果最佳,其悬浮物颗粒粒径中值0.496μm(<1.0μm)、悬浮物含量为0.77mg/L(<1.0mg/L)。  相似文献   

2.
对污水中悬浮物分析方法进行了实验研究。采用微孔膜过滤重量法、紫外可见分光光度法和激光粒度分析仪三种测试方法,对稠油污水各处理单元的出水悬浮物进行了对比分析。实验结果表明:微膜过滤重量法的影响因素为膜的溶解损失、烘干温度、烘干时间和冷却时间;紫外可见分光光度法的影响因素为搅拌强度、搅拌时间和温度。在测定沉降、浮选工艺出水中悬浮物含量时,采用重量法更准确、更有效。  相似文献   

3.
采用已知孔径的微孔过滤器,对油田采出水的过滤进水进行了筛分,分析了悬浮物的质量浓度,并同步测定了颗粒体积浓度和几何特征值。除了D[v,0.5]具有指标性意义外,粒度分析结果并不能完全代表过滤等工艺的分离精度。悬浮物几何特征值、体积浓度和质量含量降低率不是同步的,其中质量浓度降低幅度最小。当粒径小于4μm的悬浮物质含量超过3mg/L时,难以被目前普遍采用的过滤工艺去除。应选择与膜过滤类似的更精密的工艺技术,才能最终达到采出水回用标准。  相似文献   

4.
油田压裂废液处理及回注实验   总被引:1,自引:1,他引:0  
油田压裂废液具有高COD、高悬浮物等特点,处理达标难度大。以悬浮固体含量、悬浮固体颗粒粒径中值和含油量为指标,实验研究了混凝、微滤膜过滤技术参数,最佳条件为:絮凝剂投加量800~1 000mg/L,助凝剂投加量9~10mg/L,快速搅拌G值250~300s--1,慢速搅拌G值约50s--1,经50、10μm两级微滤膜过滤后悬浮固体含量、粒径中值、含油量满足SY/T 5329-2012《碎屑岩油藏注水水质指标及分析方法》标准要求。该方法工艺简单,成本低,在一定程度上解决了压裂废液难处理的问题。  相似文献   

5.
油田注水系统中悬浮物的含量和粒径中值是注水水质严格控制的两项指标。库尔特颗粒计数仪(MS3)采用最新的数字脉冲测量技术可测定水中的颗粒总数和粒径中值。文章主要论述了MS3的工作原理、功能参数。通过实验说明MS3在注水水质控制指标中的应用,以及通过测定水样的粒径分布和颗粒总数的变化情况掌握污水处理单元的处理效果,以利于更好的控制注水水质。  相似文献   

6.
高浓度ABS树脂生产污水治理技术   总被引:4,自引:0,他引:4  
ABS树脂生产装置中的污水处理一直是影响化工装置环保的一大难题。一方面,其废水水质差,悬浮物含量高,且多为细微颗粒,难以从水中分离,进入生化系统也难以去除;另一方面,污水中溶解性胶乳较多、粘性大,且为间歇式排放,对污水处理系统冲击较大。大庆石化总厂采取完善生产工艺操作过程、采用高效净水剂、对处理设备进行改进及对生产全过程进行污染控制等措施,并分阶段、分单元、分步骤地对污染源进行处理。采取这些措施后使ABS树脂生产中的废水得到了有效治理,处理后的ABS污水中CODcr含量在1000mg/L以下,悬浮物含量在500mg/L以下,石油类物质含量在30mg/L以下。处理装置的能耗、物耗也大幅度降低。  相似文献   

7.
文章以风城油田稀油污水处理为例,分析污水处理系统中悬浮物的形成机理,并对污水含油、悬浮物、固体含量、粒径中值、聚合物含量、细菌、温度、硫化物、二价铁、pH值等水质指标进行分析,找出影响污水处理的主要因素,并对油水悬浮物处理方法进行室内分析及现场物理、化学方法实践,解决污水处理系统中悬浮物问题。  相似文献   

8.
本文介绍了油田注水中悬浮颗粒粒径的常用检测方法——可见光显微镜法及计数器法。讨论了悬浮颗粒粒径指标的几种表示方法,即颗粒数百分数法、绝对粒子数量法及体积百分数法以及在制定注水中悬浮颗粒粒径指标时应考虑的几个问题。  相似文献   

9.
便携式COD快速测定仪专用氧化剂是影响测定COD准确度的关键,其中重铬酸钾含量对实验过程中的氧化效率有较大影响,含量太低时,氧化过程不充分导致测定结果偏低;含量过高,造成样品颜色被氧化剂自身色度掩盖,使得反应后吸光度值变化不明显,测定COD浓度较低的水样时吸光度值误差较大。通过正交实验对COD专用氧化剂进行配方改进,优化筛选出的COD专用氧化剂应用于现场实时监测,测定的COD准确度达到实验室要求。  相似文献   

10.
以磁铁矿滤料和石英砂滤料为填设滤料层的级配模式,一直被广泛应用于油田含聚污水处理过程,但目前这种滤料级配对过滤性能的影响及规律认识较为缺乏。文章从悬浮粒子(包含悬浮固体颗粒和油滴)吸附与截留形成的聚集特征切入,定量分析出水水质特性,对含聚污水过滤过程中滤料级配的影响效果展开数值模拟研究。研究表明:磁铁矿滤料层厚度较大的级配模式过滤,对悬浮粒子具有更好的吸附与截留效果,对小粒径悬浮粒子的截留能力更优,但滤料填充高度比与过滤效果存在一定适配性;以填充高度比1.28以上磁铁矿滤料厚度较大的级配模式过滤较低含聚浓度的污水,及以填充高度比1.67以上磁铁矿滤料厚度较小的级配模式过滤较高含聚浓度的污水,均可以实现出水悬浮固体颗粒和油滴含量低于或约等于5 mg/L,满足大庆油田含聚污水二级过滤出水回注水质指标要求。  相似文献   

11.
The milking process on dairy farms produces wastewaters, known as dairy soiled waters (DSW), which contain variable concentrations of nutrients. The most common method of disposal is by application to land. However, this practise can result in the pollution of nearby receiving water bodies. A laboratory study, comprising two sets of 0.5?m, 1?m and 1.5?m-deep filters loaded at two loading rates, examined the performance of woodchip filters in treating DSW. The filters comprised de-barked Sitka spruce (Picea sitchensis) woodchips. Dried DSW was reconstituted to 1% and 3% suspended solids (SS) concentrations and was applied at 28?L/m(2).d to the surface of the filters at loading rates of 280?g?SS/m(2).d and 840?g?SS/m(2).d, respectively. Filters were loaded for a maximum of 277 days. The filters achieved substantial decreases in SS (>99%), chemical oxygen demand (COD) (>97%) and total nitrogen (TN) (>89%). The dominant treatment mechanism appears to be physical filtration, but sorption and biological uptake likely also play a role. As the filters are aerobic, mineralisation and nitrification occur, but gaseous N losses are probably not significant. Woodchip shows potential as a filter medium for treating DSW, significantly decreasing the concentrations of SS, COD and TN.  相似文献   

12.
The application of hypochlorite for the removal of soluble COD, phenolic and polyphenolic like compounds, and other organic compounds responsible for the olive mill wastewater (OOWW) colour has been experimentally studied. After the OOWW filtration on a sand column, the effluent was subjected to a fast liming under optimal conditions. Lime application reduced polyphenols, COD and SS contents to half of their initial values but an important blackening of the treated OOWW was observed, especially when adding high concentrations of lime (10% (W/V) and 15% (W/V)).A second stage of treatment was applied using calcium hypochlorite. In this stage, removal of the studied compounds reached as much as 95% at higher concentrations, and particularly the colouring of OOWW which is generally difficult to eliminate was greatly reduced. The OOWW hypochloration acted through coagulation–flocculation and a rapid oxidation of the organic matter proceeded from the first 5 min. The kinetic study of the degradation of the waste polluting compounds from liming showed that Ca(ClO)2 reacts similarly in the elimination of organic compounds, polyphenols, SS and colouration. The analysis of the organochloride compounds generated by the reaction between hypochlorite and the organic compounds showed that DDD, DDT and the heptachlor contents exceeded the values recommended by the International and European drinking water standards.  相似文献   

13.
介绍了天津市某城镇污水处理厂NPR工艺的特点及运行状况。通过对污水厂的运行监测数据分析,研究了该工艺在低温条件下处理城镇生活污水时的脱氮除磷效果。结果表明:NPR工艺具有一定的优异性,它能在降低能耗的前提下使系统COD和SS的去除率进一步降低,出水能达到中水回用标准,有利于污水的再生利用;低温影响NPR系统的硝化及反硝化率,低温下有机物的去除更易受到有机负荷的影响;温度对生物去除SS,COD和TP的效果影响不大,对NH3-N及TN的去除效果影响比较明显。低温下污水处理厂COD、SS、NH3-N、TN、TP的平均去除率分别为72.1%、94.9%、67.5%、55.1%、66.5%。  相似文献   

14.
中空纤维膜生物反应器处理炼厂浮选池出水试验研究   总被引:2,自引:0,他引:2  
研究设计的膜生物反应器处理炼厂浮选池出水,在每天进水容积负荷1.0 kg COD/m3,进水COD浓度600 mg/L,MLSS为900~5500 mg/L的条件下,无论活性污泥表现正常还是膨胀,过滤出水中COD均稳定地小于90 mg/L,处理效果好于目前炼油厂的合建式曝气池(容积负荷为0.5 kg COD/m3左右,出水COD100 mg/L左右)。试验运行期间,膜通量最高可达到42 L/m2·h。该工艺的技术关键是采用特殊流态来降低膜堵塞的膜生物反应器和优良质量的膜。  相似文献   

15.
一种高效复合絮凝剂对多种废水的处理效果   总被引:1,自引:0,他引:1  
用聚合氯化铝(PAC)和聚丙烯酰胺(PAM)复配成复合絮凝剂(PAC+PAM)应用于污染河水、生活污水、工业废水和餐饮废水等6种废水的处理,结果表明。PAC、PAM、PAC+PAM对污染河水的CODc。SS、浊度有显著降低作用,PAC+PAM的净水效果明显优于PAC和PAM;PAC+PAM对6种废水中COD的去除率为81.5%~90.4%,平均84.6%。对SS的去除率为81.9%~96.5%,平均88.9%,对浊度的去除率为91.3%-98.0%,平均95.1%;处理后悬浮物基本被絮凝沉降,水体变得较清澈透明,异味或臭味消除。说明本PAC+PAM复合絮凝剂对各种废水均有良好的净水效果,具有重要的应用价值。  相似文献   

16.
Contamination of freshwater by estrogens from manure applied to agricultural land is of grave concern because of the potentially harmful effects on aquatic life and human health. Recent developments in liquid manure (slurry) management include partial removal of particulate slurry dry matter (PSDM) by separation technologies, which may also remove parts of the estrogens and enhance infiltration of the slurry on field application and hence the interaction between estrogens and the soil matrix. This study investigated how 17β-estradiol (E2), a natural estrogen commonly found in pig manure, sorbs to agricultural soils, to different size fractions of pig slurry separates, and to soils amended with each size fraction to simulate conditions in the soil-slurry environment. A crude fiber fraction (SS1) was prepared by sieving (<500 μm) the solids removed by an on-farm separation process. Three other size fractions (SS2 > SS3 > SS4) were prepared from the liquid fraction of the separated slurry by sedimentation and centrifugation. Sorption experiments were conducted in 0.01 mol L(-1) CaCl(2) and in natural pig urine matrix. Sorption in 0.01 mol L(-1) CaCl(2) was higher than that in pig urine for all solids used. Sorption of E2 to soil increased with its organic carbon content for both liquid phases. The solid-liquid partition coefficients of slurry separates were 10 to 30 times higher than those of soils, but the organoic carbon normalized partition coefficient values, reflecting sorption per unit organic carbon, were lower for slurry separates. Mixing slurry separates with soil increased the sorption of E2 to the solid phase significantly in the order: SS1 < SS3 < SS2 for both liquid phases. In contrast, SS4 reduced the sorption of E2 to the solid phase by increasing the sorption to suspended or dissolved organic matter. The study suggested that potentially 50 to 75% of E2 in slurry can be removed from the liquid fraction of slurry by physical separation.  相似文献   

17.
研究了新型混凝剂BMT对城市污水进行强化混凝处理的效果,并与常用混凝剂聚合氯化铝(PAC)进行了比较。结果表明,在城市污水原水COD低于500mg/L和最佳工况下,经BMT处理后的出水能够达到《城镇污水处理厂污染物排放标准》(GB18918-2002)二级标准,并具备替代PAC的能力。  相似文献   

18.
炼油化工废水处理的传统处理工艺中存在一定的弊端。为此,玉门炼油化工总厂对其废水处理设施进行了改建和扩建,其生物处理系统采用了序批式活性污泥法处理工艺。经过 3年运行的结果表明:该系统运行效果良好,处理后的水质可达到《GB8978-1996》(石化)一级排放标准的要求;化学需氧量(COD)和生化需氧量(BOD)分别降低78.6%和91.2%,硫化物去除率为98.2%,挥发酚去除率为99.6%。而且该反应器具有较强的耐冲击负荷能力,进水中COD在600 mg/L以下且有大幅度波动时,该系统仍可稳定地运行,处理后的水可达标排放。  相似文献   

19.
A significant improvement in river water quality cannot be expected unless nonpoint-source contaminants are treated in addition to the further treatment of point-source contaminants. If river water is sprayed over a floodplain, the consequent water filtration through the sediment profile can simultaneously remove organic matter and nitrogen in the water through aerobic and denitrifying reactions. This hypothesis was tested using lysimeters constructed from polyvinyl chloride (PVC) pipe (150 cm long, 15 cm in diameter) packed with loamy sand floodplain sediment. Water was applied to the top of the lysimeters at three different flow rates (48, 54, and 68 mm d(-1)). Concentrations of NO3 and dissolved oxygen (DO), chemical oxygen demand (COD), and redox potential (Eh) in the water were measured as functions of depth after the system reached steady states for both water flow and reactions. At the rate of 68.0 mm d(-1), a reducing condition for denitrification developed below the 5-cm depth due to the depletion of O2 by organic matter degradation in the surface oxidizing layer; Eh and DO were below 205 mV and 0.4 mg L(-1), respectively. At a depth of 70 cm, COD and NO3-N concentration decreased to 5.2 and 3.8 mg L(-1) from the respective influent concentrations of 17.1 and 6.2 mg L(-1). Most biodegradable organic matter was removed during flow and further removal of NO3 was limited by the lack of an electron donor (i.e., organic matter). These results indicate that the floodplain filtration technique has great promise for treatment of contaminated river water.  相似文献   

20.
采用陶粒、沸石、活性炭填料合理组合作为曝气生物滤池的填料对高校生活污水进行处理。研究了组合填料生物滤池生物膜的培养,不同水力负荷、容积负荷和气水比对污水处理效率的影响,以及该生物滤池对生活污水的处理效果。结果表明,采用组合填料生物滤池,接种挂膜培养周期为25d,在水力负荷为2.5m3/(m2·h),气水比3.5:1,组合填料生物滤池出水COD、BOD5、SS、NH3-N和色度平均值达到《城市污水再生利用城市杂用水水质》GB/T18920—2002水质要求。  相似文献   

设为首页 | 免责声明 | 关于勤云 | 加入收藏

Copyright©北京勤云科技发展有限公司  京ICP备09084417号