海上油基钻屑电磁热脱附参数优化及应用评价

选取某三级海域A平台钻井过程中离心机出口的油基钻屑开展电磁热脱附实验,分析实验过程中脱附温度、脱附时间对钻屑干渣含油量的影响规律,在此基础上优化设备运行参数:脱附温度300℃,脱附时间40 min,在此条件下,干渣含油量可达到0.84%。根据参数优化结果对现场应用进行指导,结果表明:一次性进料1 t,实际脱附温度300～320℃,脱附时间40 min,实际干渣含油量1.30%～1.70%;A平台电磁热脱附设备运行86 d,共处理油基钻屑1 116.40 t,平均处理量12.98 t/d,最大处理量21.70 t/d;油基钻屑在海上平台进行热脱附处理,实现了无害化处理,资源化利用,经济效益最大化。为提高设备处理能力,建议提高设备稳定性和增加预加热模块,为确保处理后尾气连续达标排放,建议增加尾气实时检测系统。     

基于常规处理的微污染水源水处理工艺改进措施简

我国大部分给水处理厂主要采用混凝-沉淀-过滤-消毒的常规处理工艺,该工艺对有机物、氨氮等去除效果有限,同时存在消毒副产物残留等问题。根据我国经济发展现状,分析了常规处理工艺的改进措施,包括对常规工艺进行强化,在常规处理工艺之前增加预吸附和预氧化,在常规处理工艺之后增加臭氧-生物活性炭吸附、膜处理等。这些措施在保留原处理工艺的基础上,通过调整操作条件或增加处理设施来改善出水水质,具有投资少、见效快的特点。     

基于常规处理的微污染水源水处理工艺改进措施

我国大部分给水处理厂主要采用混凝-沉淀-过滤-消毒的常规处理工艺,该工艺对有机物、氨氮等去除效果有限,同时存在消毒副产物残留等问题。根据我国经济发展现状,分析了常规处理工艺的改进措施,包括对常规工艺进行强化,在常规处理工艺之前增加预吸附和预氧化,在常规处理工艺之后增加臭氧-生物活性炭吸附、膜处理等。这些措施在保留原处理工艺的基础上,通过调整操作条件或增加处理设施来改善出水水质,具有投资少、见效快的特点。     

焦化废水脱酚的工艺研究

为脱除焦化废水中的酚，本文研究了新型化学破乳法液膜脱酚的工艺，确定了搅拌塔操作条件，并实际应用于焦化厂含酚废水的处理中，结果表明该工艺具有良好的脱酚效果。     

一种适用于低碳(超低碳)高浓度含氮废水生物脱氮工艺的探讨

传统的生物脱氮工艺对于低（超低）COD／NH4^ 条件下废水的脱氮效果很差，甚至没有脱氮效果，因为传统的生物脱氮工艺在反硝化过程中需要大量的电子供体。亚硝酸型硝化和厌氧氨氧化有机结合构成新型的生物脱氮工艺，为低碳（超低碳）高浓度含氮废水提供他一种崭新的生物脱氮工艺。但其间的反应机理，控制条件等都需进一步的研究和探讨。     

水淬渣-石英砂双层滤料反冲洗试验研究

反冲洗是快滤池的一项关键技术,反冲洗的效果关系到滤床下一个周期的过滤效果.试验证明水淬渣-石英砂双层滤料采用气-水反冲洗在冲洗效果、减少冲洗时间、降低冲洗耗水量及避免混层等方面比单水反冲洗有优势.在工程实践中水淬渣石英砂双层滤料反冲洗选用水强度为5L/m2·s、气强度为10L/m2·s、冲洗历时4min合适.     

膜生物反应器营地生活污水处理设备应用

基于膜生物反应器(Membrane Bio-Reactor,MBR)工艺建造的生活污水处理装置处理营地生活污水具有很多优势。通过对中海油乌干达营地MBR设备的调试,确定出设备的运行参数:过滤10min、停止2min;每隔4h自动进行产水反洗;产水流量200L/h;在线化学清洗时间每隔144h一次或产水抽吸压力≥30kPa时自动进行;所采用清洗剂浓度为500¹ 000mg/L,每片膜曝气量3Nm3/h。通过该系列参数的确定,保证了设备主要指标满足项目所在地的国家标准。     

苏里格气田天然气处理厂含油污泥破乳剂筛选与优化

随着化学助剂的使用量加大,苏里格气田天然气处理厂含油污泥乳化现象严重,油水分离不充分,导致后续处理难度大,环境风险加大等。为解决上述问题,开展含油污泥破乳剂筛选实验,从11种破乳剂中筛选出DS02(聚氧乙烯聚氧丙烯聚醚破乳剂)破乳效果最好。同时,利用正交优化法对其破乳过程工艺操作参数进行优化,确定最佳工艺条件为:温度35℃、加药浓度85mg/L、离心时间16min、转速3 000r/min。     

膜吸收法去除油页岩干馏污水中的氨氮

采用膜吸收的方法对经除油剂及膜过滤预处理的某页岩炼油厂油页岩干馏污水中的高浓度氨氮去除进行了现场中试实验。在进水pH值13、温度40℃、脱氮时间120 min时,氨氮去除效率为98.38%;进水pH值11、温度40℃、脱氮时间120 min时,氨氮去除率为93.24%。结果表明:膜吸收法对油页岩干馏污水具有很好的氨氮脱除效果。该方法操作简单,碱投加量较少,氨氮剩余浓度适当并可由后续生化系统去除,工程适用性强。     

不同操作条件对纳滤膜去除水中五价砷的研究

采用纳滤膜（NF90）过滤自配含砷水,研究在不同操作条件下纳滤膜对水中砷去除效果的影响。本实验探讨膜进水浓度、水的pH值、膜进水温度、操作压力、水中天然有机物浓度等对膜除砷效率的影响。结果表明：纳滤膜对水中五价砷（As（Ⅴ））的去除率很高,最高去除率能达到99%,在实验的前2.5个小时内,砷的去除率均在90%以上。但是,纳滤膜除砷效率随着时间变化,去除率会降低。不同的操作条件对纳滤膜除砷的影响很大,研究不同条件的影响对应用很有意义。     

余压过滤系统在工业循环水系统中的应用

砂过滤器是一种传统而高效的水处理设备,广泛应用于钢铁企业循环水系统。目前钢铁企业最常用的砂滤器是高速或中速砂过滤器。本文结合新型浅层砂过滤器的应用,对余压过滤系统技术（余压全滤、余压旁滤）应用于钢铁企业循环水系统进行了分析,并对具体的设计方法进行了详细的介绍,可供实际生产和工程建设参考。     

电袋复合除尘技术的试验研究

通过对电袋复合除尘器性能试验及对喷吹清灰过程的研究,分析了荷电粉尘对滤料过滤性能的影响,探讨了高强滤料的研究开发及电袋复合除尘器的大型化技术等问题。     

Accelerated ash accumulation method for diesel particulate filter and its characterization: a review

ABSTRACT

It is well known that high-efficiency wall-flow particulate filter is the most commonly used technology that can effectively reduce both particulate matter (PM) and particulate number (PN) to comply with the latest emission legislations. Ash, defined as the noncombustible, non-evaporative residue derived mostly from lubricants, has critical impact on engine backpressure, particulate filter filtration efficiency and durability performance, therefore, the investigation of ash impact on particulate filter is of great importance. Due to cost-saving potential, several published methods from different laboratories for accelerated ash loading under carefully controlled conditions are described in this review, including some characterization methods that have been used for the evaluation of filter performance. In addition, the impact of ash deposit on back pressure and regeneration performance are also discussed in this review.     

碳五加氢石油树脂化工废水的处理

本文介绍了应用新型曝气沉淀池-曝气生物滤池工艺处理碳五加氢石油树脂化工废水的工程实例。运行表明，通过调节水的pH值，改善铝的去除率。新型曝气沉淀池能有效地去除SS、CODCr、石油类和部分有机物，为后续好氧生物处理创造了一个良好的环境；新型挂膜方式的曝气生物滤池(BAF)工艺能稳定高效地去除SS、CODCr、硫化物、苯等，出水水质达到了国家一级排放标准.     

炉渣用于深层过滤的试验研究

将炉渣用作深层过滤的床层过滤,在油田水处理中具有良好的应用前景。通过对炉渣滤料的物性测定,对流体力学性能、过滤性能及反洗性能的研究,获得了有关炉渣滤料的粒径分布、床层孔隙率、密度、吸水率等物性参数,以及清洁滤料床层阻力与速度的关系曲线和流化曲线,过滤条件下床层阻力随时间的变化关系和悬浮物脱除率随时间的变化曲线,炉渣床层的反洗曲线。结果表明：炉渣表面粗糙,有棱角,吸附表面积大,孔隙率大,过滤效果好;炉渣滤料密度小,反洗效果较好,反洗用水量只是过滤水量的５％左右;同时,炉渣作为滤料用于深层过滤,不仅来源广泛,而且属废物利用。     

新型滤料──短纤维性能研究

短纤维作为一种滤料应用于水过滤器中，具有密度小，孔隙率大，比表面积大的优点，它在过滤进程中，滤速高，阻力小，过滤周期长，能使悬浮物脱除率达到９６％以上，是一种应用前景很好的滤料。在本文中对短纤维滤料的过滤性能作了系统地研究。     

Remediation of saturated soil contaminated with petroleum products using air sparging with thermal enhancement

Pollutants in the form of non-aqueous phase liquids (NAPLs), such as petroleum products, pose a serious threat to the soil and groundwater. A mathematical model was derived to study the unsteady pollutant concentrations through water saturated contaminated soil under air sparging conditions for different NAPLs and soil properties. The comparison between the numerical model results and the published experimental results showed acceptable agreement. Furthermore, an experimental study was conducted to remove NAPLs from the contaminated soil using the sparging air technique, considering the sparging air velocity, air temperature, soil grain size and different contaminant properties. This study showed that sparging air at ambient temperature through the contaminated soil can remove NAPLs, however, employing hot air sparging can provide higher contaminant removal efficiency, by about 9%. An empirical correlation for the volatilization mass transfer coefficient was developed from the experimental results. The dimensionless numbers used were Sherwood number (Sh), Peclet number (Pe), Schmidt number (Sc) and several physical-chemical properties of VOCs and porous media. Finally, the estimated volatilization mass transfer coefficient was used for calculation of the influence of heated sparging air on the spreading of the NAPL plume through the contaminated soil.     

模拟地下水微生物除铁技术的探索性研究

为探讨模拟地下水微生物除铁技术的若干控制因素以及微生物除铁的部分规律,对四个装有不同粒径石英砂填料的滤柱进行人工模拟实验及分析测试。实验结果表明：滤柱的成熟过程是铁细菌有规律的增殖并固定滤料表面的铁质活性滤膜实现对亚铁离子氧化的过程。根据细菌的成长过程,滤柱除铁效果以及滤柱能够承受的负荷,把滤砂的成熟过程分为适应期、第一增长期、第二增长期和稳定期等四个时期。在实现除铁的过程中,填料大小、滤速等条件对除铁效果有着影响。     

Flow-through rates and evaluation of solids separation of compost filter socks versus silt fence in sediment control applications

Soil loss rates from construction sites can be 1000 times the average of natural soil erosion rates and 20 times that from agricultural lands. Silt fence (SF) is the current industry standard used to control sediment originating from construction activities. Silt fences are designed to act as miniature detention ponds. Research has indicated that SF sediment filtering efficiency is related to its ability to detain and pond water, not necessarily the filtration ability of the fabric. Design capacity and spacing is based on flow-through rate and design height. In addition, increased detention of runoff and pressure from ponding may increase the likelihood of overtopping or failure of SF in field application. Testing was conducted on compost silt socks (SS) and SF to determine sediment filtering efficiency, flow-through rate, ponding depth, overtopping point, design height, and design capacity. Results indicate flow-through rate changes with time, as does ponding depth, due to the accumulation of solids on/in the sediment filters. Changes in depth with time were a linear function of flow rate after 10 min of flow, up to the time the sediment filter is overtopped. Predicting the capacity of SF and SS to handle runoff without the filter being overtopped requires consideration of both runoff rate and length of runoff time. Data show SS half the heights of SF were less likely to overtop than SF when sediment-laden runoff water flow rates are less than 1.03 L(-1) s(-1) m(-1) (5 gpm/ft, gal per minute per lineal foot). Ponded depth behind a 61.0-cm (24 in) SF increased more rapidly than behind a 30.5-cm diam. (12 in) SS, and at the end of the thirty minutes, the depth behind the SF was 75% greater than that behind the SS. Removal of solids by the SF and the SS were not shown to be statistically different. Results were used to create a Microsoft Excel-based interactive design tool to assist engineers and erosion and sediment control planners on how to specify compost SS relative to SF in perimeter sediment control applications.     

Filtering with a drill pump: an efficient method to collect suspended sediment

Water quality monitoring programs across multiple disciplines use total suspended solids (TSS), and volatile suspended solids (VSS), to assess potential impairments of surface water and groundwater. While previous methods for instream filtering have been developed, the need for rapid, cost‐effective, high volume sampling has increased with the need to verify and supplement data produced by sondes and instantaneous data loggers. We present an efficient method to filter water instream with a portable drill pump that results in reduced sample processing time, and potentially reduced error associated with sample transportation, preservation, contamination, and homogenization. This technical note outlines the advantages of filtering instream vs. in the laboratory. It also compares TSS and VSS concentrations filtered with a drill pump vs. standard filtration methods with a vacuum pump as outlined by USEPA methods 160.2 and 160.4. Samples were collected at 4 sites and filtered in the field, or transported to the laboratory and filtered within 12 or 24 h of collection. Overall TSS and VSS samples filtered instream with a drill pump vs. in the laboratory produced similar concentrations with a similar range in variability for each method. Sample filtering with a drill pump decreased processing time by five minutes per sample.