丙纶吸油材料处理含油废水

采用丙纶吸油材料从含油工业废水中吸附分离和回收油类物质,可根据废水的初始状况、最终要求、水流流量等因素,选用适合的净化处理方法。文中介绍了几种适合于一般的、高浓度的、大流量的、乳化态的、固相悬浮物高的含油废水净化处理方法,处理后净化水的油浓度可降至1—5毫克/升甚至1毫克/升以下。     

海上含油钻屑的热解析除油处理

采用间接加热的热解析技术对海上油田含油钻屑进行处理,考察了热解析处理的效果和影响因素。实验结果表明：在热解析主温度为410.0 ℃下对含油率为14.00%~23.60%（w）的钻屑进行热解析处理,处理后钻屑的石油烃含量低至0.07%;为达到处理后钻屑含油率低于1%的要求,处理速率最高可达2.47 t/h;回收油的主要烃类化合物组成与岩屑油一致,可用于泥浆复配;冷凝回收水的COD及石油类物质超标,处理后可作为循环冷却水的补充水;外排气体的污染物指标达到国家排放标准;该套实验装置处理含油率为14.00%~23.60%的钻屑,柴油消耗量小于15 L/t、电能消耗量小于9 kW·h/t。     

从氯油尾气中回收氯乙烷

工业上以酒精和氯为原料生产氯油。氯油经精制后得到三氯乙醛,这是一种很有用途的化工中间产品,可用于制农药、氯仿等。在氯油的生产过程中,排出含有大量氯乙烷和氯化氢的尾气。对于这种尾气,目前国内只有少数厂家进行回收处理,大多数厂家仍是直接外排,这样,不仅浪费资源,而且严重污染环境。     

松烃油废水的综合利用

本文主要介绍了涂料行业在生产松香改性树脂时产生的含松烃油废水,经过中和、洗涤、澄清分离的工艺处理,获得了松烃油新产品,开拓了一条松烃油有机废水综合利用的途径。该项目投资少,见效快,回收工艺成熟,松烃油的质量稳定,用户反映良好,有较明显的经济效益和环境效益,在涂料行业中具有推广应用的意义。     

日本变电设备的环境保护技术

介绍了日本变电设备的环境保护技术,包括噪声控制技术、SF6气体控制技术、防止油泄漏技术、回收利用技术等,希望对我国变电设备的运行维护提供借鉴.     

利用再生底线油生产润滑油、润滑脂的绿色关键技术取得积极进展

正再生底线油是废润滑油回收利用过程中留下的粘稠重质油,含有大量的胶质沥青质和金属磨屑等杂质,难于处理和利用,处置不当易造成环境污染。为推动再生底线油资源化、无害化利用,2016年绿色制造专项工作支持了新疆福克油品股份有限公司"利用再生底线油生产润滑油、润滑脂的关键技术突破"项目。目前该项目进展顺利,通过对底线油高值化利用绿色制造关键工艺技术和装备的创新和集成,解决     

废旧塑料的处理和利用

介绍了几种处理和利用废旧塑料的方法：再生法、热分解法、焚烧法，并着重介绍了热分解法。采用热分解法处理废旧塑料。既可以减轻环境污染，又可以回收油品，具有一定的现实意义。文中还对有关部门提出了回收利用废旧塑料的具体建议。     

用高铁酸钾处理含聚合物的油田废水

目前，我国部分油田采用了聚合物(PAM)驱油的三次采油技术，取得了较好的增油效果。但是在PAM驱油废水的处理中，PAM驱油废水的水质与水驱油废水的水质有很大的差别。PAM驱油废水在：PAM存在下，其含油量和粘度随PAM浓度的增加而增加，PAM分子集中在油水界面上，与乳化剂分子一起形成较大强度和良好弹性的复合膜，W／O和O/W混合乳层加厚，在分离和电脱水过程中使得油水分离速度减慢，破乳剂破乳效果变差。采用常规处理工艺和水处理剂处理这种废水，达不到回注或排放标准(含油量小于10mg／L)。     

废弃印刷线路板中材料的资源化回收利用技术

废弃印刷线路板（WPCBs）既有污染环境的一面,又有可资源化回收利用的一面.通过机械物理法、热解、超临界流体氧化和离子液体溶解等方法对其进行分离和回收金属和非金属材料.初步分选的金属需要进一步提纯以实现高附加值.而非金属材料可以用热解法、微波处理、超临界流体技术、等离子技术等技术进行产气和能量回收,也可以通过制备建筑材料或填料和其它功能村料进行物料回收.总之,对WPCBs进行适当地处理不但可以减轻环境压力,还可以变废为宝,实现资源再生利用.     

压缩机气缸废油的再生工艺

压缩机气缸油在长时间使用后,受温度和介质的影响,油质发生很大变化,其中沥青、胶质等杂质含量很高,粘度变大,从介质中分离排出后,若不回收,将成为环境油污染的来源.我公司为了根治油污染,成立了压缩机气缸油回收再生攻关小组,经反复试验,研究成功一种酸碱处理加白土吸附的废油再生方法.     

Biodegradation of Dispersed Forties Crude and Alaskan North Slope Oils in Microcosms Under Simulated Marine Conditions

For oil spills in the open sea, operational experience has found that conventional response techniques, such as mechanical recovery, tend to remove only a small fraction of oil during major spills, a recent exception being the Mississippi River spill in Louisiana [Spill Sci. Technol. Bull. 7 (2002) 155]. By contrast, the use of dispersants can enable significant fractions of oil to be removed from the sea surface by dispersing the oil into the water column. It is thought that once dispersed the oil can biodegrade in the water column, although there is little information on the mechanism and rate of biodegradation. Two studies were undertaken on dispersion, microbial colonisation and biodegradation of Forties crude and Alaskan North Slope (ANS) oils under simulated marine conditions. The study using the Forties crude lasted 27 days and was carried out in conditions simulating estuarine and coastal conditions in waters around the UK (15 °C and in the presence of nutrients, 1 mg N-NO₃/l), while the ANS study simulated low temperature conditions typical of Prince William Sound (8 °C) and took place over 35 days. The results of both studies demonstrated microbial colonisation of oil droplets after 4 days, and the formation of neutrally buoyant clusters consisting of oil, bacteria, protozoa and nematodes. By day 16, the size of the clusters increased and they sank to the bottom of the microcosms, presumably because of a decrease in buoyancy due to oil biodegradation, however biodegradation of n-alkanes was confirmed only in the Forties study. No colonisation or biodegradation of oil was noted in the controls in which biological action was inhibited. Oil degrading bacteria proliferated in all biologically active microcosms. Without dispersant, the onset of colonisation was delayed, although microbial growth rates and population size in ANS were greater than observed with the Forties. This difference reflected the greater droplet number seen with ANS at 8 °C than with Forties crude at 15 °C. Although these studies differed by more than one variable, complicating comparison, the findings suggest that dispersion (natural or chemical) changes the impact of the oil on the marine environment, potentially having important implications for management of oil spills in relation to the policy of dispersant use in an oil spill event.     

油田储油罐非甲烷总挥发实验及仿真模拟

针对油田单井拉油罐非密封生产带来的油气泄漏问题,建立小型原油储油罐挥发损耗实验模拟平台,通过气相色谱法探究各因素对其损耗的影响,利用Fluent仿真软件模拟储油罐的泄漏扩散。结果表明:储液温度和有无风环境对储油罐非甲烷总烃(NMHC)挥发影响较大,储液高度和环境温度对其影响较小;仿真模拟无风环境下,储油罐泄漏口短时间内存在油气积聚现象;有风环境下,当风速为1 m/s,油气积聚不明显;随风速增大,扩散浓度场面积不断增大,油品损耗量增大,在风速为5 m/s的环境下,扩散300 s时的浓度场面积相比扩散200 s时较小,但泄漏口处的油气积聚面积增大。     

CytoSol – Cleaning Oiled Shorelines with a Vegetable Oil Biosolvent

A cleanup process has been developed to aid in the removal of crude or fuel oil from shorelines using CytoSol “biosolvent” formulation based on vegetable oil methyl esters in combination with bioremediation enhancers. The CytoSol biosolvent dissolves and floats the oil, the oil/biosolvent mixture is rinsed off with ambient temperature water for collection as a consolidated layer with skimmers. The collected oil mixture can be recycled as a burner fuel. Nutrient enhancers in the formulation then stimulate the natural biodegradation of the remaining residual hydrocarbons. This new approach minimizes physical and chemical impacts to marine organisms, cleans oiled surfaces effectively, and allows the oiled ecosystem to recover with less mortality than conventional methods involving hot water, detergents or other chemical cleaners. CytoSol is ideally suited for port facilities and waterfronts dealing with occasional small oil spills and has undergone extensive laboratory testing for the US EPA. In 1997, the CytoSol biosolvent was licensed in the state of California as a shoreline cleaner and set up for commercial distribution.CytoSol biosolvent can extract heavy petroleum (crude, fuel oils) off shoreline habitats, mussel-encrusted breakwaters or pilings, and estuary vegetation. The viscosity of the product tends to limit the penetration of the CytoSol/oil mixture into sand and gravel beaches, allowing more of the dissolved oil to be removed from the shoreline by washing. The product has a low specific gravity (0.87), tends to consolidate oil, and is practically immiscible with water, so it facilitates the recovery of spilled oil with conventional skimming and absorbent boom technologies. Since it is non-volatile and non-flammable, there is little danger of explosion or fire when spraying it inside confined spaces.     

旋流萃取分离技术处理石化电脱盐废水

采用旋流萃取分离技术处理某炼油厂常减压装置电脱盐废水(初始废水含油量约为5 000 mg/L),优化了废水除油的工艺条件。试验结果表明,废水除油的最佳工艺条件为:旋流萃取分离机中心转子的转速960 r/min、废水流量2 000 L/h、废水温度80℃。废水经旋流萃取分离后,废水的含油量小于200 mg/L,废水除油效果较好;分离后油相的含水量约为0.1%(w),盐质量浓度小于20 mg/L,可回注到常减压装置原料罐循环利用。对于2 Mt/a的常减压装置,采用旋流萃取分离技术后,每年可减少支出100.4万元。     

Polyols and Polyurethanes from Hydroformylation of Soybean Oil

This paper compares physical and mechanical properties of polyurethanes derived via the hydroformylation approach and is a part of our study on the structure–property relationships in polyurethanes created from vegetable oils. The double bonds of soybean oil are first converted to aldehydes through hydroformylation using either rhodium or cobalt as the catalyst. The aldehydes are hydrogenated by Raney nickel to alcohols, forming a triglyceride polyol. The latter is reacted with polymeric MDI to yield the polyurethane. Depending on the degree of conversion, the materials can behave as hard rubbers or rigid plastics. The rhodium-catalyzed reaction afforded a polyol with a 95% conversion, giving rise to a rigid polyurethane, while the cobalt-catalyzed reaction gives a polyol with a 67% conversion, leading to a hard rubber having lower mechanical strengths. Addition of glycerine as a cross-linker systematically improves the properties of the polyurethanes. The polyols are characterized by DSC. The measured properties of polyurethanes include glass transition temperatures, tensile strengths, flexural moduli, and impact strengths.     

Oil-Mineral Aggregate Formation on Oiled Beaches: Natural Attenuation and Sediment Relocation

The significance of oil-mineral aggregate (OMA) formation on the effectiveness of the in situ shoreline treatment options of natural attenuation (natural recovery) and sediment relocation (surf washing) was examined during field trials on two mixed-sediment (sand and pebble) beaches experimentally oiled with IF-30 oil. At both sites, the amount of oil remaining in the experimental plots was dramatically reduced within five days after sediment relocation treatments. Time-series microscopy and image analysis of breaker-zone water samples demonstrate that OMA formation occurred naturally on the oiled beaches at both sites and was accelerated by the sediment relocation procedure. Lower concentrations of OMA in the breaker zone at Site 3 are attributed to the higher wave-energy levels at this site that presumably facilitated more rapid OMA dispersion. The granulometry and mineralogy of beach sediment and of subtidal sediment trap samples indicate that the material settling in nearshore waters originated from the relocated sediment and that a portion of the finer sediment was probably transported out of the study region before settling. Gas chromatography/mass spectrometry analysis demonstrated that a significant fraction of the oil dispersed into nearshore waters and sediments by interaction with mineral fines was biodegraded. The fact that little or no residual oil was found stranded on the shore in areas adjacent to the experimental plots and that only small amounts of oil were found in nearshore subtidal sediments and sediment trap samples suggests that a large fraction of the oil lost from the experimental plots may have been dispersed in the form of relatively buoyant OMA.     

老化油处理技术研究进展

老化油是石油工业生产过程中产生的含大量化学药剂、水、黏土及无机盐的状态稳定的复杂乳液,其产生量大、处理难度高。介绍了老化油的来源、成分、数量、对生产的危害、特点及处理难点,总结了老化油现有的处理方法,包括物理法、化学法、生物法及组合工艺,分析了各种方法的优缺点,并对老化油的管理和研究方向提出了建议。     

Effect of Degree of Substitution of Octenyl Succinate Starch on the Emulsification Activity on Different Oil Phases

Octenyl succinic starch (OSA starch) was synthesized from an aqueous medium and pyridine medium using previously established literature methods. Such a substitution would conceivably impart some hydrophobicity to the already hydrophilic starch chain. Thus, an amphiphilic character could be introduced wherein while the water solubility of the final product would be retained or enhanced, interactions with hydrophobic phases could be enhanced. These products find a variety of applications. The emulsifying activity of OSA starch was tested against different oil phases. It was found that the activity was dependent on the oil phase chosen. The activity was largely independent of the concentration of the substrates when the modification was conducted in an aqueous medium. Products from an organic medium did show an increase in activity with concentration. This difference in activity was attributed to the molecular weight of the final product, which seemed to be lower for the products from an organic medium as suggested by viscometry. The granular state of starch could also have a great effect on the properties of modified starch.     

Development of a catalytic dehalogenation (Cl,Br) process for municipal waste plastic-derived oil

Dehalogenation is a key technology in the feedstock recycling of mixed halogenated waste plastics. In this study, two different methods were used to clarify the effectiveness of our proposed catalytic dehalogenation process using various carbon composites of iron oxides and calcium carbonate as the catalyst/sorbent. The first approach (a two-step process) was to develop a process for the thermal degradation of mixed halogenated waste plastics, and also develop dehalogenation catalysts for the catalytic dehydrochlorination of organic chlorine compounds from mixed plastic-derived oil containing polyvinyl chloride (PVC) using a fixed-bed flow-type reactor. The second approach (a single-step process) was the simultaneous degradation and dehalogenation of chlorinated (PVC) and brominated (plastic containing brominated flame retardant, HIPS–Br) mixed plastics into halogen-free liquid products. We report on a catalytic dehalogenation process for the chlorinated and brominated organic compounds formed by the pyrolysis of PVC and brominated flame retardant (HIPS–Br) mixed waste plastics [(polyethylene (PE), polypropylene (PP), and polystyrene (PS)], and also other plastics. During dehydrohalogenation, the iron- and calcium-based catalysts were transformed into their corresponding halides, which are also very active in the dehydrohalogenation of organic halogenated compounds. The halogen-free plastic-derived oil (PDO) can be used as a fuel oil or feedstock in refineries.     

Determination of the Burning Characteristics of a Slick of Oil on Water

The burning rate of a slick of oil on a water bed is characterized by three distinct processes, ignition, flame spread and burning rate. Although all three processes are important, ignition and burning rate are critical. The former, because it defines the potential to burn and the latter because of the inherent possibility of boilover. Burning rate is calculated by a simple expression derived from a one-dimensional heat conduction equation. Heat feedback from the flame to the surface is assumed to be a constant fraction of the total energy released by the combustion reaction. The constant fraction (χ) is named the burning efficiency and represents an important tool in assessing the potential of in situ burning as a counter-measure to an oil spill. By matching the characteristic thermal penetration length scale for the fuel/water system and an equivalent single layer system, a combined thermal diffusivity can be calculated and used to obtain an analytical solution for the burning rate. Theoretical expressions were correlated with crude oil and heating oil, for a number of pool diameters and initial fuel layer thickness. Experiments were also conducted with emulsified and weathered crude oil. The simple analytical expression describes well the effects of pool diameter and initial fuel layer thickness permitting a better observation of the effects of weathering, emulsification and net heat feedback to the fuel surface. Experiments showed that only a small fraction of the heat released by the flame is retained by the fuel layer and water bed (of the order of 1%). Ignition has been studied to provide a tool that will serve to assess a fuels ease to ignite under conditions that are representative of oil spills. Two different techniques are used, piloted ignition when the fuel is exposed to a radiant heat flux and flash point as measured by the ASTM D56 Tag Closed Cup Test. Two different crude oils were used for these experiments, ANS and Cook Inlet. Crude oils were tested in their natural state and at different levels of weathering, showing that piloted ignition and flash point are strong functions of weathering level.