The Properties of PLA/Oxidized Soybean Oil Polymer Blends

Novel polymer blends based on completely renewable polymers were reported. Polymer blends based on polylactic acid (PLA) and oxidized and hydroxylated soya bean oil polymers were prepared. Plasticization and mechanical strength effect of the soya bean oil polymers on the PLA were observed. Fracture surface analysis of the polymer blends was carried out by using scanning electron microscopy. The PLA blends showed more amorphous morphologies compared to pure PLA. The blends had better elongation at break in view of the stress–strain measurement. Blend of PLA with the hydroxylated polymeric soya bean oil indicated the slightly antibacterial properties.     

超声波协同催化氧化法脱除废旧轮胎热裂解油中的硫

采用超声波氧化与催化氧化脱硫技术相结合,脱除废旧轮胎热裂解油中的硫,对脱硫工艺进行了研究.最佳操作条件为:超声波声强0.25 W/cm~2,超声时间10 min,V(H_2O_2)∶V(油)=0.04,V(CH_3COOH)∶V(H_2O_2)＝0.5,V(FeSO_4·7H_2O) ∶ V(H_2O_2)＝0.15.在上述最佳操作条件下,进行4次脱硫,可使热裂解油中硫质量分数降至0.21%,脱硫率达到72%.     

考虑油滴碰撞聚结的斜板除油过程模拟

考虑离散油滴在油田废水除油过程中发生的油滴碰撞聚结现象,模拟得出斜板除油器内全部油滴的动态信息,用于斜板除油器除油效率的计算.对矩形同向流斜板除油过程的模拟研究表明:油滴的碰撞聚结会增加斜板除油的效率;当废水的原始含油浓度增大时,斜板除油的效率会增大,碰撞聚结对除油效率提高的影响也越大;废水流动速度提高及斜板的倾斜角度增加均会使斜板的除油效率降低,但此时油滴碰撞聚结对除油效率的影响仍很明显.     

共基质和无机盐对原油降解菌株降解原油效果的影响

从大港油田石油污染土壤中分离筛选出1株原油降解菌X3,对原油的降解率达72．6％,经鉴定X3菌株属于假单胞菌属（Psedomonas）。利用生物摇床对X3菌株降解原油的实验发现,共代谢基质α-乳糖对X3菌株降解原油有促进作用,可使原油降解率提高到80．3％;而葡萄糖和蔗糖对X3菌株降解原油有抑制作用。Fe2＋对X3菌株的降解原油也有促进作用,在α-乳糖和Fe2＋的共同作用下,X3菌株对原油的降解率可达82．3％;K＋和Mg2＋对X3菌株降解原油则有抑制作用。在FeSO4质量浓度为0．2～0．3mg／L时,X3菌株对原油的降解率最高,FeSO4质量浓度继续增加,X3菌株对原油的降解率下降。     

Analytical determination of the suitability of different processes for the treatment of odorous waste gas

In order to determine the efficiency of different treatment systems for the reduction of odorous emissions, a gas chromatographic method followed by simultaneous mass spectrometry and olfactometry (GC-MS/O) was developed. Samples from a coffee bean roasting and a fat and oil processing plant were analyzed, respectively. The results were compared with the data obtained by olfactometric measurements. At a coffee bean roasting plant, cooling gases were analyzed prior to and after treatment in a full scale bioscrubber. The GC-MS/O analysis showed that the amounts of aldehydes and ketones decreased after treatment of cooling gases of coffee bean roasting in the bioscrubber, whereas the contents of the heterocyclic compounds, like pyridine and the pyrazines, and acetophenone and guaiacol remained almost unchanged. The amounts of dimethyl disulfide, 3-hydroxy-2-butanone, and the carboxylic acids increased after bioscrubber treatment. Furthermore, the performance of each stage of a combined experimental plant for the treatment of exhaust air of fat and oil processing was investigated. This treatment plant consisted of a bioscrubber, a biofilter, and an activated carbon adsorber. The important odor-active compounds of the exhaust air of fat and oil processing were the typical fat oxidation products (aldehydes, ketones) and with lower importance 2-pentylfuran, a few terpenes and aromates. Again, the key odor-active compounds, aldehydes and ketones, were degraded in the bioscrubber. Further degradation of aliphatic, unsaturated, methylated, and cyclic alkanes, as well as aromates, terpenes, and furans by the biofilter was observed. After the last treatment stage, the activated carbon filter, only small amounts of aliphatic, unsaturated, methylated, and cyclic alkanes and aromates remained in the waste gas. For both applications, the results of the developed GC-MS/O method correlated very well with olfactometric measurements.     

柴油低温临界吸收法回收装车挥发油气

研究了采用柴油低温临界吸收法回收装车挥发油气的效果。实验结果表明：按装车挥发油气中的总烃体积分数为20.88%、装车挥发油气流量为280 m³/h、年运行时间为2 668 h计,装置年回收油气量为291 t,装置年最大运行功率为206.770 MW,装置投资回收期为3 a;处理后净化气中的总烃体积分数为1.24%,排放质量浓度低于25 g/m³,油气回收率达95%。处理后净化气满足GB 20950—2007《储油库大气污染物排放标准》,取得了较好的环保效益和经济效益。     

微生物降解重油的初步研究

丛石油污染的土壤中筛选出一株假单胞菌,考察了其对重油的降解效果。降解18d,重油的降解率达到42．8％,饱和烃、芳香烃、胶质、沥青质的降解率分别为42．95％,43．85％,44．5％,5．55％;质量浓度2．5g／L的表面活性剂Tween-80可使重油的18d降解率达到51．0％;弱碱性条件有利于重油的生物降解;生物泥浆法处理重油污染的土壤,1kg土壤中重油质量100g,降解45d,重油的降解率达到38．85％。     

壳聚糖复合吸附剂对油的吸附性能

以天然可生物降解的壳聚糖和硬脂酸为原料,通过壳聚糖2位氨基与硬脂酸的羧基相互作用,引入疏水烷基链,制备了疏水的壳聚糖-硬脂酸复合吸附剂(简称复合吸附剂),采用傅立叶红外光谱、X射线衍射对复合吸附剂的结构进行表征,并考察了复合吸附剂对油的回收性能.实验结果表明:壳聚糖和硬脂酸以离子形式结合得到复合吸附剂;当硬脂酸与壳聚糖质量比为0.7时,硬脂酸的结合量最大;复合吸附剂对油的吸附量、保油率、脱附率的顺序分别为花生油(14.93 g/g)>甲基硅油(10.71 g/g)>液体石蜡(9.37 g/g),花生油(94.51%)>液体石蜡(90.74%)>甲基硅油(78.69%),花生油(95.62%)>液体石蜡(93.27%)>甲基硅油(90.73%).     

Oil/Suspended Particulate Material Interactions and Sedimentation

The interactions of physically dispersed oil droplets with suspended particulate material (SPM) can be important for the transport of bulk quantities of spilled crude oil and polycyclic aromatic hydrocarbons (PAH) to subtidal sediments. The literature regarding oil/SPM interactions is reviewed, and results from whole-oil droplet/SPM interaction kinetics and pure-component (Prudhoe Bay crude oil distillate cut) equilibrium partitioning experiments are presented. The effects of oil type, SPM characteristics, and salinity on the interaction rates are examined, and the importance of whole-oil droplet/SPM interactions on particle agglomeration and settling behavior are discussed. Whole-oil droplet/SPM interactions are retarded as oil droplet dispersion into the water column is inhibited by oil viscosity increases due to evaporation weathering and water-in-oil emulsification. Compared to whole oil droplet/SPM interactions, dissolved-component/SPM adsorption is not as significant for transport of individual components to sediments. The information presented in this paper can be used to augment computer-based models designed to predict oil-spill trajectories, oil-weathering behavior, and spilled oil impacts to the marine environment.     

微生物菌剂强化处理油砂

研究了微生物菌剂对油砂的处理效果,并通过第15天和第30天两次追加微生物菌剂和营养物质来加速分解石油类污染物。试验结果表明,经过56d的处理,菌剂强化处理单元最终油去除率达到47．4％;添加营养物质和农家肥的对照单元油去除率为23．6％,证明土著菌种在得到适宜的营养和共代谢基质后降解了部分石油;未做任何处理的原始油砂单元含油量基本没有变化。通过气相色谱一质谱联用分析表明,微生物菌剂对于较少碳原子数的有机物质有较好的降解效果。处理单元中随着石油分解过程的进行,系统pH会有一个明显的下降过程。通过对照单元细菌数的检测发现,改善营养物质和氧含量,可以提高土著菌种的石油降解件能。     

The Oil Pollution Act of 1990: A Decade Later

Analysis of oil spills data confirms that accidental oil spills are natural phenomenon and that there is a relationship between accidental oil spills and variables like vessel size, vessel type, time and region of spill. The volume of oil spilled bears relationship with the volume of petroleum imports and domestic movement of petroleum and proportion of large oil spills. Finally, navigational risk increases with increase in marine traffic and is also determined by variables like hydrographic and meteorological conditions, water configuration, maneuvering space, obstructions and nuisance vessels. The Oil Pollution Act, 1990 (OPA 90) was passed by the US Congress in the aftermath of 11 million gallon spill of crude oil in Prince William Sound, Alaska. The objective of OPA 90 was to minimize marine casualties and oil spills by addressing preventive, protective, deterrent and performance aspects of accidental oil spills. The arm of various regulations like double-hull tankers and vessel response plans extended to both US flagged and foreign-flagged tank vessels. The cost–benefit analysis of major regulations shows that the estimated costs exceed estimated benefits. We observe from USCG data on oil spills by size, by vessel type, Coast guard district and type of petroleum product that there have been significant reductions in the number and the quantity of oil spills. Our regression results show that the quantity of oil spilled increases with increase in oil imports but increases at a decreasing rate. The quantity of oil spilled decreases with increases in the domestic oil movements. Furthermore, percent of oil spills larger than 10,000 gallons also increases the potential quantity of oil spilled. OPA 90 has been a deterrent to accidental oil spills but the finding is not conclusive.     

Oil outflow estimates for tankers and barges

Results of an analysis to estimate potential oil outflow from tankers in the event of groundings and collisions is presented. Three baseline tanker types are considered: pre-MARPOL (COW), MARPOL '73 (SBT only), MARPOL '73/'78 (PL/SBT) before and after these tankers have been retrofitted with various combinations of pollution prevention measures. Specifically the analysis examines four tanker sizes, 46 600, 71 000, 152 000 and 268 000 dwt, and various pollution measures — protectively located spaces (PL/spaces) in various ballast arrangements and with clean ballast tanks (CBTs), hydrostatically balanced loading (HBL), probabilistically located HBL, combinations of HBL and PL/spaces, double bottom or double side retrofits, and replacement of the tanker with a double hull vessel. Additionally, oil outflow estimates are presented for a US coastal and an ocean going barge of over 5000 gt with and without PL/spaces, PL/SBT, and HBL. The accidental oil outflow estimates are developed in accordance with probabilistic and deterministic models of IMOs MARPOL Annex I Regulations 13F and 13G. The accidental oil outflow estimates presented in the paper may provide oil spill response and related organizations with information to assist in planning for oil spill response activities.     

用带式压滤机处理含油污泥

对中油集团锦州石化分公司污水处理场的含油污泥装置进行了改造，介绍了带式压滤机处理含油污泥的机理，特点及工艺流程，从装置近10个 月的运行效果看，生产运行指标，达到了设计要求，同时，带式压滤机处理含油污泥仍具有一些不足之处。     

Oil adsorbent produced by the carbonization of rice husks

In this study, rice husks considered to be agricultural waste are converted into an adsorbent intended for use in the disposal of oil spills. The raw and refined (defiberized) husks of Japanese Akita Komachi rice were pyrolyzed in a vacuum (500 Pa) at 300-800 degrees C. The amount of A-heavy and B-heavy oils adsorbed on the carbonized rice husk were then evaluated. Oil adsorption is dependent on the type of oil. Rice husks refined and then pyrolyzed at 600-700 degrees C (1.0 g) adsorbed >6.0 g of B-heavy oil and <1.5 g of water, which indicates their usefulness as an adsorbent for oil spill cleanup in Japan. The refining process contributes to an improvement in the oil adsorption capacity, while the carbonization time (at 600 degrees C) has only a minor influence. The residual fluid components in the carbonized rice husks, rather than their porosity, are closely related to oil adsorption capacity.     

稠油废水破乳剂的研究进展

介绍了稠油废水的来源、特点和乳化成因,综述了稠油废水破乳剂的研究进展,分析了不同破乳剂的破乳机理和优缺点,并对破乳剂的发展方向进行了展望和建议。     

Development of a National Marine Oil Transportation System Model

This paper presents the development of a model of the marine oil transportation in the United States. NMOTSM, the National Marine Oil Transportation System Model, is a high-level strategic decision-making tool that will be used to systematically identify causes of oil spills and prioritize oil pollution R and D needs for prevention and response. Three distinct phases in the analysis are identified, namely the formulation of the oil transport model, the risk and safety performance assessment and the evaluation of potential prevention, and response measures and approaches.     

水域泄漏油品回收处理技术

提出了水域泄漏油品回收技术的装备需求,介绍了水域泄漏油品问收处理措施.采用拦油栅来控制漂浮在水上的油品,将泄漏油品集中在相对较小的区域内,并使水面的浮油层加厚,然后使用人工或机械对泄漏油品进行回收.对于水域中的少量泄漏油品,采用吸油材料来进行吸附.在油膜较薄,难以用机械方法回收的情况下,使用消油剂或固化剂进行处理.水域...     

Oil and water separation in marine oil spill clean-up operations

This paper discusses the changes in spilled oil properties over time and how these changes affect differential density separation. It presents methods to improve differential density, and operational effectiveness when oil-water separation is incorporated in a recovery system. Separators function because of the difference in density between oil and seawater. As an oil weathers this difference decreases, because the oil density increases as the lighter components evaporate. The density also increases as the oil incorporates water droplets to form a water-in-oil emulsion. These changes occur simultaneously during weathering and reduce the effectiveness of separators. Today, the state-of-the-art technologies have limited capabilities for separating spilled marine oil that has weathered.For separation of emulsified water in an emulsion, the viscosity of the oil will have a significant impact on drag forces, reducing the effect of gravity or centrifugal separation. Since water content in an emulsion greatly increases the clean up volume (which can contain as much as two to five times as much water as the volume of recovered oil), it is equally important to remove water from an emulsion as to remove free water recovered owing to low skimmer effectiveness. Removal of both free water and water from an emulsion, has the potential to increase effective skimming time, recovery effectiveness and capacity, and facilitate waste handling and disposal. Therefore, effective oil and water separation in marine oil spill clean-up operations may be a more critical process than credited because it can mean that fewer resources are needed to clean up an oil spill with subsequent effects on capital investment and basic stand-by and operating costs for a spill response organization.A large increase in continuous skimming time and recovery has been demonstrated for total water (free and emulsified water) separation. Assuming a 200 m³ storage tank, 100 m³ h⁻¹ skimmer capacity, 25% skimmer effectiveness, and 80% water content in the emulsion, the time of continuous operation (before discharge of oil residue is needed), increases from 2 to 40 h and recovery of oil residue from 10 to 200 m³.Use of emulsion breakers to enhance and accelerate the separation process may, in some cases, be a rapid and cost effective method to separate crude oil emulsions. Decrease of water content in an emulsion, by heating or use of emulsion breakers and subsequent reduction in viscosity, may improve pumpability, reduce transfer and discharge time, and can reduce oily waste handling, and disposal costs by a factor of 10. However, effective use of emulsion breakers is dependant on the effectiveness of the product, oil properties, application methods and time of application after a spill.     

A Numerical Simulation of an Oil Spill in Tokyo Bay

An oil spill accident happened in Tokyo Bay on 2 July 1997. About 1500 m³ of crude oil was released on the sea surface from the Japanese tanker Diamond Grace. An oil spill model is applied to simulate the fate of spilled oil. The Lagrangian discrete-parcel method is used in the model. The model considers current advection, horizontal diffusion, mechanical spreading, evaporation, dissolution and entrainment in simulating the oil slick transformation. It can calculate the time evolution of the partition of spilled oil on the water surface, in the water column and the sedimentation on the bottom. A continuous source at constant rate is set up as a tanker off the coast of Yokohama. The grid size is 1 km in the calculation domain. The residual flow simulated by a 3-D hydraulic model and observed wind data are used for advection. The simulated distribution of oil spreading agrees well with observations from satellite remote-sensing.