溶剂萃取法修复石油污染土壤

对溶剂萃取法修复石油类污染土壤的新技术做了较为全面的概述.首先,介绍了溶剂萃取技术的概念、机理和适用范围;其次,介绍了包括有机溶剂、表面活性剂、环糊精、超临界流体在内的萃取剂的研究进展;再次,阐述了影响溶剂萃取效率的因素和溶剂萃取的工艺条件;最后,对溶剂萃取技术的研究和应用做了展望.     

微波辐射柴油脱硫实验研究

采用微波辅助氧化反应的方法对辽河常二线柴油配制油样进行了脱硫实验，过氧化氢作氧化剂，可以把柴油中的含硫化合物有选择性地氧化成相应的具有很强极性的砜，根据相似相溶原理，这些砜因溶于剂相而从柴油中除去，从而降低了硫含量。实验过程中分别考察了氧化荆用量、剂油比、反应体系压力、氧化时间、微波功率等对柴油硫含量的影响。确定了实验室适宜的操作条件：剂油体积比为0．25：1，微波辐射压力为0．05MPa，微波功率为375w，辐射时间为6min，柴油的脱硫率为60％．而在无微波辐射的条件下，脱硫率仅为12％。     

Preparation of bitumen from oil sand by centrifugation

Centrifugation was shown to have certain advantages over solvent extraction for the separation of bitumen from oil sand for research purposes. No fractionation of the bitumen during centrifugation was detected by chemical analysis. Some limitations of the method are pointed out.     

Preparation of bitumen from oil sand by ultracentrifugation

Ultracentrifugation was investigated as a means to obtain solvent-free bitumen from oil sand. The bitumen from three oil sands of varying grades was separated by placing the sands in specially designed tubes and centrifuging for 2 h at 198 000 at 20 °C. For all grades of oil sand, approximately 70% of the bitumen was recovered. The recovered bitumen was compared to the residual remaining on the sand, and to that extracted by the conventional Soxhlet technique. The ultracentrifuged bitumen contained some emulsified water and a small amount of fine solids. The solvent-extracted material was water-free, but contained a small amount of residual solvent and fine solids. The ultracentrifuge caused some fractionation of the bitumen, resulting in a product slightly enriched in asphaltene components compared to the solvent-extracted material. The residual bitumen remaining on the sand was correspondingly slightly depleted in asphaltenes. However, as evidenced by gas Chromatographic simulated distillation data, ultracentrifugation did retain the light (180–220 °C) components of the bitumen which were lost during the solvent removal step following solvent extraction. Other analyses such as density, viscosity and elemental composition verified that ultracentrifugation resulted in some fractionation of bitumen components.     

柴油脱氮精制技术研究进展

柴油中氮化物的存在对油品安定性的影响极为严重,对油品的颜色和胶质的生成影响也很大,是成胶的主要因素之一。而且有机氮化物在燃烧过程中会造成空气污染,形成酸雨。如何脱除柴油中的氮化物,提高柴油的安定性,满足对柴油产品质量的更高要求,是目前研究的重点。柴油脱氮精制技术可分为加氢脱氮和非加氢脱氮两大类,作者综述了各种柴油脱氮精制技术的原理、优缺点以及最新的研究进展。     

柴油非加氢脱氮技术研究

柴油中氮化物的存在对油品安定性的影响极为严重,对油品的颜色和胶质的生成影响也很大,是成胶的主要因素之一。有机氮化物在燃烧中会造成空气污染,形成酸雨。如何脱除柴油中的氮化物,提高柴油的安定性,满足对柴油产品质量的更高要求是目前研究的重点。作者综述了各种柴油脱氮精制技术的原理、优缺点。     

Bitumen—sand interaction in oil sand processing

Bitumen—sand interaction was studied as a function of pH, particle size, temperature and solvent addition to bitumen. Sand particles can be easily detached from the bitumen surface at pH> 6. At pH < 6, strong attachment between bitumen and sand is observed. The bitumen—sand interaction is also particle-size dependent: the finer the particles, the stronger the attachment. The detachment of coarse particles from bitumen can be achieved by increasing the alkalinity of the solution, but not for fine particles, indicating that the particle size is one of the critical factors affecting liberation of bitumen from sand. Increasing temperature has two effects: it is not only reduces the viscosity to facilitate bitumen liberation, but also increases the electrostatic repulsion between sand and bitumen. This is confirmed by the DLVO theory and is in agreement with the batch extraction results on real oil sands.     

微波辐射脱除柴油中碱性氮化物实验研究

提出以质量分数95％的乙醇为萃取剂,采用微波辐射脱除柴油中碱性氯化物的新方法,实验考察了微波辐射功率、辐射时间、压力、剂油比对脱氮效果的影响。结果表明,在功率为412．5 W,辐射时间为6min,压力为0．5 MPa,剂油体积比为0．5时碱性氮脱除率可达58．6％。该方法与传统实验方法相比工艺简单、反应时间短、清洁无污染。     

Performance of a diesel generator fuelled with palm oil

Pure palm oil may be employed in diesel engines as an alternative fuel. Engine performance and emissions were influenced by basic differences between diesel fuel and palm oils such as mass based heating values, viscosity, density and molecular oxygen content. The high viscosity of palm oil resulted in poor atomisation, carbon deposits, clogging of fuel lines and starting difficulties in low temperatures. When heated at 100 °C palm oil presented lower viscosity, better combustion and less deposits. Tests were conducted in a naturally aspirated MWM 229 direct injection four-stroke 70 kW diesel-generator fueslled with 100% palm oil.     

High quality diesel by hydrotreating of atmospheric gas oil/light cycle oil blends

An improved process for high-quality diesel fuel production by hydrotreating atmospheric gas oil (SRGO) and light cycle oil (LCO) blends is presented in this paper. For this purpose, a set of blends of 5, 10 and 15% by volume of LCO with final boiling points of 300, 325 and 350 °C with a full range gas oil (FBP 350 °C) was hydrotreated in a pilot plant at 340-380 °C, 5.4 MPa, 2.5 h⁻¹ LHSV using a commercial Co-Mo catalyst. A relationship between the concentration of refractory sulfur compounds (those boiling above 316 °C) and aromatics content in the feedstock with the hydrotreating temperature required for meeting a 0.05% sulfur specification was found.The experimental data obtained during the desulfurization was quantitatively represented by a 1.50 to 1.56 order rate equation, with activation energies between 18.9 and 34.1 kcal/mol, depending on the feedstock.     

Enhancement of media filter performance with coagulant use for treatment of diesel oil contaminated surface water

The objective of this study was to investigate the effect of coagulant addition on the filter performance and effluent quality during media filtration of surface water contaminated with diesel oil. A pilot scale multi-media filter system was operated under constant head conditions and at a constant loading rate of 30 L/min. The tests were conducted with and without coagulant addition prior to filtration of the surface water contaminated with diesel oil. Each filtration run was continued until the pressure drop increased to 0.7 bar. The source water with a turbidity of 10-15 NTU was prepared by mixing bentonite clay with tap water. The effect of coagulant addition on the performance of a multi-media filter for treatment of diesel oil contaminated source water was evaluated based on pressure change, filter run time before the filter clogged, and turbidity removal. The coagulant addition significantly improved the operational time of the media filter by reducing the rate of clogging. Both turbidity and PHC removal was achieved during the runs with coagulant addition.     

Deep desulfurization of diesel oil oxidized by Fe (VI) systems

Fe (VI) compound, such as K₂FeO₄, is a powerful oxidizing agent. Its oxidative potential is higher than KMnO₄, O₃ and Cl₂. Oxidation activity of Fe (VI) compounds can be adjusted by modifying their structure and pH value of media. The reduction of Fe (VI), differing from Cr and Mn, results in a relatively non-toxic by-product Fe (III) compounds, which suggests that Fe (VI) compound is an environmentally friendly oxidant. Oxidation of model sulfur compound and diesel oil by K₂FeO₄ in water-phase, in organic acid and in the presence of phase-transfer catalysts is investigated, respectively. The results show that the activity of oxidation of benzothiophene (BT) and dibenzothiophene (DBT) is low in water-phase, even adding phase-transfer catalyst to the system, because K₂FeO₄ reacts rapidly with water to form brown Fe(OH)₃ to lose ability of oxidation of organic sulfur compounds. The activity of oxidation of the BT and DBT increases markedly in acetic acid. Moreover, the addition of the solid catalyst to the acetic acid medium promotes very remarkably oxidation of organic sulfur compounds. Conversions of the DBT and BT are 98.4% and 70.1%, respectively, under the condition of room temperature, atmospheric pressure, acetic acid/oil (v/v) = 1.0, K₂FeO₄/S (mol/mol) = 1.0 and catalyst/K₂FeO₄ (mol/mol) = 1.0. Under the same condition, diesel oil is oxidized, followed by furfural extraction, the results display sulfur removal rate is 96.7% and sulfur content in diesel oil reduces from 457 ppm to 15.1 ppm.     

Combustion characteristics of droplets composed of light cycle oil and diesel light oil in a hot-air chamber☆

Development of gas turbines fueled with light cycle oil (LCO) and oil mixture of LCO and diesel light oil (LO) requires an understanding of the droplet burning and vaporization characteristics of those oils. The present study is devoted to comparing the burning characteristics of isolated fuel droplets composed of an LCO and an LO. The tests were conducted in an atmospheric hot-air chamber preset at 1173 K, and the examined LCO had a lower cetane number but higher volatility and aromatics content compared to LO. It was demonstrated that the burning of the LCO droplet was sootier, while that of the LO droplet was more disruptive. At the tested temperature, coke formation was indistinct for both the oils, whereas slightly higher ignition delay time was shown for the LO droplet. The microexplosive burning more or less complicated the time-series droplet size d, an explicit burning rate constant, however, was still definable according to the d²-law to show the overall regression speed of the droplet surface area d² with burning time t. The rate constant exhibited little difference for smaller LCO and LO droplets but was greater for LO when the droplet was larger. The rate constant also gradually increased with increasing the initial droplet diameter d₀, which caused the relative size d/d₀ to be unified (normalized) into a single curve by a burning time t/d₀ⁿ (1.0<n<2.0). Analysis revealed that this unification resulted from the respective overlaps of the unsteady and quasi-steady burning phases for differently sized droplets. Further, it was clarified that the unification and analysis are generally valid to isolated liquid fuel droplet burning in hot ambiences.     

Recovery of heavy oil from contaminated sand by using exfoliated graphite

Heavy oil was recovered from contaminated sand through capillary suction into exfoliated graphite with differentpacked densities by using model sands, alumina powders, with different particle sizes. For efficient recovery it was important to have an appropriate combination of average size of sand particles and packed density of exfoliated graphite. Pumping of heavy oil into exfoliated graphite occurs as a balance in an attracting capillary force between exfoliated graphite and sand, the former being stronger than the latter because of the hydrophobic nature of the surface of graphite.     

油砂分离剂的实验研究

油砂是非常规能源的一种,随着国际油价的不断攀升,油砂分离技术的研究引起广大学者的重视。本文针对内蒙古图牧吉水润型油砂进行其分离剂的研究工作。结果表明,自制分离剂FLJ中加入3%体积的沸点小于350℃的页岩油可以提高油砂洗油率的3.37%。     

微波辐射催化裂化柴油脱硫工艺研究

介绍了以过氧化氢-甲酸为氧化剂对催化裂化(FCC)柴油进行微波辐射氧化脱硫,采用正交设计和单因素方法分别考察了微波辐射压力、辐射功率、恒压时间、萃取剂与油的体积比以及复合剂油的体积比对氧化脱硫反应的影响。得出最佳的实验条件:辐射压力0.4 MPa,恒压时间6 min,辐射功率412.5 W,复合溶剂用量为柴油用量的0.08倍,萃取剂油体积比1.5。在此条件下,硫的质量分数由5538.2μg/g降至825.2μg/g,回收率达到95%以上。     

Remediation of soil contaminated with lubricating oil by extraction using subcritical water

The remediation of lubricating oil contaminated soil was investigated by extraction using subcritical water. The effects of temperature and time on extraction efficiency were studied by performing eight individual extractions and varying the subcritical water temperature (200, 225, 250, and 275 °C) and extraction time (90, 120, 180, and 240 min) in a dynamic mode. Also, a comparison was carried out of the feasibility of two operational modes, namely, dynamic and static-dynamic mode. Of the 25,088 mg/kg of lubricating oil as the total petroleum hydrocarbon (TPH) concentration in untreated soil, the residual concentration was found to be ∼500 and 235 mg/kg for after 120 min extraction in a lab-scale apparatus and 150 min extraction in a 30-fold scale-up experiment, respectively, at 275 °C in static-dynamic mode. The result of this study showed the significant effect of the static-dynamic mode on extraction efficiency. The time and volume of water needed for the static-dynamic mode were much lower than those needed for the dynamic mode. These results are of practical interest in developing the subcritical water extraction technology for extraction of lubricating oil and, in a broad sense, petroleum hydrocarbons contaminated soil.     

柴油氧化脱硫技术新进展

柴油低硫化及其含硫标准的日趋严格,是世界各国柴油产品质量与标准的发展趋势。加氢脱硫技术生产低硫柴油,存在投资大、操作费用高和操作条件苛刻的缺点,导致柴油成本大幅攀升,柴油氧化脱硫技术已成为研究热点。综述了国内外柴油氧化脱硫技术的研究进展,认为柴油氧化脱硫技术将成为今后生产超低硫清洁柴油的主要工艺之一。     

微波辐射脱除催化裂化柴油中碱性氮化物研究

在微波辐射的条件下,用乙酸-w(乙醇)=95%络合萃取催化裂化柴油中碱性氮化物,考察了剂油体积比、乙酸加入量、微波辐射功率、辐射时间、辐射压力等工艺条件对碱性氮化物脱除率和柴油回收率的影响。结果表明:在剂油体积比1.0、乙酸与95%乙醇体积比0.05、辐射压力0.5 MPa、恒压辐射时间10 min、微波功率375 W最佳反应条件下,碱性氮化物脱除率82.4%,柴油回收率90.1%,较无微波辐射的条件下,碱性氮化物脱除率显著提高。     

Characterization of oil component and solid particle of oily sludge treated by surfactant-assisted ultrasonication

The ultrasonic technique has been demonstrated to be a promising method for the disposal of hazardous oily sludge.However,the separation of oil from the surfaces of the solid particles is still difficult due to the strong in-teraction between the oil and solid particle.In this study,three types of surfactants were used to assist the ultra-sonic treatment of oily sludge.The oil component,surface composition,and structure of the solid particle were determined.The results showed that different surfactants had different oil removal abilities.In the three surfactant-assisted sonication systems,the oil removal rate increased during the starting reaction period and then decreased with longer sonication time.The results of four components analysis suggested that surfactant easy to be ionized in water posed a better removal effect on resins,while the amphiphilic surfactant preferred saturates,aromatics and asphaltenes.The morphology analysis indicated that particle size was shattered into smaller ones by the ultrasonic process,and the wettability of the solid surface also changed during this treatment.The characterization of the oil component and solid particle during surfactant-assisted ultrasonication treatment will help to better understand the separation of oil from oily sludge and improve the oil recovery efficiency from oily sludge.