催化剂对原油低温氧化的影响

在模拟地下油藏条件下,加入催化剂进行重质原油低温氧化反应实验研究,对氧化前后的气体组成及含量变化、原油组分变化进行分析.结果表明,加入催化剂后在150℃以下显著提高了原油低温氧化效率,且与未加入催化剂的低温氧化反应对比,加入催化剂后氧气消耗更多,生成二氧化碳含量增加.200℃以下原油重质组分含量下降,饱和烃、芳香烃轻质组分含量增加.     

重度原油注空气低温氧化过程研究(英文)

低温氧化反应对现场燃烧(ISC)技术点火的成功有十分重要的影响.采用高压氧化管,研究了不同温度压力下,新疆克拉玛依重度原油的低温氧化过程.结果表明,温度和压力的变化对低温氧化反应的放热程度、持续时间以及气体产物有明显影响.适合油样低温氧化反应的温度和压力分别为150℃和10MPa.此外,采用纯组分替代原油族组分进行低温氧化实验,研究低温氧化反应对原油族组分(饱和烃、芳香烃、胶质、沥青质)含量的影响.结果表明,原油所含族组分中,芳香烃组分最易被氧化,其含量由氧化前的19.17%减少到12.38%(150℃)和9.51%(250℃).随着低温氧化过程的进行,结构复杂的族组分(胶质、沥青质)的含量明显增加.实验数据对油藏实施注空气技术,以及该技术现场实施条件的确定有十分重要的指导意义.     

原油组分低温氧化机理和反应活性实验研究

分析了原油和原油组分低温氧化的机理,通过实验进行了不同油品低温氧化反应,考察了氧化反应前后原油族组成的变化,并研究了单组分(正十六烷、蜡、蒽、沥青质)在不同温度下的低温氧化速率和反应活性,得出了不同原油组分的低温氧化反应的活化能。结果表明,稠油较轻质油有更好的氧化反应活性,在较低温度下稠油更容易被氧化,原油中不同组分及含量是影响氧化反应活性和氧化反应速率的重要因素,重组分的沥青质和长链烷烃在低温下(70~90℃)氧化活性较高,正十六烷和蒽反应活性较之重组分低。揭示了原油组分低温氧化反应机理以及不同组分氧化反应活性的区别,为油田注空气工艺方案设计提供基础。     

马瑞原油在空气和氮气中的热解-氧化性能

低温氧化是注空气采油及原位燃烧采油技术中的重要化学反应,为深入认识原油在有氧环境下复杂热反应过程中的低温氧化特性,我们采用热重/差热分析法(TG/DTA)研究了线性升温和等温条件下马瑞(Merey)原油的热反应行为。 结果表明,Merey原油在空气及线性升温条件下的受热过程分4个阶段:气化段、低温氧化段、热解段和高温氧化段;相邻阶段的物理、化学主导过程的重叠增加了分析原油热反应特征的难度。 升温速率提高,气化段和低温氧化段的终止温度不变;热解段和高温氧化段的终止温度以及热解段的峰温随升温速率的增加而升高。 N₂气与空气下Merey原油的热重/微分热重(TG/DTG)数据对比表明,升温速率越高,空气下的高温氧化段与热解段重叠程度越大,这有利于燃烧但会降低原油采收率。 空气下等温时的TG/DTA结果表明随升温速率增加,升温至300 ℃时的失重率降低,不利于原油轻组分的气化。 反应温度越高,气化过程时间越长,失重分数越大。 Merey原油在低于300℃时低温氧化反应不是主导反应。     

PdO-CeO2复合氧化物催化剂的CO低温氧化

采用共沉淀法制备了一系列不同Pd含量的PdO-CeO2复合氧化物催化剂, 并考察了该催化剂的CO低温氧化反应催化性能. 运用X射线衍射(XRD), 物理吸附(BET), CO化学吸附, 程序升温还原(TPR), 脉冲反应等技术对催化剂进行了表征. XRD结果表明, 焙烧温度从400 ℃升高到800 ℃, 有利于CexPd1-xO2-δ固溶体的形成. 然而焙烧温度升至1000 ℃时, 导致Pd从固溶体中析出. 催化剂的CO氧化活性(TOF)与CexPd1-xO2-δ固溶体的含量存在一定的对应关系. 随着CexPd1-xO2-δ固溶体含量的增加, CO氧化的TOF值大, 可见CexPd1-xO2-δ固溶体的形成对CO氧化活性有着主要的贡献. 在催化剂焙烧温度相同的条件下, 催化剂的CO氧化活性与Pd粒子大小无对应关系. 脉冲反应进一步说明PdOx的CO氧化活性高于金属Pd.     

PdO-CeO2复合氧化物催化剂的CO低温氧化

采用共沉淀法制备了一系列不同Pd含量的PdO-CeO2复合氧化物催化剂,并考察了该催化剂的CO低温氧化反应催化性能.运用X射线衍射(XRD),物理吸附(BET),CO化学吸附,程序升温还原(TAR),脉冲反应等技术对催化剂进行了表征.XRD结果表明,焙烧温度从400 ℃升高到800℃,有利于CexPd1-xO2-δ固溶体的形成.然而焙烧温度升至1000℃时,导致Pd从固溶体中析出.催化剂的CO氧化活性(TOF)与CexPd1-xO2-δ固溶体的含量存在一定的对应关系.随着CexPd,1-xO2-δ固溶体含量的增加,CO氧化的TOF值大,可见CexPd1-xO2-δ固溶体的形成对CO氧化活性有着主要的贡献.在催化剂焙烧温度相同的条件下,催化剂的CO氧化活性与Pd粒子大小无对应关系.脉冲反应进一步说明PdOx的CO氧化活性高于金属Pd.     

原油空气氧化前后多环芳烃组分的气相色谱-质谱分析

采用柱层析法对空气氧化前后的原油进行族组分分离,利用气相色谱-质谱(GC-MS)分离测定其芳香烃组分,分析多环芳烃组分的变化.结果表明,随着氧化过程的进行,烷基化多环芳烃占多环芳烃的含量从氧化前的71.5%增加到92.0%(175℃)和90.2%(225℃).轻质组分萘和菲的优势逐渐被重质组分艹屈取代.侧链少的多环芳烃比侧链多的更易氧化.氧化后,其他稠环化合物蒽、萤蒽、芘、苯并蒽含量降低,苯并萤蒽含量增加;苯并芘在175℃氧化后含量降低,而在225℃氧化后含量增加.与此同时,175℃氧化后生成了原油所不含有的三芳甾烃、联苯和苯并呋喃.     

凝结热对低阶煤低温氧化过程的影响

选用Pulse Calorimeter仪器，研究了低阶煤在干燥氧气下低温氧化过程的反应热和相对湿度为80％的氮气下凝结热与温度的变化，以研究凝结热对低阶煤低温氧化过程的影响。结果表明,随着温度的上升体系的反应热增加，而凝结热减少。在26℃~60℃的低温下，体系的凝结热明显高于反应热。因此，低温下凝结热是影响低阶煤的低温氧化过程的重要因素。研究还得到了低阶煤在干燥氧气下低温氧化过程的动力学方程及活化能。     

V-Ce/TiO2脱硝催化剂的SO2中毒机理研究

通过表相、体相硫组分的表征分析,结合不同温度下含硫气氛下的活性演变及原位红外研究,获得了VCe(0.1)/TiO2催化剂在180、240和300℃下含硫氛围的NH3-SCR反应中毒机理. 180℃下催化剂上沉积了大量的硫酸氢铵和少量的金属硫酸盐,共同导致在8 h内活性从77.8%降至51.2%,热再生后的活性测试结果表明硫酸氢铵的沉积导致了催化剂活性降低8.3%,金属硫酸盐的沉积导致了催化剂活性降低18.3%.原位红外结果表明中毒后催化剂在180℃下的NH3-SCR反应遵循L-H反应路径.随着温度升高至240、300℃,催化剂上沉积的硫酸氢铵逐渐减少,金属硫酸盐含量增加.不同温度下的抗硫活性结果表明,低温NH3-SCR反应需要较高的氧化还原性能,中高温NH3-SCR反应则需要较高的酸性,金属硫酸盐的生成导致了氧化还原性能降低、酸性增加,因此低温NH3-SCR活性大幅降低,中高温活性则能保持在100%.     

稠油的可控氧化热采：MnO2催化剂上的重油低温氧化分解行为

采用MnO2纳米催化剂促进稠油重组分的低温氧化裂解及高温氧化生热,进而促进火烧油层技术在超稠油油藏开发中的应用,提高火烧油层技术的采收率.结果表明, MnO2促进了稠油的低温裂解,高温生热量并不随燃料沉积量的减少而降低. MnO2的加入促进了低温下小分子的生成,并使高温氧化反应更加温和,提高了高温产物的氧化度.相比无催化剂的氧化反应, MnO2使稠油的低温氧化和高温氧化的表观活化能分别降低了10–30 kJ/mol和20–40 kJ/mol.     

A comprehensive analysis of the properties of light crude oil in oxidation experimental studies

The analysis of light crude oil for oxidation reaction experiments is a kind of important technological for evaluating an air injection project in a reservoir. In this study, the paper comprehensively analyzes the variations of Jilin crude oil composition comparing crude oil component’s variations before and after oxidation, and investigates the effluent gas composition and hydrocarbon, analyzes the mechanism of low temperature oxidation reaction (LTO), and rebuilds the light crude oil cracking reaction of intermediate component in a new pattern. In the early stage of the oxidation reaction, firstly, oxygen is captured by forming chemical bond in liquid hydrocarbon. And then oxygen takes part in the free radical chain reaction by forming hyperoxide and decomposes to ketones, aldehydes, alcohols, and so on. Meanwhile, chain scission reaction comes up. Research result shows that the intermediate components (C_7–17) of crude oil make great contribution to crude oil cracking. The experimental result shows that Jilin reservoir has the potential of implementing air injection project.     

Determination of gas-oil miscibility conditions by interfacial tension measurements

Processes that inject gases such as carbon dioxide and natural gas have long been and still continue to be used for recovering crude oil from petroleum reservoirs. It is well known that the interfacial tension between the injected gas and the crude oil has a major influence on the efficiency of displacement of oil by gas. When the injected gas becomes miscible with the crude oil, which means that there is no interface between the injected and displaced phases or the interfacial tension between them is zero, the oil is displaced with maximum efficiency, resulting in high recoveries. This paper presents experimental measurements of interfacial tension between crude oil and natural gases (using a computerized drop shape analysis technique) as a function of pressure and gas composition at the temperature of the reservoir from which the crude oil was obtained. The point of zero interfacial tension was then identified from these measurements by extrapolation of data to determine minimum miscibility pressure (MMP) and minimum miscibility composition (MMC). The gas-oil miscibility conditions thus obtained from interfacial tension measurements have been compared with the more conventional techniques using slim-tube tests and rising-bubble apparatus as well as predictive correlations and visual observations. The miscibility pressures obtained from the new VIT technique were 3-5% higher than those from visual observations and agreed well with the slim-tube results as well as with the correlations at enrichment levels greater than 30 mol% C2+ in the injected gas stream. The rising bubble apparatus yielded significantly higher MMPs. This study demonstrates that the VIT technique is rapid, reproducible, and quantitative, in addition to providing visual evidence of gas-oil miscibility.     

Characterization of a heavy oil–propane system in the presence or absence of asphaltene precipitation

When a light hydrocarbon solvent is injected into a heavy oil reservoir under a sufficiently high reservoir pressure, asphaltene precipitation occurs so that the heavy oil is in situ deasphalted during a hydrocarbon solvent-based heavy oil recovery process. The physicochemical properties of this in situ deasphalted heavy oil are rather different from those of the original crude oil in the heavy oil reservoir. In this paper, a heavy oil sample is saturated with a typical light hydrocarbon solvent (i.e., propane) under different saturation pressures in a see-through windowed high-pressure saturation cell. The heavy oil–propane system is characterized by measuring and comparing several important physicochemical properties of the propane-saturated heavy oil samples under different saturation pressures and the flashed-off heavy oil samples, such as the solubility, oil-swelling factor, density, viscosity, asphaltene content, hydrogen and carbon aromaticities. When the heavy oil is saturated with propane at P ≤ 780 kPa and T = 20.8 °C, there is no observable asphaltene precipitation and deposition under a microscope camera. The respective properties of the propane-saturated heavy oil samples taken from the upper and lower parts of the saturation cell are measured and found to be essentially the same within the experimental errors so that the entire system is considered to be almost homogeneous. If the saturation pressure is increased to P = 850 kPa, strong asphaltene precipitation occurs and some large asphaltene particles are deposited onto the bottom of the saturation cell. In this case, the heavy oil is deasphalted and the flashed-off heavy oil has lower density, viscosity, asphaltene content, hydrogen and carbon aromaticities than those of the original heavy crude oil.     

Effects of CO2 Injection on Phase Behavior of Crude Oil

CO₂ flooding is a win-win technology, sequestrating greenhouse CO₂ while producing a significant amount of crude oil to help defray the cost of CO₂ sequestrating and enhancing oil recovery. However, due to the difference of sedimentary environment and poor properties of formations, physical properties of the crude oil and the effect of CO₂ flooding are not always satisfactory in most oilfields of China. Therefore, in this article, to improve the understanding of the oil recovery mechanisms and feasibility of CO₂ flooding in China, based on the oil and gas of Mao-3 oilfields, phase behavior of the CO₂ and crude oil system was investigated. Parameters like saturated pressure, volume factor, gas oil ratio, and viscosity were measured and their relationships analyzed. Results show that crude oil of Mao-3 reservoir and CO₂ has good mutual dissolution under reservoir conditions, and CO₂ could expand the oil and reduce the oil viscosity greatly. As a result, formation energy could be enhanced and flow characteristics of the oil could be improved by CO₂ flooding.     

改进的广义回归神经网络用于基于气相色谱法的原油密度定量分析

在油气勘探开发领域,快速识别储集层原油性质对于工程技术人员有非常重要的指导意义.地球化学录井技术是用于判断储集层原油性质的常规手段,能为储集层综合评价提供专业认识.该文研究了地化录井中的岩石热解分析和气相色谱分析的原理,提出了一种利用色谱谱图对原油密度进行定量分析的新方法,再结合原油性质密度划分标准,可快速判断储集层原...     

Characterization of complex assemblages of organic acids in geological samples by negative electrospray ionization mass spectrometry using a double‐focusing magnetic sector field mass spectrometer

Four different geological sample types (a crude oil, a crude oil asphaltene, a reservoir core extract and a reservoir core asphaltene) have been characterized by negative ionization electrospray mass spectrometry at low and high mass resolution using a double‐focusing magnetic sector field mass spectrometer. The mass range, shape of the spectra and the signal distribution of the acidic constituents as well as the average molecular weights, the total ion abundance and signal intensity in the spectra were compared for the different sample types. Nominal mass classes have been evaluated and Kendrick mass plots were generated in order to identify homologous series. For the crude oil sample, accurate mass assignments were made by high‐resolution double‐focusing magnetic sector field mass spectrometry (DFMSFMS) and were compared with those obtained by negative ion electrospray ionization (ESI) Fourier transform ion cyclotron resonance mass spectrometry (FTICRMS). With both instrument types, compounds with the molecular composition C_nH_2n+zO₂, among which carboxylic acids predominated, were the main acidic compound class detectable in negative ESI mass spectra. Good agreement was achieved for the double bond class distribution and the carbon number distribution of the O₂ class. In addition, minor compound classes could be identified using FTICRMS. Copyright © 2010 John Wiley & Sons, Ltd.     

青海出露油砂沥青的烃类组成分析

利用气相色谱(GC)和气相色谱／质谱联机(GC／MS)检测了青海出露油砂沥青的烃类组成与分布。结果表明，其为陆源湖相有机质生成的原油经生物氧化降解形成的。由于所处的独特地理、地质环境，其生物氧化降解程度低，饱和烃含量甚高，分布规整，轻质组分很多，明显不同于其它地区的油砂沥青。鉴于其特殊的化学组成与分布，该油砂矿必须采用新的方式进行开采。     

Enriching Oryzanol in Rice Bran Oil using Membranes

Oryzanol present in rice bran is associated with various physiological functions. However, these beneficial ferulate esters are lost to the extent of 87% during conventional refining of crude rice bran oil. In the present investigation, oryzanol enrichment in rice bran oil was attempted using nonporous polymeric membranes under undiluted as well as hexane-diluted conditions with different (crude, refined, and model oil) systems varying widely in their oryzanol content. During membrane processing, oryzanol content in the refined rice bran oil increased from 2,420 to 7,340 mg/kg (approximately threefold enrichment). While processing crude oil and model oil systems, the oryzanol content in the oil improved from 17,600 to 27,300 mg/kg and 20,400 to 30,300 mg/kg, respectively. The enrichment of oryzanol was due to its moderate rejection by the nonporous hydrophobic membrane owing to the hydrophilic nature of the ferulic esters. Hexane dilution improved the oil flux by one order of magnitude but reduced the selectivity. Enriched rice bran oil may find wider applications in the pharmaceutical, therapeutic, and dietary preparations as well as in producing standard cooking oil with guaranteed oryzanol content.     

Physicochemical properties and fatty acid composition of Juglans regia cultivars grown in Serbia

Tree cultivars (Jupiter, Sejnov, and Elit) of walnut (Juglans regia L.) were collected during the 2004 harvest from Cacak, Central Serbia. The chemical composition, including moisture, total oil content, crude protein, ash, and carbohydrates, was determined. Afterwards, two techniques of oil extraction were implemented: cold pressing extraction and organic solvent extraction. Iodine value, saponification value, acid value, and peroxide value of obtained walnut oils were analyzed. The fatty acid composition of the walnut oils was determined using gas chromatography with flame ionization detector. The oleic acid content of the oils ranged from 15.9–23.7% of the total acids, while linoleic acid content ranged from 57.2–65.1% and the linolenic acid from 9.1–13.6%. The process of oil extraction had no significant effect on content and composition of fatty acids. Published in Khimiya Prirodnykh Soedinenii, No. 2, pp. 118–120, March–April, 2008.     

Thermal kinetics study of light oil oxidation using TG/DTG techniques

In this study, the oxidation behavior of crude oils in the presence and absence of rock cuttings was investigated by thermogravimetry/derivative thermogravimetry (TG/DTG) techniques. Prior to these tests, the composition of cuttings and properties of crude oils were analyzed. Three obvious reaction regions were observed from the TG/DTG curves which are recognized as low-temperature oxidation (LTO), fuel deposition (FD), and high-temperature oxidation. The effects of light components (C_7–15), heavy fractions (asphaltene, paraffin, resin), and cutting on oil oxidation behavior were analyzed. Kinetic analysis of crude oils and oil + cutting mixtures was performed by Arrhenius method, and the data were analyzed at last. Results show that high content C_7–15 hydrocarbons can provide negative effect on the LTO behavior of crude oil. On the contrary, the high content unsaturated heavy hydrocarbons including asphaltene, paraffin, and resin are benefit for the oxidation performance. In addition, a shortened FD stage and higher peak temperature in LTO region are observed by addition of cutting. Cutting especially clay in it plays an active role of catalyzing in oil oxidation reaction.