泥炭在超临界水中热解的研究

以氧化钙做为催化剂和CO2化学固定剂,详细考察了Ca/C摩尔比、反应温度﹑停留时间、压力等条件对泥炭在超临界水中转化的影响。在723K,Ca/C摩尔比为0.46时,CO2被完全固定,在气相产物中只有氢气、甲烷和低碳烃,碳转化率由未添加CaO时的68.73％提高到85.36％。CaO能够促进泥炭的裂解,并对烃类的重整反应和水煤气变换反应起到催化作用。液相产物的收率在723K达到极大值,在36.5MPa,液相产物的收率是热解条件下的3倍,随着停留时间的延长,液相产物中的极性组分发生分解。     

Mathematical modelling for extraction of oil from Dracocephalum kotschyi seeds in supercritical carbon dioxide

Extraction of oil from Dracocephalum kotschyi Boiss seeds using supercritical carbon dioxide was designed using central composite design to evaluate the effect of various operating parameters including pressure, temperature, particle size and extraction time on the oil yield. Maximum extraction yield predicted from response surface method was 71.53% under the process conditions with pressure of 220 bar, temperature of 35 °C, particle diameter of 0.61 mm and extraction time of 130 min. Furthermore, broken and intact cells model was utilised to consider mass transfer kinetics of extracted natural materials. The results revealed that the model had a good agreement with the experimental data. The oil samples obtained via supercritical and solvent extraction methods were analysed by gas chromatography. The most abundant acid was linolenic acid. The results analysis showed that there was no significant difference between the fatty acid contents of the oils obtained by the supercritical and solvent extraction techniques.     

超临界水中煤与聚苯乙烯的共液化研究

在间歇式高压反应装置中,研究了兖州烟煤与塑料聚苯乙烯(PS)在超临界水中的共液化,考察了水/物料比(质量比10～30)、反应温度(360℃～430℃)和塑料添加量(10%～40%)对煤液化转化率及产物收率的影响.结果表明,随着水/物料比的增加,煤液化转化率先升高,之后变化不大;油气产率则呈上升的趋势.反应温度高于420...     

液态及超临界CO_2萃取八角茴香油的研究

本文用液态及超临界CO_2对八角茴香油进行了萃取研究，在萃取压力为20．0～25．0MPa的条件下，详细地考察了临界温度上下萃取温度和解析温度对出油率和油的表观相态的影响，结果表明，萃取温度越高和／或解析温度越低出油率越低；用液体CO_2萃取比用超临界CO_2萃取的出油率要高得多；萃取温度大约在318K以下或解析温度在临界温度以下时，萃取所得八角茴香油都有明显分层现象．     

聚乙烯塑料在连续超临界水反应器中的油化研究

在连续超临界水（SCW）反应器中考察了反应温度、停留时间和反应压力对聚乙烯（PE）降解油化的影响。实验结果表明,在120s、25MPa下,从500℃提高到550℃,液体收率呈现先升后降的趋势,在530℃达到最大值（79%）;在520℃、25MPa下,随停留时间的延长,PE裂解程度加深,产物轻质化程度提高,导致液体收率降低,停留240s时,气体收率达到43%;反应压力对产物收率的影响较小,气、液产物中烯/烷比随反应压力的增加而增大。     

煤焦油在超临界水中的改质研究

在自制的间歇式高压反应釜中，对煤焦油在超临界水中的改质反应进行了研究。考察了温度、反应停留时间、水密度等对产物分布及组成的影响。通过与N2气氛下的焦油常压热解、高压热解过程所得结果进行对比，表明煤焦油在超临界水中发生了轻质化反应，获得一定量的轻质化油品；超临界水介质的存在还对产气量和过程结焦产生一定的抑制作用。为获得较高的轻组分收率，最佳的反应条件为：450℃左右，反应停留时间约为20 min，水密度约为0.40 g/cm3在此反应条件下的轻质油收率为51.55 w%，比原料中的增加了约30％。     

超临界二氧化碳萃取羌活研究初探

研究了用超临界二氧化碳法萃取羌活的工艺条件,探讨了萃取压力、温度、时间对萃取效果的影响。萃取物最高收率为８．７５％,比水蒸汽蒸馏法收率高六倍以上。     

生物质在超临界水中热解行为的初步研究

在间歇式高压反应釜中，考察了生物质（稻杆）在超临界水中的热解行为，研究了热解产物分布随反应温度、压力以及停留时间的变化规律。结果表明,气体收率随温度升高而增加，油收率则先增加后减少，380 ℃～410 ℃产油量较大，可达28.57%；气体收率和油收率随压力升高而增加，残渣收率则明显减小，但当压力高于31.5 MPa后，油收率基本不再随压力的升高而变化；气体收率随停留时间的延长而增加，油收率则先增加后减少。     

水稻秸秆在亚/超临界乙醇中的液化实验研究

在间歇式高压反应釜中采用乙醇为溶剂在亚/超临界状态下对水稻秸秆进行液化实验研究，考察了反应温度、稻秆/乙醇比及停留时间对稻秆液化的影响，确定了反应温度325 ℃、稻秆与乙醇比为1.0/10.0（g/mL）、反应时间60 min为最佳液化条件。在此条件下，稻秆转化率为78.32%，液化油收率达55.03%；通过GC-MS对液化油进行分析，结果表明，生物油的主要成分是酚类和酯类，占总体的50%左右。液化油的热值为28.95 MJ/kg，运动黏度为5.63 mm²/s，水分含量为2.2%。     

Optimisation of steam distillation extraction oil from onion by response surface methodology and its chemical composition

Oil extraction from onion was performed by steam distillation. Response surface methodology was applied to evaluate the effects of ratio of water to raw material, extraction time, zymolysis temperature and distillation times on yield of onion oil. The maximum extraction yield (1.779‰) was obtained as following conditions: ratio of water to raw material was 1, extraction time was 2.5 h, zymolysis temperature was 36° and distillation time was 2.6 h. The experimental values agreed well with those predicted by regression model. The chemical composition of extracted onion oil under the optimum conditions was analysed by gas chromatography-mass spectrometry technology. The results showed that sulphur compounds, like alkanes, sulphide, alkenes, ester and alcohol, were the major components of onion oil.     

Thermal dissolution of Estonian oil shale

The thermal dissolution of Estonian oil shale, kukersite and thermobitumen (TBO) formed, in the presence of solvents (benzene, ethanol, water and oil shale petrol) in autoclaves was studied. In all the solvents, except subcritical water, the total yield of benzene-soluble products, TBO, has a maximum (about 90%) at an optimum residence time and thereafter decreases due to coke formation. The formation of TBO from kukersite in supercritical water, ethanol and oil shale petrol is accelerated in comparison with low-temperature pyrolysis of kukersite without any solvent. The tests carried out with TBO without the mineral matter indicate deceleration of the coke formation in comparison with the initial kukersite.     

超临界水中钾对甲醛降解过程影响的研究

为掌握生物质中钾对生物质超临界水降解过程的影响,选择生物质气化转化过程中生成的重要小分子中间产物甲醛作为研究对象,研究不同工艺条件下(反应温度400～650℃、压力23～29 MPa、停留时间4～12 s),单一钾成分(KHCO₃/K₂CO₃/KCl)或混合钾成分(KHCO₃、K₂CO₃、KCl)对甲醛超临界水降解气体产物的影响。结果表明,KHCO₃、K₂CO₃、KCl、混合钾均降低了气体产物中CO的体积分数,提高了CO₂的体积分数,但KCl的影响程度弱于其他三种钾成分。此外,由于不同钾成分均不利于气体产物中CO和H₂体积分数的提高,从而使得气体产物的热值降低。KHCO₃、K₂CO₃、KCl、混合钾均降低了H₂、CO、CO₂的产率以及气化率,其对H₂产率以及气化率的抑制程度从大到小依次为:混合钾、KHCO₃、K₂CO₃、KCl,且提高反应温度、延长反应停留时间时抑制气体生成的作用相对越明显。而当反应压力改变时,钾成分对H₂产率及气化率的影响程度变化较小。较高反应温度、较高反应压力、较长停留时间时,混合钾中各成分出现协同作用,明显抑制了气体产物的生成。     

In vivo antioxidant activity of Pinus koraiensis nut oil obtained by optimised supercritical carbon dioxide extraction

In this study, an orthogonal array design OA? (3?) was employed to optimise the conditions of supercritical carbon dioxide (SC-CO?) extraction of Pinus koraiensis nut oil. The effects of pressure, temperature and extraction time on the oil yield were investigated. Next, the fatty acid composition of the oil was examined by gas chromatography-mass spectrometry (GC-MS). The in vivo antioxidant activity of the oil was determined by estimating the superoxide dismutase (SOD) and glutathione peroxidase (GSH-Px), total antioxidant capacity (T-AOC) and the content of malondialdehyde (MDA) in rats fed with a high-fat diet. The results showed that extraction pressure and time were the main variables that influenced the oil yields. The optimal conditions with which to obtain highest yield of oil were determined to be 5760.83?psi, 50°C and 3.0?h (extraction yield was 458.5?g?kg?1); nine compounds, constituting about 99.98% of the total oil, were identified. The most abundant polyunsaturated fatty acids identified in the oil, linoleic acid and α-linolenic acid, constituted 41.79% and 15.62% of the oil, respectively. Moreover, the results on their antioxidant activities showed that the oil could improve the activities of SOD, GSH-Px and T-AOC, and reduce the content of MDA significantly, in the serum. These results indicate that P. koraiensis nut oil obtained by SC-CO? extraction had excellent antioxidant activities.     

废弃生物质在超临界水中转化制氢过程的研究

以废弃生物质转化为富氢气体为目的，使用间歇式超临界水反应器，在反应温度773 K～923 K、压力15.5 MPa～34.5 MPa停留时间1 min～30 min和Ca/C摩尔比0～0.56范围内，对木屑在超临界水条件下生成的气体组成及产率进行了考察。实验表明，Ca/C摩尔比和温度对木屑转化的影响较大。当Ca/C摩尔比为0.48时，碳的气体转化率和氢气产率提高了近一倍。温度从773 K提高到923 K，碳的气体转化率由47％提高到76％，氢气产率由4.5 mmol/g上升到6.9 mmol/g。与温度相比，停留时间和压力的影响不大。     

Extraction and separation of volatile and fixed oils from berries of Laurus nobilis L. by Supercritical CO2

Isolation of volatile and fixed oils from dried berries of Laurus nobilis L. from Tunisia have been obtained by supercritical fractioned extraction with carbon dioxide. Extraction experiments were carried out at a temperature of 40 degrees C and pressures of 90 and 250 bar. The extraction step performed at 90 bar produced a volatile fraction mainly composed of (E)-beta-ocimene (20.9%), 1,8-cineole (8.8%), alpha-pinene (8.0%), beta-longipinene (7.1%), linalool acetate (4.5%), cadinene (4.7%), beta-pinene (4.2%), alpha-terpinyl acetate (3.8%) and alpha-bulnesene (3.5%). The oil yield in this step of the process was 0.9 % by weight charged. The last extraction step at 250 bar produced an odorless liquid fraction, in which a very small percentage of fragrance compounds was found, whereas triacylglycerols were dominant. The yield of this step was 15.0 % by weight. The most represented fatty acids of the whole berry fixed oil were 12:0 (27.6%), 18:1 n-9 (27.1%), 18:2 n-6 (21.4%), and 16:0 (17,1%), with the 18:1 n-9 and 18:2 n-6 unsaturated fatty acids in particular averaging 329 microg/mg of oil.     

Supercritical fluid extraction of ecdysterone from the roots of Achyranthes bidentata BL

Ecdysterone has been found in a great many plants and animals and has some valuable pharmaceutical properties. The present study was conducted to investigate optimal conditions for the extraction of the compound by supercritical fluid extraction from the roots of Achyranthes bidentata BL. An orthogonal array design (OAD), OA(9)(3(4)), was employed as a chemometric method for optimization of the extraction of ecdysterone from the herbal medicine. Four parameters, namely, pressure and temperature of the supercritical fluid, the dynamic extraction time, and the flow rate of dimethyl sulfoxide, were studied and optimized by a three-level OAD. Determinations of the extracts were performed by high-performance liquid chromatography. The effects of the parameters were studied using analysis of variance. The results shown that the yield of ecdysterone could be influenced by the four parameters to a similar degree. The yield for DMSO-modified supercritical CO(2) was in the range from 0.65 to 1.03 mg/g under the selected conditions. In comparison with methanol-modified supercritical CO(2 )and Soxhlet extraction, a higher yield was obtained when DMSO-modified supercritical CO(2) was used.     

超临界流体萃取-GC-MS分析西黄丸中挥发性成分

建立西黄丸中挥发油成分乙酸辛酯的含量测定方法,为西黄丸的质控标准提供依据。方法:超临界CO2萃取西黄丸中挥发油成分,采用气相色谱法测定乙酸辛酯含量;研究压力、温度、时间和粒度因素对挥发油得率与乙酸辛酯含量的影响,并进行了化学计量学分析。采用GC-MS分析了适宜条件的挥发油的成分。综合考虑挥发油得率和乙酸辛酯含量双指标,确定的西黄丸挥发油萃取条件为:粉碎粒度为80目,萃取压力为25 MPa,温度为40℃,时间为2 h。在此条件下,挥发油得率达到7.76%,乙酸辛酯含量达到0.72 mg·g^-1。通过指纹图谱、主成分分析(PCA)、正交偏最小二乘判别分析(OPLS-DA)化学计量学分析可知,不同萃取条件对所提取的挥发油物质组分及其含量没有显著性差异。GC-MS鉴定出的主要成分有(1S-endo)-2-甲基-3-亚甲基-2-(4-甲基-3--3-戊烯基)-二环[2.2.1庚烷、10α-羟基日本刺参萜、(±)-麝香酮、4-亚甲基-2,8,8-三甲基-2-乙烯基-双环[5.2.0]壬烷和2-甲基-4-(2,6,6-三甲基-1-环己烯-1-基)丁醛。结论:西黄丸挥发油成分适宜萃取条件,及建立的乙酸辛酯含量测定方法准确、可靠,为有效控制西黄丸质量,完善其质量标准及进一步的药效成分研究提供了科学依据。     

Pyrolysis of asphaltenes and biomarkers for the fingerprinting of the Amoco-Cadiz oil spill after 23 years

The geochemical technique of asphaltenes pyrolysis was successfully applied to the long-term monitoring of the Amoco-Cadiz oil spill 23 years after the wreck in the salt marshes of Île Grande, Northern Brittany, France. This method allows the reconstitution of the saturated fraction of the original oil from the asphaltenes fraction of severely degraded oil residues. The results showed that the oil reached a degradation rate of 60% relatively to the initial oil. The asphaltenes pyrolysis generated a gas chromatographic profile very similar to the original Amoco-Cadiz oil. In the biomarkers fraction, gas chromatographic/mass spectrometric (GC-MS) analyses demonstrated that terpanes were conserved whereas steranes were partly degraded. We also showed that the class of seco-hopanes biomarkers are conserved and can be used in the long-term monitoring of oil pollutions.     

超临界水中聚乙烯油化的研究

采用125mL间歇式高压釜反应器，在超临界水条件下考察了反应温度、反应时间、水/聚乙烯比和水填充率对聚乙烯降解油化的影响。实验结果表明,聚乙烯在超临界水中迅速降解，油收率可达90%以上；随温度从450℃提高到480℃，油收率从91.4％下降到61.7％，气体收率从1.9％提高到27.7％；在450 ℃反应时间从1 min延长到30 min时，油收率略有下降，油品中C7-11组分所占比例增大一倍。水/聚乙烯比和水填充率的增加在一定程度上对聚乙烯的降解起抑制作用。     

Comparison and optimisation of biodiesel production from <Emphasis Type="Italic">Jatropha curcas</Emphasis> oil using supercritical methyl acetate and methanol

In this study, biodiesel has been successfully produced by transesterification using non-catalytic supercritical methanol and methyl acetate. The variables studied, such as reaction time, reaction temperature and molar ratio of methanol or methyl acetate to oil, were optimised to obtain the optimum yield of fatty acid methyl ester (FAME). Subsequently, the results for both reactions were analysed and compared via Response Surface Methodology (RSM) analysis. The mathematical models for both reactions were found to be adequate to predict the optimum yield of biodiesel. The results from the optimisation studies showed that a yield of 89.4 % was achieved for the reaction with supercritical methanol within the reaction time of 27 min, reaction temperature of 358°C, and methanol-to-oil molar ratio of 44. For the reaction in the presence of supercritical methyl acetate, the optimum conditions were found to be: reaction time of 32 min, reaction temperature of 400°C, and methyl acetate-to-oil molar ratio of 50 to achieve 71.9 % biodiesel yield. The differences in the behaviour of methanol and methyl acetate in the transesterification reaction are largely due to the difference in reactivity and mutual solubility of Jatropha curcas oil and methanol/methyl acetate.