胜利褐煤二硫化碳-丙酮萃取物的超临界醇解物的GC/MS分析

胜利褐煤经CS2-丙酮混合溶剂(V/V=1 1)萃取获得萃取物EM,EM在300℃的甲醇中热溶2 h获得热溶物ET.对EM和ET进行了气相色谱/质谱联用(GC/MS)分析,在EM中有43种GC/MS可检测组分,而在ET中检测到了132种有机化合物,其中包括32种在EM中未检测到的甲酯类化合物(MAs)和16种酚类化合物.分析了MAs和酚类化合物的形成机理,得出了胜利褐煤CS2-丙酮可溶大分子化合物中可能存在的4种结构单元.本文提供了一种研究煤中可溶大分子化合物的有效方法,弥补了GC/MS在检测大分子化合物时的不足.     

三核银穴合物的合成及其相应穴醚盐酸盐的电离喷雾质谱研究

在Ａｇ＾＋模板作用下，三（３－氨基丙基）胺与２，６－二甲酰基吡啶进行（２＋３）希夫碱缩合，合成了一个全新的三核银（Ｉ）穴合物，将此穴合物还原后得到一个新奇的穴醚。用电离喷雾质谱新技术研究了该穴醚盐酸盐的裂解机理。     

GC/MS分析鸡毛松枝精油的化学成分

为了促进罗汉松科植物鸡毛松在医药、农药和精细化工等领域中的应用,本研究利用水蒸气蒸馏法提取鸡毛松枝精油,进一步采用气相色谱-质谱联用(GC/MS)方法对其化学成分进行分析,分离鉴定出18种化学成分,主要有β 石竹烯(2 03%)、大根香叶烯(61 39%)、γ 榄香烯(12 14%)、β 杜松烯(2 14%)和rimuene(7 66%)。已鉴定化合物占总离子流出峰面积的92 69%,其中大部分是萜烯类化合物。     

GC／FTIR／FID联用鉴定复杂精油组分

采用气红联用 (GC /FTIR /FID)和气质联用 (GC /MS)的方法 ,对烟用精油 -缬草油挥发成分进行分析。着重讨论了GC /FTIR /FID联用对分析复杂精油的应用。通过不同波数区的官能团重建图和红外谱图与质谱的相互验证的方法 ,提高了分析精油成分定性和定量的准确性。     

超临界CO2萃取丁香花蕾的工艺研究及对萃取物的GC—MS分析

本文应用超临界二氧化碳技术 ,研究了丁香花蕾的最佳萃取工艺。结合温度、压力、堆积密度、CO2 流量等因素对丁香花蕾提取物的萃出率的影响 ,采用四因素三水平的正交设计 ,得出丁香花蕾油萃取的最佳工艺条件为 :压力30MPa ,温度 4 5℃ ,CO2 流量 10L/h ,低堆积密度。作者还对萃取出的丁香花蕾油进行了GC—MS成分分析     

蜂蜡净油挥发性成分的分析和研究

采用气相色谱 质谱联用技术 ,通过质谱库检索并结合保留指数 ,对蜂蜡净油的挥发性成分进行了定性分析 ;同时采用气相色谱技术 ,对其中的大部分挥发性成分进行了定量分析。共检出 75个组分。主要成分为 :1,8 桉树脑 (1.70 % )、芳樟醇 (6 .5 3% )、乙酸芳樟酯 (12 .5 1% )、乙酸松油酯 (1.85 % )、苯乙酸甲酯 (2 .5 9% )、苯乙酸乙酯 (2 .6 0 % )、苯甲醇 (5 .6 7% )、丁酸苯乙酯 (2 .11% )、洋茉莉醛 (1.0 5 % )、苯乙酸 (14 .79% )、香兰素 (8.0 1% )、苯乙酸苄酯 (10 .97% )、肉桂酸苄酯 (2 .5 5 % )等。     

一种变种留兰香精油化学成分的研究

本文采用GC/MS法 ,研究了一变种留兰香精油的化学成分。鉴定出 39种化合物 ,主要成分为胡椒烯酮醚(30 .5 11) %、1,8-桉叶素 (2 8.791% )、烯 (9.986 % )、β -月桂烯 (8.4 81% )和 β -蒎烯 (4 .796 % ) ,而作为一般留兰香油主成分的香芹酮则未能检测到。     

A GC–MSD method for analysis of dimethyl sulfate in palm oil-based esterquat

Dimethyl sulfate (DMS) is a quarternizing agent for esteramine used for the synthesis of esterquat. To date there is no reliable published method for quantification of DMS in palm-based esterquat. Esterquat is used in the formulation of personal care and textile cleaning. The process of quaternization is usually incomplete and there will be unreacted DMS. This work presents a new simple method involving solvent extraction of DMS followed by analysis with gas chromatography–mass spectrometry detector to quantify the unreacted DMS. This method was validated as per International Council for Harmonization requirements. This novel method showed good repeatability (relative standard deviation [RSD] < 5%) and inter-day with different analyst reproducibility (RSD < 5%). The limits of detection and quantification were 5 and 10 μg mL⁻¹, respectively. The accuracy of the method was evaluated by the analysis of spiked samples and it was found that good recovery was found at spiking levels of 20, 30, and 50 μg mL⁻¹ with % recovery falling within the 80%–120% acceptable limit. However, at 10 μg mL⁻¹, the percentage recovery was slightly below the recommended limit.     

Catalytic Pyrolysis of Pine Wood Sawdust to Produce Bio-oil: Effect of Temperature and Catalyst Additives

In this work, non-catalytic pyrolysis of Turkish pine (Pinus brutia Ten.) wood sawdust was performed in a fixed-bed reactor at various temperatures to obtain the optimum conditions to achieve a maximum bio-oil yield. The highest yield of bio-oil was obtained about 46 wt% at 550°C for non-catalytic pyrolysis. At the optimum conditions, the effects of different catalyst types (KOH, ZnCl₂, and ZnO) and amount of catalyst (5, 10, 15, and 20 wt%) on the pyrolysis product yields and bio-oil properties were investigated. The presence of catalysts changed the product distribution considerably. Increasing the amount of catalyst led to a decrease in the yield of liquid product, while the gas and char yields increased compared to non-catalytic pyrolysis. The chemical compositions of bio-oil were determined with GC-MS analyses. It was determined that bio-oils contain a large variety of organic compounds, such as furans, aldehydes, ketones, phenols, acids, benzenes, alcohols, alkanes, and polycyclic aromatic hydrocarbons (PAHs). The catalysis by KOH significantly increased the levels of phenols, while it reduced the formation of acids and aldehydes. ZnCl₂ produced bio-oil with high percentages of aldehydes. Moreover, ZnO reduced the proportion of PAH in the bio-oil. These results demonstrated that bio-oils could improve with a catalyst. Therefore, catalyst selection for high bio-oil quality is crucial in industrial applications.