苏码罐采样-气相色谱-质谱法测定环境空气中三甲胺的含量北大核心CSCD

针对现行的三甲胺分析方法在采样、样品保存、前处理等方面存在的不足,在优化预浓缩仪的冷阱捕集温度和填料、色谱和质谱条件等基础上,提出了苏玛罐采样-气相色谱-质谱法(GC-MS)测定环境空气中三甲胺含量的方法。将采样后的苏码罐连接到自动进样器上,经预浓缩仪的三级冷阱浓缩、富集后,按照色谱、质谱条件进行分析,以质谱图和保留时间定性,外标法定量。结果表明:优化的一级冷阱捕集温度为80℃,二级冷阱捕集温度为10℃,解吸温度为240℃,二级冷阱填料为石墨化碳黑Carbopack B;色谱分析中使用GL InertCap For Amines色谱柱,柱流量为1.4 mL·min^(-1),升温速率为15℃·min^(-1),溶剂延迟时间为6.0 min。在优化的仪器工作条件下,三甲胺峰形较好,响应值较大,并且避免了残留的CO_(2)的干扰。三甲胺标准曲线的线性范围为12.5~200 nmol·mol^(-1),检出限(3.143s)为0.003 mg·m^(-3);对不同浓度水平的加标样品进行回收试验,三甲胺测定值的相对标准偏差(n=6)为0.20%~5.3%,回收率为92.1%~111%。     

罐采样-冷聚焦-气相色谱中心切割-氢火焰/质谱双检测器法同时测定空气中104种挥发性有机物

本文建立了苏码罐采样-冷聚焦-气相色谱中心切割-氢火焰离子化/质谱双检测器测定环境空气中挥发性有机物(VOCs)的方法,通过选择色谱柱和中心切割时间实现104种VOCs的良好分离,通过优化冷阱温度消除了实际样品中CO_2对目标化合物的干扰。实验结果表明,该方法目标化合物标准曲线平均响应因子均在15%以内,检出限在0.07～0.72μg/m~3范围,精密度(RSD)均在10%以内,能较好地应用于环境空气中104种VOCs的定性定量分析。     

利用热脱附/冷阱捕集提取土壤中挥发性有机物的条件研究

采用热脱附/冷阱捕集提取土壤中的挥发性有机物,以17种VOCs作为目标研究对象进行挥发性有机物的提取条件研究。试验确定的提取条件为:热脱附温度300℃,热脱附时间3 min,冷阱捕集温度–10℃。优化条件后添加水平为1 mg/kg的加标土壤样品测定结果在0.75～0.94 mg/kg之间,相对标准偏差为2.89%～7.16%。     

痕量磷化氢的冷阱二次富集机理与GC/FID分析方法研究

将火焰离子化检测器(FID)应用于二次富集气相色谱检测中构建了冷阱二次富集-GC/FID系统检测环境中痕量磷化氢的分析方法。研究了冷阱温度、载气流量、柱温箱温度和检测器温度对该系统富集检测效果的影响,讨论了磷化氢富集的机理,并将该系统应用于广州地区典型水稻田环境中结合态磷化氢(MBP)的检测。结果表明:当冷阱温度为-90℃,载气流量为1.5 mL/min,柱温箱温度为90℃,检测器温度为220℃时,系统操作条件最优。冷阱二次富集磷化氢的主要机理是富集毛细管柱(KB-Al2O3/NaSO4)对磷化氢的吸附作用,属气-固吸附。系统检出限为0.041 7 pg,精密度为4.3%。整个水稻生长周期内,水稻土中结合态磷化氢(MBP)的平均含量为120.59 ng/kg,测定结果的相对标准偏差均值为8.5%。该方法对痕量磷化氢的检测效果与使用氮磷检测器(NPD)的传统方法相近,但FID检测器的结构简单、操作方便、价格经济,使环境中痕量磷化氢的检测更容易实现,可推广应用。     

顶空进样气相色谱法检测啤酒中乙醛

建立了项空自动进样气相色谱法测定啤酒发酵液中乙醛含量的方法.检测条件优化为:顶空进样器平衡温度70℃,平衡时间30 min;色谱柱初始温度40℃,经程序升温10℃/min到180℃;柱流量1.2 mL/min,加盐量1.8g.对不同浓度的乙醛标准溶液进样测定,标准曲线证明线性良好,R2为0.999,线性范围2～64 m...     

电冷阱富集-光电离移动质谱快速检测痕量挥发性有机物

采用电动制冷机设计并搭建了一套低温富集-高温解析冷阱装置,与光电离移动质谱联用,实现了大气中痕量挥发性有机物(VOCs)快速、自动富集检测。与传统冷阱制冷方式相比,电动制冷机低温可至!196℃,体积小巧、无制冷剂消耗、便于携带。利用冷阱结合在线质谱分析了苯、甲苯和二甲苯混合气,对冷阱各参数进行了优化,结果表明:冷阱富集后苯、甲苯和二甲苯的信号强度分别提高了212、254和242倍,回收率分别达到98%、87%和85%,单样品分析时间14 min。将电冷阱结合移动式在线质谱直接分析含有39种VOCs的EPA TO-14标准混合气和室内环境空气,仪器灵敏度低于国家对室内空气中VOCs阈值。电冷阱富集在线移动式质谱可以实现大气、室内环境中痕量VOCs快速富集检测,在挥发性有机污染物现场、实时监测中具有重要的应用潜力。     

气相色谱-氮磷检测器分析痕量磷化氢

采用柱前两次冷阱富集和气相色谱 -氮磷检测器 (GC -NPD)法 ,测定了大气环境中存在的痕量磷化氢 ;在原有的冷阱富集装置中配置温度控制仪和夹套冷阱控温 ,可在线检测并控制磷化氢的富集温度 ,并可选择不同的温度范围将其与厌氧环境中普遍存在的甲烷气体分离 ;该法的检出限为1.25×10-2pg。     

电子制冷预浓缩-双柱气相色谱-质谱/氢火焰检测器法测定空气中104种挥发性有机物

基于吸附剂辅助电子制冷预浓缩技术，建立了多维切割双柱气相色谱-质谱/氢火焰离子化检测器（GC-MS/FID）同时测定环境空气中104种挥发性有机物（VOCs）的方法。将采集于苏玛罐中的环境空气样品在配有吸附剂的电子制冷预浓缩系统中富集、脱附、除水、除CO₂和浓缩，然后通过GC-MS/FID的多维切割单元将C₂~C₃组分和C₄~C₁₂组分分别引入PLOT柱和InterCap-624柱进行分离。C₂~C₃组分用FID检测，以保留时间定性、外标法定量；C₄~C₁₂组分采用电子轰击离子源质谱检测，以保留时间和特征离子定性、内标法定量。考察了冷阱吸附剂种类、辅助压力控制单元压力设置、双柱切换时间切割点等参数对分析结果的影响，优化了GC-MS/FID条件，并评估了在此优化条件下的方法性能。104种VOCs在0.0446~0.892 μmol/m³范围内线性关系良好，相关系数（r）为0.9984~0.9999，对0.0446 μmol/m³和0.223 μmol/m³水平的混合标准气体重复6次进样，平均回收率为86.4%~116.1%，相对标准偏差为0.9%~11.3%；方法的检出限为0.145~1.90 μg/m³，定量限为0.435~5.70 μg/m³。该法稳定性好，灵敏度高，操作简便，可用于环境空气中104种VOCs的测定。     

冷凝收集-离子色谱法测定呼出气中的有机酸和阴离子

建立了一种非侵入式冷凝收集-离子色谱方法测定人体呼出气中乳酸、甲酸、乙酸、丙酮酸、Cl^-、NO₂^-、NO₃^-、SO₄^2-。搭建自制呼出气冷凝装置,该装置包括吹气口、与吹气口相连的单向阀和流量计、置于半导体冷凝装置中的冷阱以及一次性冷凝收集管。通过呼出气冷凝装置对人体呼出气进行收集,利用离子色谱对冷凝液(EBC)中有机酸和阴离子的含量进行检测。优化采集冷阱温度和采集流量,得到冷阱最佳冷凝温度为-15℃,呼气流量为15 L/min。采用1.5 mmol/L碳酸钠和3 mmol/L碳酸氢钠混合溶液作为流动相,泵流速为0.8 mL/min,分析柱为IC-SA3 (250 mm×4.0 mm),柱温为45℃。8种有机酸和阴离子的线性范围均为0.1～10.0 mg/L,相关系数均≥0.999 3。在进样量为100μL时,方法的检出限为0.001 7～0.015 0 mg/L(S/N=3),定量限为0.005 7～0.050 0 mg/L(S/N=...     

离子液体富集-热脱附-气相色谱-质谱联用法测定空气中半挥发性有机物

利用离子液体1-丁基-3-甲基咪唑双三氟甲烷黄酰亚铵盐[BMIM][NTF2]作为富集剂,建立了离子液体富集-热脱附-气相色谱-质谱联用(ILs-ATD-GC-MS)快速测定室内空气中5种邻苯二甲酸酯类物质(DMP、DEP、DBP、BBP、DEHP)和2种多溴联苯醚(PBDE-28、PBDE-47)半挥发性有机物的方法。采用白色担体负载[BMIM][NTF2]离子液体,主动采样的方式来进行采样,离子液体的负载量为15%,采样流量为1 L/min,采样时间为90 min;热脱附的条件为:二阶段脱附模式,脱附气体为氦气;第一阶段样品管脱附,脱附温度280℃,脱附时间15 min,脱附流速50 mL/min;冷阱捕集温度0℃,第二阶段冷阱脱附,脱附温度280℃,脱附时间5 min,升温速率40℃/s,阱前阱后均无分流;六通阀温度230℃,传输线温度280℃;气相色谱质谱的条件为:初始温度为100℃保持1 min,以10℃/min的速率升至200℃,再以6℃/min的速率升至250℃,保持10 min。本方法的检出限为0.001~0.014 ng,回收率为97.1%~113.8%,相对标准偏差RSD为3.3%~9.9%。对来自于北京市区内10个办公室的空气样品进行了测定。在这些样品中,主要检测到DMP,DEP,DBP,DEHP这4类物质,浓度在189.4~2074 ng/m3之间。结果表明,离子液体能够作为空气中SVOCs的富集材料,进一步开拓了离子液体应用的领域。     

油浆高温快速裂解过程的气固相产物研究

采用高频炉快速热解装置研究油浆的高温快速热解特性,考察了热解温度、氮气流量对气固相产物的组成和产率的影响。温度是影响气相产物产率的关键因素,气相产物主要为甲烷、氢气和乙烯,升高温度可提高甲烷和氢气的产率,而乙烯产率受高温下二次反应的影响在800℃到达最大值后逐渐降低,乙烷、丙烯产率较小且受二次反应的影响在700℃到达最大值后逐渐降低,温度高于800℃时会有少量乙炔生成且升温可提高乙炔产率。增加氮气流量可降低甲烷、氢气分压,缩短乙烯、丙烯等在高温区的停留时间,从而增加气相产物的产率。积炭产率随热解温度升高迅速增加,氮气流量的增加能够削弱二次反应从而降低积炭产率。     

毛细管多维气相色谱法分析炼厂气

用ＨＰ６８９０气相色谱仪,使用多孔层空心毛细管柱（ＰＬＯＴ）,选用ＨＰ－ＰＬＯＴ／Ｐｏｒａｐａｃｋ Ｑ色谱柱测定ＣＯ２;ＨＰ－ＰＬＯＴ ５Ａ分子筛柱测定Ｏ２,Ｎ２,ＣＨ４;ＨＰ－ＰＬＯＴ／Ａｌ２Ｏ３柱测定有机烃类。采用３阀４柱色谱运行系统,用ＦＩＤ及ＴＣＤ分别检测烃类及无机气体组分。用色谱工作站控制气动切换阀切换气样走向及两种检测器数据的转换校正和归一化定量计算,用已知物对照法定性,测定了炼厂气中     

A Gas Chromatographic Analysis of Light Hydrocarbons on a Column Packed with Modified Silica Gel

IntroductionAnalysis of light hydrocarbons achieved by gas-solid chromatography is important in petrochemical industry, environmental protection and some other areas. A variety of columns have been used, including conventional packed column1, Al2O3 and graphitized carbon black PLOT column2, 3 and silica gel SCOT column4. Al2O3 PLOT column is excellent for the analysis of light hydrocarbons. Conventional packed column also has its own advantages, such as easy column preparation, resistanc…     

Olefin/paraffin gas separations with 6FDA-based polyimide membranes

Pure gas permeation and sorption experiments were carried out for the gases ethylene, ethane, propylene and propane using polyimides based on 4,4′-(hexafluoroisopropylidene) diphthalic anhydride (6FDA). Composite membranes and free films were used. Experiments were performed at 308 K and feed pressures up to 17 atm for ethylene and ethane and 9 atm for propylene and propane. Mixed gas permeation experiments were carried out with 50 : 50 olefin/paraffin feed mixtures. For all investigated polyimides, the ideal ethylene/ethane separation factor ranged between 3.3 and 4.4 and the ideal propylene/propane separation factor ranged between 10 and 16 at a feed pressure of 3.8 atm and 308 K. In mixed gas permeation experiments, up to 20% lower selectivity was found for the ethylene/ethane separation and up to 50% reduced selectivity for the propylene/propane separation compared to the ideal selectivity. The influence of feed temperature on separation and permeation properties will be discussed based on pure gas permeability data at 298 and 308 K.     

金属有机骨架材料在轻烃分离中的应用

金属有机骨架材料(metal-organic frameworks,MOFs)是一种由金属离子或金属簇通过与有机配体自组装而形成的新型材料。近年来,金属有机骨架材料在轻烃(包括甲烷、乙炔、乙烯、乙烷、丙烯和丙烷)分离方面引起了广泛兴趣。本文简要地介绍了多种金属有机骨架材料分离不同轻烃气体的最新研究进展,并对影响分离效果的因素与研究前景进行了总结和展望。     

Highly selective sorption of small unsaturated hydrocarbons by nonporous flexible framework with silver ion

Ag2[Cr3O(OOCC2H5)6(H2O)3]2[alpha-SiW12O40] [1] is a nonporous flexible ionic crystal composed of 2D-layers of polyoxometalates ([alpha-SiW12O40](4-)) and macrocations ([Cr3O(OOCC2H5)6(H2O)3](+)) stacking along the b-axis. The silver ions are located in the vicinity of the oxygen atoms of the polyoxometalates. The sorption amounts of small unsaturated hydrocarbons such as ethylene, propylene, n-butene, acetylene, and methyl acetylene into 1 are comparable to or larger than 1.0 mol mol(-1) and large hystereses are observed, while those of paraffins and larger unsaturated hydrocarbons are smaller than the adsorption on the external surface (<0.2 mol mol(-1)). Fine crystals of 1 exhibit ethylene/ethane and propylene/propane sorption ratios over 100 at 298 K and 100 kPa, and the values are larger by 1 order of magnitude among those reported. The results of sorption kinetics, in situ IR spectroscopy, single crystal X-ray crystallography, and in situ powder XRD studies show that small unsaturated hydrocarbons penetrate into the solid bulk of 1 through the pi-complexation with Ag(+). The sorption property of 1 is successfully applied to the collection of ethylene from the gas mixture of ethane and ethylene.     

Vapor–liquid equilibrium of systems containing alcohols,water, carbon dioxide and hydrocarbons using SAFT

The statistical associating fluid theory (SAFT) equation of state is employed for the correlation and prediction of vapor–liquid equilibrium (VLE) of eighteen binary mixtures. These include water with methane, ethane, propane, butane, propylene, carbon dioxide, methanol, ethanol and ethylene glycol (EG), ethanol with ethane, propane, butane and propylene, methanol with methane, ethane and carbon dioxide and finally EG with methane and ethane. Moreover, vapor–liquid equilibrium for nine ternary systems was predicted. The systems are water/ethanol/alkane (ethane, propane, butane), water/ethanol/propylene, water/methanol/carbon dioxide, water/methanol/methane, water/methanol/ethane, water/EG/methane and water/EG/ethane. The results were found to be in satisfactory agreement with the experimental data except for the water/methanol/methane system for which the root mean square deviations for pressure were 60–68% when the methanol concentration in the liquid phase was 60 wt.%.     

Reactions of 12C+ with hydrocarbons at 296 K:carbon-carbon bond formation

Rate constants and product distributions have been determined for the ion-molecule reactions between ¹²C⁺ and methane, ethane, propane, ethylene, propylene, allene, acetylene, propyne and benzene. The measurements were carried out with the SIFT technique at a temperature of 296 ± 2K. The results provide insight into the build-up of carbon skeletons to form C⁺_n+1 ions and other competing modes of reaction at room temperature.     

C2 and C3 hydrocarbon separations in poly(1,5-naphthalene-2,2′-bis(3,4-phthalic) hexafluoropropane) diimide (6FDA-1,5-NDA) dense membranes

The transport of olefin and paraffin namely ethane, ethylene, propane and propylene in aromatic poly(1,5-naphthalene-2,2′-bis(3,4-phthalic) hexafluoropropane) diimide (6FDA-1,5-NDA) dense membranes was investigated. The gas permeability coefficients were measured at pressures from 2.5 to 16 atm for the C₂ hydrocarbon gases and pressures up to 8.4 atm for C₃ systems at 35 °C. This membrane exhibits permeabilities of 0.15, 0.87, 0.023 and 0.24 Barrer with respect to pure ethane, ethylene, propane and propylene, and shows an ideal selectivity of 5.8 for the separation of ethylene/ethane, 10 for propylene/propane, 7.6 for nitrogen/ethane and 50 for nitrogen/propane. The olefins showed a preferred permeability to paraffins and discussion were drawn to the permeability, diffusivity and solubility coefficients. The activation energies of permeation, diffusion and solution were also reported and the effect of temperature on the permeation properties was discussed for the pure gas permeability data obtained from 30 to 50 °C. The plasticisation effect was also found for propane and propylene, respectively, although it was neither detected in the saturated nor unsaturated C₂ hydrocarbons at pressures up to 16 atm.     

Adsorption of ethane, ethylene, propane, and propylene on a magnesium-based metal-organic framework

Separation of olefin/paraffin is an energy-intensive and difficult separation process in petrochemical industry. Energy-efficient adsorption process is considered as a promising alternative to the traditional cryogenic distillation for separating olefin/paraffin mixtures. In this work, we explored the feasibility of adsorptive separation of olefin/paraffin mixtures using a magnesium-based metal-organic framework, Mg-MOF-74. Adsorption equilibria and kinetics of ethane, ethylene, propane, and propylene on a Mg-MOF-74 adsorbent were determined at 278, 298, and 318 K and pressures up to 100 kPa. A dual-site Sips model was used to correlate the adsorption equilibrium data, and a micropore diffusion model was applied to extract the diffusivities from the adsorption kinetics data. A grand canonical Monte Carlo simulation was conducted to calculate the adsorption isotherms and to elucidate the adsorption mechanisms. The simulation results showed that all four adsorbate molecules are preferentially adsorbed on the open metal sites where each metal site binds one adsorbate molecule. Propylene and propane have a stronger affinity to the Mg-MOF-74 adsorbent than ethane and ethylene because of their significant dipole moments. Adsorption equilibrium selectivity, combined equilibrium and kinetic selectivity, and adsorbent selection parameter for pressure swing adsorption processes were estimated. The relatively high values of adsorption selectivity suggest that it is feasible to separate ethylene/ethane, propylene/propane, and propylene/ethylene pairs in a vacuum swing adsorption process using Mg-MOF-74 as an adsorbent.