毛细管气相色谱/傅立叶变换红外光谱分析高温煤焦油中的重油馏分

在原有工作基础上 ,采用毛细管气相色谱 /傅立叶变换红外光谱 -色谱保留指数 ( GC/ FTIR- RI)联合解析技术 ,研究了高温煤焦油重油馏分的化学组成。分别从重油馏分 F7( 30 0～ 330℃ )和 F8( 330～ 360℃ )中分离并鉴定出 70和 61种化合物 ,了解到不同配煤工艺对煤焦油组成与性能的影响 ,从而获得了一些有意义的结果 ,为煤焦油的集中加工和新产品开发提供了重要依据     

NiMo/Al_2O_3-USY催化剂上中低温煤焦油加氢裂化性能研究

采用等体积浸渍法制得一系列NiMo/Al_2O_3-USY催化剂,在200 mL固定床上考察了不同金属负载量对其中低煤焦油加氢裂化催化性能的影响,进一步用NH_4F溶液改性USY以提高催化剂的脱硫性能,并结合XRD、氮气吸附-脱附、XPS、HR-TEM、H_2-TPR和NH_3-TPD等手段对催化剂进行了表征分析。结果表明,NiM o/Al_2O_3-USY催化剂适宜的M oO_3负载量为15%(质量分数);当MoO_3含量超过15%后,MoS_2活性相在载体上团聚,硫化程度趋于稳定,强酸酸量和孔径减少,增加金属负载量对煤焦油加氢裂化转化率影响较小。NH_4F改性USY可增大NiM o/Al_2O_3-USY催化剂的孔径,有利于提高煤焦油加氢裂化转化率。表面强酸酸量减少后,产品中的硫含量明显增加,说明强酸酸量是影响产物硫含量的关键因素。当NH_4F浓度为0.6 mol/L时,NH_4F改性USY制得的NM 0.6催化剂上煤焦油加氢裂化的转化率为87.65%,产品汽油馏分(≤180℃)硫含量为5.96 mg/kg,柴油馏分(180-320℃)硫含量为34.98 mg/kg。     

原料组成对针状焦结构的影响

在330–390℃、8 MPa、加氢时间为1.5 h和剂油比为1:40的条件下对中低温煤焦油原料进行加氢处理,得到精制原料后再通过热聚合煅烧等过程制得针状焦.通过元素分析、红外光谱(FT-IR)、气相色谱-质谱联用仪(GC-MS)等检测方法分析了精制原料组成,并采用扫描电子显微镜(SEM)、X射线衍射仪(XRD)和偏光...     

NiW/γ-Al2O3催化剂的低温煤焦油加氢性能研究

以γ-Al₂O₃为载体,采用等体积浸渍法制备了不同Ni/W原子比的低温煤焦油加氢处理催化剂,并以BET、XRD、H₂-TPR和TG对催化剂进行表征。在固定床反应器中,以低温煤焦油小于350 ℃馏分作为原料对催化剂进行了加氢性能的评价,并采用蒸馏、GC/MS、荧光指示剂吸附及元素分析对原料及产物的馏分分布及组成进行了分析。结果表明,NiO和WO₃在载体上形成了均匀分散,NiO含量较低时与γ-Al₂O₃有较强的作用力而难以还原。当Ni/W原子比为0.38时,酚类化合物的转化率、航煤馏分选择性以及产物中环烷烃和氢化芳烃的含量均最高,加氢脱硫(HDS)活性、加氢脱氮(HDN)活性及产物的H/C原子比也最高,说明Ni/W原子比为0.38时,NiW/γ-Al₂O₃催化剂对煤焦油加氢处理具有较好的效果。     

填充毛细管液相色谱-高温毛细管气相色谱在线联用分析重油

重油的组成分析一直是个难题,它的沸点高,族组分种类多,各族内组分的异构体又极为繁多.最好的分析方法是用高效液相色谱(HPLC)做族分离,馏分收集后再用CGC分析.但HPLC的族馏分体积比CGC进样量大100倍.本文采用填充毛细管液相色谱(μHPLC)与高温毛细管气相色谱(HTGC)在线联用技术[1]分析重油.正相μHPLC将样品按族分离,μHPLC的柱效高,族分离能力强,而小的馏分体积(<100μL)可避免GC分流进样.在一次LC进样后,多位储存型联用接口将分离后的各族组分切割、存储并分别无损失转入HTGC分析,利用FID对高于C10的有机物的响应值相…     

采用模拟蒸馏对原油馏分分布的色谱法测定

提出了色谱模拟蒸馏测定原油馏分分布的方法,采用高温模拟蒸馏分析原油中重组分,用详细烃组成技术(DHA方法)分析原油中轻组分,通过组分整合得到原油馏分分布。试验表明:采用nC5～nC120的正构烷烃混合物作为模拟蒸馏的沸点校正样,分析的馏程范围为初馏点至750℃。该方法重复性好,初馏点和终馏点的标准偏差小于1℃,各馏分收率的标准偏差小于0.35%。此法与实沸点蒸馏方法结果基本一致,小于500℃各馏分的收率差值小于2.5%,可明显看出在500～750℃范围的馏分分布,有利于重质馏分的进一步加工利用。     

平朔气煤DF_5的组成特性及煤液体统计平均结构参数的相似性

烟煤煤焦油、沥青和煤萃取物的表观特性的相似性已受到人们广泛关注[1]。早在1956年Ｏｒｉｎｇ等人[2]已用红外光谱研究了高真空短途径热解煤焦油和原煤的组成。研究表明,煤焦油中存在和原煤相同或相似的物质。80年代Ｌａｄｎｅｒ[3]指出,煤的萃取物结构特征反映了煤中的部分原始结构单元,所以根据萃取物的结构特征去推测煤的结构是合理的。研究也指出[1],煤萃取馏分的平均分子量和部分沥青馏分的平均分子量非常相近。因此煤中在强溶剂中能溶解的部分(萃取馏分)和煤焦油、沥青之间的相似性已被作为一个煤焦油中的部分高分子化合物代表煤中部…     

中温热解焦油重馏分悬浮床加氢裂化的研究

以中温热解煤焦油为原料,对其性质进行了分析,其中,350℃重质馏分中胶质含量30.88%,沥青质含量37.27%,四氢呋喃不溶物3.36%,属于常规固定床加氢裂化难以直接处理的馏分。合成了一种Mo系超分散催化剂,采用FT-IR、XPS、XRD、SEM和TEM等对催化剂进行了表征,催化剂中含有Mo=O和Mo-S特征结构,活性金属的硫化率为84.34%,在体系中具有优良的分散性,在反应体系内原位分解为超分散MoS_2颗粒;在0.25 t/d连续装置上进行了热解重油悬浮床加氢裂化实验研究,考察了反应条件对产物分布情况和结焦率的影响,得出适宜的反应条件为19 MPa,440℃,催化剂的添加量为300 mg/kg;此条件下石脑油收率24.47%,柴油馏分收率49.71%,结焦率1.32%。     

煤焦油为原料的有机合成工业

一、煤炭焦化时大体上得到三大主要产品,即焦炉气、煤焦油和焦炭煤焦油的产量与煤的化学年代,焦化温度,焦炉结构等有关。例如,煤焦油量与煤中挥发物量间之关系:挥发物量% 15.0 20.0 22.5 25.0 30.0 32.0焦油量% 1.25 1.84 2.83 3.64 4.12 4.31通常规划焦油量时可取为干煤的2.5%。煤焦油分馏时可得到轻油、中油、重油、蒽油及沥青五个馏分(实际的分法,略有不同),其成分亦有较大     

色谱与色谱/质谱法相结合分析热裂解汽油C9馏分

采用毛细管气相色谱-氢火焰离子化检测器（CGC-FID）和气相色谱-质谱法(GC/MS)分析了热裂解汽油C9 馏分的组成。实验使用PONA毛细管气相色谱柱(100 m×0.25 mm i.d.×0.5 μm),根据烃类化合物在PONA柱上的保留规律,以正构烷烃标样保留值作为碳数分布依据,定量分析了裂解汽油C9 馏分中烃类化合物的碳数分布和单体烃含量;用GC/MS联用技术和CGC保留值定性法相结合对裂解汽油C9 馏分中相对含量大于0.2%的39种化合物进行了定性。     

A multi-dimensional high performance liquid chromatographic method for fingerprinting polycyclic aromatic hydrocarbons and their alkyl-homologs in the heavy gas oil fraction of Alaskan North Slope crude

We report an offline multi-dimensional high performance liquid chromatography (HPLC) technique for the group separation and analysis of PAHs in a heavy gas oil fraction (boiling range 287-481 degrees C). Waxes present in the heavy gas oil fraction were precipitated using cold acetone at -20 degrees C. Recovery studies showed that the extract contained 93% (+/-1%; n=3) of the PAHs that were originally present while the wax residue contained only 6% (+/-0.5%; n=3). PAHs present in the extract were fractionated, based on number of rings, into five fractions using a semi-preparative silica column (normal-phase HPLC). These fractions were analyzed using reverse-phase HPLC (RP-HPLC) coupled to a diode array detector (DAD). The method separated alkyl and un-substituted PAHs on two reverse-phase columns in series using an acetonitrile/water mobile phase. UV spectra of the chromatographic peaks were used to differentiate among PAH groups. Further characterization of PAHs within a given group to determine the substituent alkyl carbon number used retention time matching with a suite of alkyl-PAH standards. Naphthalene, dibenzothiophene, phenanthrene and fluorene and their C1-C4 alkyl isomers were quantified. The concentrations of these compounds obtained using the current method were compared with that of a GC-MS analysis obtained from an independent oil chemistry laboratory.     

Compositional studies of high-temperature coal tar by GC/FTIR analysis of light oil fractions

Summary A method for determination of the composition of the light oil fractions in high-temperature coal tar by means of distillation, followed by gas chromatography on a crosslinked fused-silica, capillary column coated with optimum amount of stationary phase and identification by capillary gas chromatography/Fourier transform infrared spectrometry combined with GC retention indices (GC/FTIR-RI) is described. This method was effectively used to identify complex mixture such as coal tar without any standard samples, especially, adapted for isomeric compounds. More than 60 and 50 compounds were also separated and identified respectively in light oil fractions. This shows the capability of the capillary GC/FTIR combined with GC retention indices to identify isomers not accomplished by GC/MS.     

Application of high-temperature simulated distillation to the residuum oil supercritical extraction process in petroleum refining

The gas chromatographic method of high-temperature simulated distillation (HTSD) is described, and the results are presented for the application of HTSD to the characterization of petroleum refinery feed and products from solvent deasphalting operations. Results are presented for refinery residual feed, deasphalted oil, and asphaltene fractions from the residual oil supercritical extraction process. Asphaltene removal from petroleum residuum using solvent deasphalting results in the improved quality and high recovery of deasphalted oil product for use as lube oil, fluid catalytic cracking, or hydrocracker feedstocks. The HTSD procedure presented here proves valuable for characterizing the fractions from the deasphalting process to obtain the percentage yield with boiling point data over the range from approximately 36 degrees C (97 degrees F) to 733 degrees C (1352 degrees F), which covers the boiling range of n-paraffins of carbon number C5 to C108.     

Determination of the boiling-point distribution by simulated distillation from n-pentane through n-tetratetracontane in 70 to 80 seconds

This work presents the carrying out of boiling-point distributions by simulated distillation with direct-column heating rather than oven-column heating. Column-heating rates of 300 degrees C/min are obtained yielding retention times of 73 s for n-tetratetracontane. The calibration curves of the retention time versus the boiling point, in the range of n-pentane to n-tetratetracontane, are identical to those obtained by slower oven-heating rates. The boiling-point distribution of the reference gas oil is compared with that obtained with column oven heating at rates of 15 to 40 degrees C/min. The results show boiling-point distribution values nearly the same (1-2 degrees F) as those obtained with oven column heating from the initial boiling point to 80% distilled off. Slightly higher differences are obtained (3-4 degrees F) for the 80% distillation to final boiling-point interval. Nonetheless, allowed consensus differences are never exceeded. Precision of the boiling-point distributions (expressed as standard deviations) are 0.1-0.3% for the data obtained in the direct column-heating mode.     

Selectivity of stationary phases in reversed-phase liquid chromatography based on the dispersion interactions

Selectivity of 15 stationary phases was examined, either commercially available or synthesized in-house. The highest selectivity factors were observed for solute molecules having different polarizability on the 3-(pentabromobenzyloxy)propyl phase (PBB), followed by the 2-(1-pyrenyl)ethyl phase (PYE). Selectivity of fluoroalkane 4,4-di(trifluoromethyl)-5,5,6,6,7,7,7-heptafluoroheptyl (F13C9) phase is lowest among all phases for all compounds except for fluorinated ones. Aliphatic octyl (C8) and octadecyl (C18) phases demonstrated considerable selectivity, especially for alkyl compounds. While PBB showed much greater preference for compounds with high polarizability containing heavy atoms than C18 phase, F13C9 phase showed the exactly opposite tendency. These three stationary phases can offer widely different selectivity that can be utilized when one stationary phase fails to provide separation for certain mixtures. The retention and selectivity of solutes in reversed-phase liquid chromatography is related to the mobile phase and the stationary phase effects. The mobile phase effect, related to the hydrophobic cavity formation around non-polar solutes, is assumed to have a dominant effect on retention upon aliphatic stationary phases such as C8, C18. In a common mobile phase significant stationary phase effect can be attributed to dispersion interaction. Highly dispersive stationary phases such as PBB and PYE retain solutes to a significant extent by (attractive) dispersion interaction with the stationary phase ligands, especially for highly dispersive solutes containing aromatic functionality and/or heavy atoms. The contribution of dispersion interaction is shown to be much less on C18 or C8 phases and was even disadvantageous on F13C9 phase. Structural properties of stationary phases are analyzed and confirmed by means of quantitative structure-chromatographic retention (QSRR) study.     

Temperature requirements for thermal modulation in comprehensive two-dimensional gas chromatography

Temperature requirements for trapping and release of compounds in a cryogenic gas loop-type GC x GC modulator were determined. Maximum trapping temperatures on the uncoated, deactivated modulator capillary were determined for compounds from C4 (bp -0.5 degrees C) to C40 (bp 522 degrees C). The liquid-nitrogen cooled gas flow rate was reduced from a high of 15.5 to 1.5 SLPM over the range to achieve the required trapping temperature. Excessive cold jet flow rates caused irreversible trapping and peak tailing for semi-volatile compounds above C26. Alternate cold jet coolants were investigated. An ice water-cooled jet was able to trap compounds with boiling points from C18 (bp 316 degrees C) to C40 and a room temperature air-cooled jet was able to trap compounds from C20 (bp 344 degrees C) to C40. The hot jet produced launch temperatures approximately 40 degrees C hotter than the elution temperature with heating time constants of 8 to 27 ms. Modulated compound peaks were symmetrical with half-height peak widths of 43 to 56 ms for compounds with little second column retention, and 70 to 75 ms for compounds with more second column retention. The liquid nitrogen-cooled loop modulator with gas flow programming was used to produce a GC x GC chromatogram for a crude oil that contained compounds from C7 to C47.     

Analysis of sulfur-containing compounds in crude oils by comprehensive two-dimensional gas chromatography with sulfur chemiluminescence detection

This paper reports an analytical method for separating, identifying, and quantifying sulfur-containing compounds in crude oil fraction (IBP-360 degrees C) samples based on comprehensive two-dimensional gas chromatography coupled with a sulfur chemiluminescence detector. Various sulfur-containing compounds and their groups were analyzed with one direct injection. 3620 peaks were detected including 1722 thiols/thioethers/ disulfides/1-ring thiophenes, 953 benzothiophenes, 704 dibenzothiophenes, and 241 benzonaphthothiophenes. The target sulfur compounds and their groups were identified based on the group separation feature and structured retention of comprehensive two-dimensional gas chromatography as well as standard substances. The quantitative analysis of major sulfur-containing compounds and total sulfur was based on the linear response of the sulfur chemiluminescence detector using the internal standard method. The sulfur contents of target sulfur compounds and their groups in 4 crude oil fractions were also determined. The recoveries for standard sulfur-containing compounds were in the range of 90-102%. The quantitative result of total sulfur in the Oman crude oil fraction sample was compared with those from ASTM D 4294 standard method (total S by X-ray fluorescence spectrometry), the relative deviation (RD%) was 4.2% and the precision of the method satisfactory.     

松油醇的分析及其生产工艺改进的研究

 应用气相 红外光谱(GC FTIR)和气相 质谱(GC MS)对合成松油醇及其杂质成分、原料松节油、合成过程中间体粗油(红油和黄油)和天然松油醇进行了分析研究,为判断松油醇产品中杂质产生的原因及改进生产工艺提供了依据。研究结果表明,松油醇中的杂质主要为长叶烯和石竹烯,是由原料松节油带入的。天然松油醇粗油中主要成分是1,8 桉叶素、反式 4 艹守醇、p 异丙烯基甲苯、顺式 4 艹守醇、芳樟醇、樟脑、龙脑、4 松油醇、α 松油醇和黄樟素。天然松油醇中β 松油醇和γ 松油醇含量不如合成松油醇中的含量高,以此可判断松油醇是天然的还是合成的。     

烷烃同系物气相色谱保留指数的分子拓扑研究

定义了分子中原子的平衡电负性,并用原子的平衡电负性对分子图进行着色,在距离矩阵的基础上结合分子中各原子的支化度构建了一种新的拓扑指数N1,N2和N3。该拓扑指数对分子结构实现惟一性表征,具有优良的结构选择性。将拓扑指数N1,N2和N3与烷烃在固定相角鲨烷(柱温50　℃)及SE-30(柱温80　℃)上的气相色谱保留指数进行多元线性回归,结果表明烷烃的气相色谱保留指数可分别定量描述为I(Squalane)=23.97842N1-3.86562N2+0.787379N3+42.33061,I(SE-30)=23.83937N1-3.5687N2+0.939876N3+22.11952。用上述回归方程对烷烃的气相色谱保留指数进行预测,结果表明预测值与实验值的平均相对误差均为1.31%,预测结果误差在实验误差范围内。     

橄榄石基固体热载体影响褐煤热解产物分布的分析

为了提高固体热载体煤热解工艺中焦油的品质,降低焦油中沸点大于360 ℃的重质组分含量,本实验采用固定床反应器,在450~600 ℃下进行褐煤固体热载体快速热解反应.分析对比了橄榄石基和石英砂固体热载体对褐煤热解产物收率、焦油馏分、气体组成的影响.结果发现,Co能改变煤内部挥发分氢元素的分布,橄榄石负载Co热载体能将焦油中重质组分转化为轻质焦油和热解气.热解温度为550 ℃时,与橄榄石相比,负载Co的橄榄石固体热载体使焦油收率提高了19.2%.与石英砂相比,负载Co的橄榄石固体热载体使焦油中重质组分含量降低了17.0%,轻质组分收率达5.1%,其中,轻油、酚油和萘油分别提高了19.6%、17%和15.2%,气体产物中H₂、CH₄含量下降.