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CN106590734A - Enrichment and separation method for basic nitrides in shale diesel oil - Google Patents

Enrichment and separation method for basic nitrides in shale diesel oil Download PDF

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CN106590734A
CN106590734A CN201611132250.6A CN201611132250A CN106590734A CN 106590734 A CN106590734 A CN 106590734A CN 201611132250 A CN201611132250 A CN 201611132250A CN 106590734 A CN106590734 A CN 106590734A
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diesel oil
shale
alkali
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CN106590734B (en
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韩冬云
金阳
曹祖宾
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Liaoning Xincheng Technology Co ltd
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Liaoning Shihua University
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G53/00Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more refining processes
    • C10G53/02Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more refining processes plural serial stages only
    • C10G53/04Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more refining processes plural serial stages only including at least one extraction step
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/20Characteristics of the feedstock or the products
    • C10G2300/201Impurities
    • C10G2300/202Heteroatoms content, i.e. S, N, O, P
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2400/00Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/04Diesel oil

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

本发明涉及一种富集分离页岩柴油中碱性氮化物的方法,该方法的核心是采用溶剂精制和柱色谱相结合的分离方法。将所用萃取剂与页岩油柴油馏分按比例混合进行溶剂精制,精制后得到初步富集碱性氮化物的抽出油;抽出油作为碱性氮化物深度富集的原料,再经柱色谱进一步浓缩分离、脱溶剂、真空干燥得到碱性氮化物。

The invention relates to a method for enriching and separating basic nitrogen compounds in shale diesel oil. The core of the method is a separation method combining solvent refining and column chromatography. Mix the used extractant with the shale oil diesel fraction in proportion for solvent refining, and obtain the extracted oil that is initially enriched in basic nitrogen compounds after refining; the extracted oil is used as the raw material for deep enrichment of basic nitrogen compounds, and then further concentrated by column chromatography Separation, solvent removal, and vacuum drying give basic nitrides.

Description

一种页岩柴油中碱性氮化物富集分离的方法A method for the enrichment and separation of basic nitrogen compounds in shale diesel oil

技术领域technical field

本申请属于页岩油加工技术领域,具体涉及一种页岩柴油中碱性氮化物富集分离的方法。The application belongs to the technical field of shale oil processing, and in particular relates to a method for enriching and separating basic nitrides in shale diesel oil.

背景技术Background technique

页岩油是世界上储存量十分丰富的潜在能源,它的总存储量远远超过石油。与天然石油相比,页岩油中含有大量的不饱和烃和N、S、O等非烃化合物。在我国,页岩油大部分作为燃料进行粗放式燃烧,在燃烧过程中产生大量的NOx和SO2,造成环境污染的同时能源利用价值低。油品中的含氮化物一般可分为碱性氮化物和非碱性氮化物。碱性氮化物的存在对页岩油的再加工和利用有着直接的影响,是要除去或转化的有毒物质,但其本身是非常宝贵的化工原料。碱性氮化物广泛应用于工业、医药、防腐剂、浮选剂、合成材料等领域。近几年来,从煤焦油、页岩油及石油产品中提取碱性氮化物的研究已引起国内外研究者的广泛关注。Shale oil is a potential energy source with abundant reserves in the world, and its total storage capacity far exceeds that of petroleum. Compared with natural petroleum, shale oil contains a large amount of unsaturated hydrocarbons and non-hydrocarbon compounds such as N, S, and O. In China, shale oil is mostly used as fuel for extensive combustion, which produces a large amount of NO x and SO 2 during the combustion process, causing environmental pollution and low energy utilization value. Nitrogen compounds in oil products can generally be divided into basic nitrogen compounds and non-basic nitrogen compounds. The existence of basic nitrides has a direct impact on the reprocessing and utilization of shale oil, and they are toxic substances to be removed or transformed, but they are very valuable chemical raw materials. Basic nitrides are widely used in industry, medicine, preservatives, flotation agents, synthetic materials and other fields. In recent years, the research on extracting basic nitrogen compounds from coal tar, shale oil and petroleum products has attracted extensive attention of researchers at home and abroad.

目前,页岩油中碱性氮化物的提取方法主要有溶剂精制、络合分离、酸碱洗脱、柱色谱、薄层色谱及上述方法的组合等。At present, the extraction methods of basic nitrogen compounds in shale oil mainly include solvent refining, complexation separation, acid-base elution, column chromatography, thin-layer chromatography, and combinations of the above methods.

溶剂精制是20世纪迅速发展起来的一种新的分离技术,即溶剂萃取,采用的方法为相似相溶原理,根据所要分离的碱性氮化物在油品中与采用的溶剂之间的溶解度的差异有选择性的将其分离,分离效果较好。Solvent refining is a new separation technology developed rapidly in the 20th century, that is, solvent extraction. The method adopted is based on the principle of similar miscibility. The difference is selectively separated, and the separation effect is better.

络合分离法应用的是Lewis酸碱理论,络合剂和碱性氮化物在Lewis酸与Lewis碱的络合作用力下,形成络合物与油相分层,从而将碱性氮化物从油品中分离。但直接用络合精制处理页岩油,则效果不佳。中国专利CN 103937522 A公开煤焦油中含氮化合物的分离方法,采用的络合分离剂含有金属氯化物、磷酸盐和卤代盐,其中金属氯化物与卤代盐质量比为0.05~0.2、磷酸盐和卤代盐的质量比为0.04~0.15,络合分离剂与煤焦油的质量比为0.05~0.7。该方法实现了煤焦油中含氮化合物选择性地快速分离,分离效果较好。但该方法所采用的络合分离剂成本较高,制备较复杂。The complexation separation method applies the Lewis acid-base theory, and the complexing agent and the basic nitrogen compound form a complex and layer the oil phase under the complexing force of the Lewis acid and the Lewis base, thereby separating the basic nitrogen compound from the Oil separation. However, the direct treatment of shale oil by complexation refining is ineffective. Chinese patent CN 103937522 A discloses a method for separating nitrogen-containing compounds in coal tar. The complexing separation agent used contains metal chlorides, phosphates and halogenated salts, wherein the mass ratio of metal chlorides to halogenated salts is 0.05-0.2, phosphoric acid The mass ratio of the salt to the halogenated salt is 0.04-0.15, and the mass ratio of the complexing separation agent to the coal tar is 0.05-0.7. The method realizes the selective and rapid separation of nitrogen-containing compounds in coal tar, and the separation effect is good. However, the cost of the complexing and separating agent used in this method is relatively high, and the preparation is relatively complicated.

酸碱洗脱是根据碱性氮化物具有碱性,利用酸碱中和的原理与强酸进行反应将碱性氮化物分离出来。美国专利US 52637是先加入一种相对页岩油具有较高挥发性的易混合的非极性稀释剂,或采用直接加热的方法,来降低页岩油的黏度,然后用一种由甲酸、乙酸、三氯乙酸中的一种或几种组成的选择性溶剂来萃取氮化物,用甲酸和乙酸分别可以脱除76.38%、87.62%的氮。此法选择性高,但需大量使用酸碱,对设备防腐要求高。Acid-base elution is based on the basic nitrides are basic, and the principle of acid-base neutralization is used to react with strong acids to separate the basic nitrides. U.S. Patent US 52637 is to add a kind of relatively shale oil has higher volatility easy-to-miscible non-polar diluent, or adopt the method of direct heating, to reduce the viscosity of shale oil, then use a kind of formic acid, Selective solvents composed of one or more of acetic acid and trichloroacetic acid are used to extract nitrogen compounds, and 76.38% and 87.62% of nitrogen can be removed with formic acid and acetic acid, respectively. This method has high selectivity, but it needs to use a large amount of acid and alkali, and has high requirements for equipment anticorrosion.

柱色谱属于液-固吸附色谱,它是基于吸附-溶解的原理的一种技术。利用两相之间范德华力和氢键等各种分子间力的作用,当混合物溶液加在固定相时,混合物中的各组分以不同的作用强度被吸附在固体表面。由于吸附剂对各物质的吸附能力不同,吸附强的组分在流动相中分配少,而吸附弱的组分在流动相中分配多,从而混合物中的各组分得到有效的分离。Column chromatography belongs to liquid-solid adsorption chromatography, which is a technique based on the principle of adsorption-dissolution. Using various intermolecular forces such as van der Waals force and hydrogen bonds between the two phases, when the mixture solution is added to the stationary phase, each component in the mixture is adsorbed on the solid surface with different strengths of action. Due to the different adsorption capacity of the adsorbent for each substance, the components with strong adsorption are less distributed in the mobile phase, while the components with weak adsorption are distributed more in the mobile phase, so that the components in the mixture are effectively separated.

薄层色谱属于固-液吸附色谱,是一种微量的分离分析方法,具有设备简单、速度快、分离效果好、灵敏度高等优点,但仅适用于小量样品的分离。Thin-layer chromatography belongs to solid-liquid adsorption chromatography. It is a trace separation and analysis method. It has the advantages of simple equipment, fast speed, good separation effect, and high sensitivity. However, it is only suitable for the separation of small amounts of samples.

发明内容Contents of the invention

本发明针对上述现有技术中存在的问题,提供了一种页岩柴油中碱性氮化物富集分离的方法。该方法采用溶剂精制和柱色谱相结合的分离方法,操作简便可行,能将碱性氮化物与烃类、非碱性氮化物、酚类化合物分开,使页岩油中的碱性氮化物得到有效的富集分离。The present invention aims at the problems existing in the above-mentioned prior art, and provides a method for enriching and separating basic nitrogen compounds in shale diesel oil. The method adopts a separation method combining solvent refining and column chromatography, which is simple and feasible to operate, and can separate basic nitrogen compounds from hydrocarbons, non-basic nitrogen compounds, and phenolic compounds, so that the basic nitrogen compounds in shale oil can be obtained Effective enrichment separation.

本发明的技术方案包括以下步骤:Technical scheme of the present invention comprises the following steps:

将萃取剂与页岩柴油按摩尔比0.3-2:1比例混合进行搅拌反应,静置沉降一段时间后油品分为两层,上层和下层的萃取剂可通过减压蒸馏回收,循环利用;下层脱萃取剂后得到初步富集碱性氮化物的抽出油;抽出油经柱色谱浓缩分离、酸抽提碱性化合物、碱中和酸、溶剂反抽提碱性氮化物、脱溶剂、真空干燥得碱性氮化物。The extractant and shale diesel are mixed in a molar ratio of 0.3-2:1 for stirring reaction. After standing for a period of time, the oil product is divided into two layers. The extractant in the upper layer and the lower layer can be recovered by vacuum distillation and recycled; After the lower layer removes the extractant, the extracted oil that is initially enriched in basic nitrogen compounds is obtained; the extracted oil is concentrated and separated by column chromatography, acid extracts basic compounds, alkali neutralizes acid, solvent back extracts basic nitrogen compounds, solvent removal, vacuum Dry to obtain basic nitrides.

所述的萃取剂为N,N-二甲基甲酰胺、糠醛、二甲基亚砜、N-甲基吡咯烷酮的一种或几种。The extractant is one or more of N,N-dimethylformamide, furfural, dimethylsulfoxide and N-methylpyrrolidone.

所述的搅拌反应温度为50-80℃。The stirring reaction temperature is 50-80°C.

所述的沉降时间为10-50min。The settling time is 10-50min.

所述的柱色谱固体吸附剂为硅胶。The column chromatography solid adsorbent is silica gel.

所述的柱色谱流动相为石油醚、苯/甲醇混合溶液。The mobile phase of the column chromatography is a mixed solution of petroleum ether and benzene/methanol.

所述的柱色谱流动相中苯/甲醇混合溶液的体积比为1-2:1。The volume ratio of the benzene/methanol mixed solution in the column chromatography mobile phase is 1-2:1.

所述的酸为盐酸,浓度为3mol/L。Described acid is hydrochloric acid, and concentration is 3mol/L.

所述的碱为氢氧化钠或氢氧化钾。Described alkali is sodium hydroxide or potassium hydroxide.

所述的溶剂为正己烷。Described solvent is n-hexane.

本发明的优点效果如下:The advantages and effects of the present invention are as follows:

本发明采用溶剂精制和柱色谱相结合的分离方法,操作简便可行,能将碱性氮化物与烃类、非碱性氮化物、酚类化合物分开,有利于碱性氮化物的富集分离。同时,既避免了大量酸、碱水溶液的使用,萃取剂可回收利用,大大降低了生产成本,又使页岩油中的碱性氮化物得到有效的富集分离,提高页岩油的综合利用价值,同时有利于页岩油的加工、精制。The invention adopts a separation method combining solvent refining and column chromatography, which is simple and feasible to operate, can separate basic nitrogen compounds from hydrocarbons, non-basic nitrogen compounds and phenolic compounds, and is beneficial to the enrichment and separation of basic nitrogen compounds. At the same time, the use of a large amount of acid and alkali aqueous solutions is avoided, and the extraction agent can be recycled, which greatly reduces the production cost, and effectively enriches and separates the basic nitrogen compounds in shale oil, improving the comprehensive utilization of shale oil At the same time, it is beneficial to the processing and refining of shale oil.

附图说明Description of drawings

图1为最终产物的色谱图。Figure 1 is the chromatogram of the final product.

具体实施方式detailed description

实施例1Example 1

取90ml N,N-二甲基甲酰胺与300ml页岩柴油混合(摩尔比为0.3:1),水浴加热搅拌,设定加热温度为50℃,搅拌结束后,倒入分液漏斗中待试样分层,静置10min后,将下层的油品进行蒸馏,得到抽出油和N,N-二甲基甲酰胺,N,N-二甲基甲酰胺循环利用。将抽出油进行柱色谱分离,称取硅胶50g,依次用80mL石油醚、80mL苯/甲醇混合溶液(体积比为1:1)对色谱柱进行层析洗脱。得到的苯/甲醇冲出液经水抽提3次后分离出苯层溶液,再用3mol/L的HCl抽提苯层溶液得到无机层,用6mol/L的NaOH溶液对无机层进行中和至PH=11,之后加入正己烷抽提3次,将碱性氮化物从水相中提取出来,蒸出溶剂,得到碱性氮化物。Mix 90ml of N,N-dimethylformamide with 300ml of shale diesel (the molar ratio is 0.3:1), heat and stir in a water bath, set the heating temperature to 50°C, and pour it into a separatory funnel after stirring The sample was separated into layers, and after standing for 10 minutes, the oil product in the lower layer was distilled to obtain extracted oil and N,N-dimethylformamide, and N,N-dimethylformamide was recycled. The extracted oil was separated by column chromatography, 50g of silica gel was weighed, and chromatographically eluted with 80mL of petroleum ether and 80mL of benzene/methanol mixed solution (1:1 by volume) in sequence. The obtained benzene/methanol eluate was extracted 3 times with water to separate the benzene layer solution, then extracted the benzene layer solution with 3mol/L HCl to obtain the inorganic layer, and neutralized the inorganic layer with 6mol/L NaOH solution to PH = 11, then adding n-hexane for extraction three times, extracting the basic nitrogen compound from the water phase, and distilling off the solvent to obtain the basic nitrogen compound.

实施例2Example 2

将萃取剂二甲基亚砜与页岩柴油按摩尔比0.5:1比例混合进行搅拌反应,搅拌反应温度为50℃,静置沉降20min后油品分为两层,上层和下层的萃取剂可通过减压蒸馏回收,循环利用;下层脱萃取剂后得到初步富集碱性氮化物的抽出油;抽出油经柱色谱浓缩分离、酸抽提碱性化合物、碱中和酸、溶剂反抽提碱性氮化物、脱溶剂、真空干燥得碱性氮化物。所述的柱色谱固体吸附剂为硅胶;所述的柱色谱流动相为石油醚、苯/甲醇混合溶液;苯/甲醇混合溶液的体积比为1:1;其它步骤同实施例1。Mix the extractant dimethyl sulfoxide and shale diesel at a molar ratio of 0.5:1 for a stirring reaction. The stirring reaction temperature is 50°C. After standing and settling for 20 minutes, the oil product is divided into two layers. Recover by vacuum distillation and recycle; the lower layer removes the extractant to obtain the extracted oil that is initially enriched with basic nitrogen compounds; the extracted oil is concentrated and separated by column chromatography, acid extraction of basic compounds, alkali neutralization of acid, and solvent back extraction Basic nitrides, solvent removal, and vacuum drying to obtain basic nitrides. The column chromatography solid adsorbent is silica gel; the column chromatography mobile phase is petroleum ether, benzene/methanol mixed solution; the volume ratio of benzene/methanol mixed solution is 1:1; other steps are the same as in Example 1.

实施例3Example 3

将萃取剂N-甲基吡咯烷酮与页岩柴油按摩尔比1:1比例混合进行搅拌反应,搅拌反应温度为70℃,静置沉降50min后油品分为两层,上层和下层的萃取剂可通过减压蒸馏回收,循环利用;下层脱萃取剂后得到初步富集碱性氮化物的抽出油;抽出油经柱色谱浓缩分离、酸抽提碱性化合物、碱中和酸、溶剂反抽提碱性氮化物、脱溶剂、真空干燥得碱性氮化物。所述的柱色谱固体吸附剂为硅胶;所述的柱色谱流动相为石油醚、苯/甲醇混合溶液;苯/甲醇混合溶液的体积比为1.2:1;其它步骤同实施例1。The extraction agent N-methylpyrrolidone and shale diesel are mixed in a molar ratio of 1:1 for stirring reaction. The stirring reaction temperature is 70°C. After standing for 50 minutes, the oil product is divided into two layers. Recover by vacuum distillation and recycle; the lower layer removes the extractant to obtain the extracted oil that is initially enriched with basic nitrogen compounds; the extracted oil is concentrated and separated by column chromatography, acid extraction of basic compounds, alkali neutralization of acid, and solvent back extraction Basic nitrides, solvent removal, and vacuum drying to obtain basic nitrides. The column chromatography solid adsorbent is silica gel; the column chromatography mobile phase is petroleum ether, benzene/methanol mixed solution; the volume ratio of benzene/methanol mixed solution is 1.2:1; other steps are the same as in Example 1.

实施例4Example 4

将萃取剂糠醛与页岩柴油按摩尔比1:1比例混合进行搅拌反应,搅拌反应温度为60℃,静置沉降30min后油品分为两层,上层和下层的萃取剂可通过减压蒸馏回收,循环利用;下层脱萃取剂后得到初步富集碱性氮化物的抽出油;抽出油经柱色谱浓缩分离、酸抽提碱性化合物、碱中和酸、溶剂反抽提碱性氮化物、脱溶剂、真空干燥得碱性氮化物。所述的柱色谱固体吸附剂为硅胶;所述的柱色谱流动相为石油醚、苯/甲醇混合溶液;苯/甲醇混合溶液的体积比为1:1;其它步骤同实施例1。Mix the extractant furfural and shale diesel at a molar ratio of 1:1 for stirring reaction. The stirring reaction temperature is 60°C. After standing for 30 minutes, the oil product is divided into two layers. The extractant in the upper layer and the lower layer can be distilled under reduced pressure. Recovery and recycling; after the lower layer removes the extractant, the extracted oil that is initially enriched with basic nitrogen compounds is obtained; the extracted oil is concentrated and separated by column chromatography, acid extraction of basic compounds, alkali neutralization of acid, and solvent back extraction of basic nitrogen compounds , solvent removal, and vacuum drying to obtain basic nitrides. The column chromatography solid adsorbent is silica gel; the column chromatography mobile phase is petroleum ether, benzene/methanol mixed solution; the volume ratio of benzene/methanol mixed solution is 1:1; other steps are the same as in Example 1.

实施例5Example 5

将萃取剂N,N-二甲基甲酰胺与页岩柴油按摩尔比2:1比例混合进行搅拌反应,搅拌反应温度为80℃,静置沉降50min后油品分为两层,上层和下层的萃取剂可通过减压蒸馏回收,循环利用;下层脱萃取剂后得到初步富集碱性氮化物的抽出油;抽出油经柱色谱浓缩分离、酸抽提碱性化合物、碱中和酸、溶剂反抽提碱性氮化物、脱溶剂、真空干燥得碱性氮化物。所述的柱色谱固体吸附剂为硅胶;所述的柱色谱流动相为石油醚、苯/甲醇混合溶液;苯/甲醇混合溶液的体积比为2:1;其它步骤同实施例1。Mix the extractant N, N-dimethylformamide and shale diesel oil in a molar ratio of 2:1 for stirring reaction. The stirring reaction temperature is 80°C. After standing for 50 minutes, the oil product is divided into two layers, the upper layer and the lower layer. The extractant can be recovered by vacuum distillation and recycled; after the lower layer removes the extractant, the extracted oil that is initially enriched with basic nitrogen compounds is obtained; the extracted oil is concentrated and separated by column chromatography, acid extracts basic compounds, alkali neutralizes acid, Solvent back extraction of basic nitrides, solvent removal, and vacuum drying to obtain basic nitrides. The column chromatography solid adsorbent is silica gel; the column chromatography mobile phase is petroleum ether, benzene/methanol mixed solution; the volume ratio of benzene/methanol mixed solution is 2:1; other steps are the same as in Example 1.

实施结果Implementation results

通过气相色谱-质谱联用仪(GC-MS)对实施例4富集的最终产物进行表征,结果见图1和表1。实施例4中碱性氮化物的梯度富集结果见表2。The final product enriched in Example 4 was characterized by gas chromatography-mass spectrometry (GC-MS), and the results are shown in FIG. 1 and Table 1. Table 2 shows the gradient enrichment results of basic nitrides in Example 4.

页岩油中的碱性氮化物可通过溶剂精制和柱色谱相结合的方法得到有效的富集与分离,碱性氮化物的相对质量分数由抽出油的12.08%梯度浓缩至最终富集产物的69.48%。在富集分离的最终产物中鉴定出了60种碱性氮化物,其中主要为苯胺、吡啶、喹啉、异喹啉等烷基取代化合物。The basic nitrogen compounds in shale oil can be effectively enriched and separated by combining solvent refining and column chromatography. The relative mass fraction of basic nitrogen compounds is gradually concentrated from 12.08% of the extracted oil to that of the final enriched product. 69.48%. In the final product of enrichment and separation, 60 kinds of basic nitrogen compounds were identified, mainly alkyl-substituted compounds such as aniline, pyridine, quinoline, and isoquinoline.

表1最终产物的GC-MS结果The GC-MS result of table 1 final product

表2页岩柴油中碱性氮化物的梯度富集结果Table 2 Gradient enrichment results of basic nitrogen compounds in shale diesel

Claims (10)

1. a kind of method of shale diesel oil neutral and alkali nitride concentration and separation, its feature:The method is comprised the following steps:Will extraction Agent is mixed by a certain percentage with shale oil diesel oil distillate, is stirred reaction at a certain temperature, standing sedimentation for a period of time after Oil product is divided into two-layer, and the extractant of the upper and lower can be reclaimed by vacuum distillation, be recycled.Obtain after the de- extractant of lower floor The tapped oil of preliminary concentration basic nitrogen compound.Tapped oil Jing column chromatography concentrating and separating, acid extracting alkali compoundss, in alkali and acid, Solvent back suction carries basic nitrogen compound, desolventizing, is vacuum dried to obtain basic nitrogen compound.
2. the method for a kind of shale diesel oil neutral and alkali nitride concentration and separation according to claim 1, it is characterised in that:Extraction The mass ratio that agent is taken with shale diesel oil is 0.3-2:1.
3. the method for a kind of shale diesel oil neutral and alkali nitride concentration and separation according to claim 1 and 2, its feature exist In:Described extractant is one or more of DMF, furfural, dimethyl sulfoxide, N-Methyl pyrrolidone.
4. the method for a kind of shale diesel oil neutral and alkali nitride concentration and separation according to claim 1, it is characterised in that:Institute The stirring reaction temperature stated is 50-80 DEG C.
5. the method for a kind of shale diesel oil neutral and alkali nitride concentration and separation according to claim 1, it is characterised in that:It is heavy The drop time is 10-50min.
6. the method for a kind of shale diesel oil neutral and alkali nitride concentration and separation according to claim 1, it is characterised in that:Post Chromatography solid adsorbent is silica gel, and mobile phase is petroleum ether, benzene/methanol mixed solution.
7. the method for a kind of shale diesel oil neutral and alkali nitride concentration and separation according to claim 6, it is characterised in that:Post In chromatogram flow phase, the volume ratio of benzene/methanol mixed solution is 1-2:1.
8. the method for a kind of shale diesel oil neutral and alkali nitride concentration and separation according to claim 1, it is characterised in that:Institute The acid stated is hydrochloric acid, and concentration is 3mol/L.
9. the method for a kind of shale diesel oil neutral and alkali nitride concentration and separation according to claim 1, it is characterised in that:Institute The alkali stated can use sodium hydroxide or potassium hydroxide.
10. the method for a kind of shale diesel oil neutral and alkali nitride concentration and separation according to claim 1, it is characterised in that: Described solvent is normal hexane.
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