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CN114496106A - Construction method of diesel oil steam cracking reaction network - Google Patents

Construction method of diesel oil steam cracking reaction network Download PDF

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CN114496106A
CN114496106A CN202210097198.4A CN202210097198A CN114496106A CN 114496106 A CN114496106 A CN 114496106A CN 202210097198 A CN202210097198 A CN 202210097198A CN 114496106 A CN114496106 A CN 114496106A
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杨遥
任玉
廖祖维
王靖岱
阳永荣
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ZJU Hangzhou Global Scientific and Technological Innovation Center
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Abstract

本发明公开了一种柴油蒸汽裂解反应网络的构建方法,包括:对柴油进行成分分析,筛选具有代表性的碳氢化合物分子作为柴油的烃类组成,具有代表性的含硫化合物分子和含氮化合物分子作为柴油的杂原子组成;采用反应网络生成工具Reaction Mechanism Generator对烃类组成和杂原子组成中的每一种分子进行单分子的反应网络自动生成;将生成的所有烃类组成分子和杂原子组成分子的反应网络进行合并,构建柴油蒸汽裂解的总反应网络。本发明可以低成本、短时间内获取柴油蒸汽裂解自由基机理水平的反应网络,所需时间仅为RMG程序运行时长,无需额外的人工梳理工作。

Figure 202210097198

The invention discloses a method for constructing a diesel steam cracking reaction network. The compound molecule is used as the heteroatom composition of diesel; the reaction network generation tool Reaction Mechanism Generator is used to automatically generate a single-molecule reaction network for each molecule in the hydrocarbon composition and heteroatom composition; all the generated hydrocarbon composition molecules and heteroatoms are generated. The reaction networks of atoms that make up the molecules are merged to construct the overall reaction network of diesel steam cracking. The invention can obtain the reaction network at the level of the diesel steam cracking radical mechanism at low cost and in a short time, and the required time is only the running time of the RMG program, and no additional manual carding work is required.

Figure 202210097198

Description

一种柴油蒸汽裂解反应网络的构建方法A kind of construction method of diesel steam cracking reaction network

技术领域technical field

本发明涉及石油化工领域,具体涉及一种柴油蒸汽裂解反应网络的低成本快速构建方法。The invention relates to the petrochemical field, in particular to a low-cost and rapid construction method of a diesel steam cracking reaction network.

背景技术Background technique

近年来柴油产能过剩现象明显,众多炼厂已将柴油作为蒸汽裂解装置的重要原料之一,用于生产高附加值的低碳烯烃。公开号为CN101139529A、CN105622310A的专利说明书分别将焦化柴油、费托合成柴油进行蒸汽裂解反应,扩大蒸汽裂解制烯烃原料的来源。In recent years, the overcapacity of diesel has become obvious, and many refineries have used diesel as one of the important raw materials for steam cracking units to produce high value-added low-carbon olefins. The patent specifications with publication numbers of CN101139529A and CN105622310A respectively carry out steam cracking reaction of coking diesel oil and Fischer-Tropsch synthetic diesel oil to expand the source of steam cracking to produce olefin raw materials.

众所周知,烃类热裂解遵循自由基机理,其反应过程随机性强,复杂性高。柴油是复杂的烃类混合物,裂解反应路径极为复杂。对于复杂反应过程的动力学建模,传统的反应动力学模型构建方法一般将多种组分进行集总,根据各族组成的已知反应规则或模板,依靠人工手动整理反应路径、估算动力学参数。公开号为CN108108572A的专利说明书对蜡油加氢裂化过程采用六集总动力学模型,以降低反应网络的复杂度。公开号为CN109698014A的专利说明书为催化重整原料建立多个反应规则,遵循制定的反应规则确定原料与产物之间的反应路径。对于柴油这类复杂混合物的蒸汽裂解过程而言,传统的反应动力学模型构建方法费时费力,成本极高,且集总动力学模型或分子反应层面的动力学模型难以准确描述自由基水平的相互作用,特别是杂原子组分对烯烃产物的调控机理。It is well known that the thermal cracking of hydrocarbons follows a free radical mechanism, and the reaction process is highly random and complex. Diesel is a complex hydrocarbon mixture, and the cracking reaction path is extremely complex. For the kinetic modeling of complex reaction processes, the traditional reaction kinetic model building method generally aggregates multiple components, and manually organizes the reaction paths and estimates the kinetics according to the known reaction rules or templates of each family composition. parameter. The patent specification with publication number CN108108572A adopts six lumped kinetic models for the hydrocracking process of wax oil to reduce the complexity of the reaction network. The patent specification with publication number CN109698014A establishes a plurality of reaction rules for catalytic reforming raw materials, and the reaction paths between the raw materials and products are determined according to the established reaction rules. For the steam cracking process of complex mixtures such as diesel, the traditional reaction kinetic model construction method is time-consuming and labor-intensive, and the cost is extremely high, and the lumped kinetic model or the kinetic model of the molecular reaction level is difficult to accurately describe the interaction at the free radical level. effects, especially the regulation mechanism of heteroatom components on olefin products.

随着计算机技术的磅礴发展,反应网络自动生成工具应运而生。借助自动反应网络生成器,能够在较短的时间、人力物力消耗最少的情况下得到自由基水平的详细反应网络。现有文献报道中,反应网络自动生成技术多见用于纯物质的反应网络生成,以及组成相对纯粹的石脑油馏分。With the rapid development of computer technology, the automatic generation tool of reaction network emerges as the times require. With the help of the automatic reaction network generator, detailed reaction networks at the free radical level can be obtained in a short time and with the least consumption of human and material resources. In the existing literature reports, the automatic reaction network generation technology is mostly used for the reaction network generation of pure substances, and the composition of relatively pure naphtha fractions.

柴油相比于传统的石脑油裂解原料,组成更加复杂,重组分含量更高,且含有一定比例的以含硫化合物和含氮化合物为代表的杂原子化合物。柴油馏分的碳原子数可达22,同分异构体随着碳数的增加而呈指数型增长,使得其蒸汽裂解反应网络的规模极为庞大。并且,含硫化合物和含氮化合物的热裂解相比于碳氢化合物更加复杂多变,其中间产物还会对蒸汽裂解制烯烃的结焦过程具有调变作用。Compared with the traditional naphtha cracking feedstock, diesel fuel has a more complex composition, higher content of heavy components, and contains a certain proportion of heteroatom compounds represented by sulfur-containing compounds and nitrogen-containing compounds. The number of carbon atoms in the diesel fraction can reach 22, and the isomers increase exponentially with the increase of carbon number, which makes the scale of the steam cracking reaction network extremely large. In addition, the thermal cracking of sulfur-containing compounds and nitrogen-containing compounds is more complex and changeable than that of hydrocarbons, and the intermediate products also have a modulating effect on the coking process of steam cracking to olefins.

因此,采用自动反应网络生成技术,不仅可以低成本快速构建柴油蒸汽裂解反应网络,还能够实现从自由基层面阐释柴油中烃类物质与含硫化合物和含氮化合物的相互作用,预测柴油蒸汽裂解产物分布。Therefore, the use of automatic reaction network generation technology can not only quickly build a diesel steam cracking reaction network at low cost, but also interpret the interaction of hydrocarbons in diesel with sulfur-containing compounds and nitrogen-containing compounds from the radical level, and predict diesel steam cracking. product distribution.

发明内容SUMMARY OF THE INVENTION

本发明提供了一种柴油蒸汽裂解反应网络的构建方法,构建成本低、速度快,所构建的柴油蒸汽裂解的总反应网络包含了以含硫化合物分子和含氮化合物分子为代表的杂原子组成反应网络,将烃类分子反应网络和含硫化合物、含氮化合物反应网络相耦合。The invention provides a method for constructing a diesel steam cracking reaction network, which has low construction cost and high speed. The constructed overall reaction network of diesel steam cracking includes heteroatoms represented by sulfur-containing compound molecules and nitrogen-containing compound molecules. The reaction network couples the reaction network of hydrocarbon molecules with the reaction network of sulfur-containing compounds and nitrogen-containing compounds.

一种柴油蒸汽裂解反应网络的构建方法,包括步骤:A method for constructing a diesel steam cracking reaction network, comprising the steps of:

(1)对柴油进行成分分析,筛选具有代表性的碳氢化合物分子作为柴油的烃类组成,具有代表性的含硫化合物分子和含氮化合物分子作为柴油的杂原子组成;(1) Carry out component analysis on diesel oil, and screen representative hydrocarbon molecules as the hydrocarbon composition of diesel fuel, and representative sulfur-containing compound molecules and nitrogen-containing compound molecules as the heteroatom composition of diesel fuel;

(2)采用反应网络生成工具Reaction Mechanism Generator(RMG)对烃类组成和杂原子组成中的每一种分子进行单分子的反应网络自动生成;(2) Using the reaction network generation tool Reaction Mechanism Generator (RMG) to automatically generate a single-molecule reaction network for each molecule in the hydrocarbon composition and heteroatom composition;

(3)将生成的所有烃类组成分子和杂原子组成分子的反应网络进行合并,构建柴油蒸汽裂解的总反应网络。(3) The reaction networks of all the generated hydrocarbon constituent molecules and heteroatom constituent molecules are combined to construct the overall reaction network of diesel steam cracking.

步骤(1)中,可采用色谱技术对柴油进行成分分析。In step (1), a chromatographic technique can be used to analyze the components of the diesel oil.

步骤(1)中,所述碳氢化合物分子包括直链烷烃、异构烷烃、烯烃、环烷烃和芳烃。直链烷烃和异构烷烃虽同属烷烃,但其裂解路径和裂解产物分布均差异较大,因此本发明将其区分为两个子类进行分子统计。炔烃由于在柴油中含量极低,可忽略不计。In step (1), the hydrocarbon molecules include straight-chain alkanes, iso-alkanes, alkenes, cycloalkanes and aromatic hydrocarbons. Although straight-chain alkanes and iso-alkanes belong to the same alkanes, their cracking paths and cracking product distributions are quite different, so the present invention divides them into two subclasses for molecular statistics. Alkynes are negligible due to their extremely low content in diesel fuel.

质量分数阈值设置得越低,所筛选出的柴油代表性组成分子越多,越能更加真实地描述柴油组成,但是所需构建的单分子反应网络数目也越多,总体计算耗时越长。而且,含量过低的分子对柴油蒸汽裂解反应过程影响甚微。因此,为了能够近乎真实地描述柴油组成,兼顾效率,步骤(1)中:The lower the mass fraction threshold is set, the more representative components of diesel are screened out, and the more realistic the diesel composition can be described, but the more the number of single-molecule reaction networks that need to be constructed, the longer the overall calculation time is. Moreover, molecules with too low content have little effect on the diesel steam cracking reaction process. Therefore, in order to be able to describe the diesel composition almost realistically, taking into account the efficiency, in step (1):

所述具有代表性的碳氢化合物分子为柴油中质量占比不低于0.3%(优选不低于0.5%)的碳氢化合物分子;The representative hydrocarbon molecules are hydrocarbon molecules whose mass ratio in diesel oil is not less than 0.3% (preferably not less than 0.5%);

所述具有代表性的含硫化合物分子和含氮化合物分子为柴油中质量占比不低于0.05%(优选不低于0.1%)的含硫化合物分子和含氮化合物分子。The representative sulfur-containing compound molecules and nitrogen-containing compound molecules are sulfur-containing compound molecules and nitrogen-containing compound molecules whose mass ratio in diesel fuel is not less than 0.05% (preferably not less than 0.1%).

步骤(2)中,单分子的反应网络自动生成过程为指定对应单分子反应系统的温度、压力、反应物分子种类及比例、终止条件和用户自定义容差因子,启动反应网络生成工具Reaction Mechanism Generator执行该反应系统的自动反应网络生成。In step (2), the automatic generation process of the single-molecule reaction network is to specify the temperature, pressure, species and proportion of reactant molecules, termination conditions and user-defined tolerance factors of the corresponding single-molecule reaction system, and start the reaction network generation tool Reaction Mechanism. Generator performs automatic reactive network generation for this reactive system.

单分子的反应网络自动生成过程中,反应系统的温度可设置为780~900℃,此温度范围属于常规的蒸汽裂解炉温度操作范围。对于自动反应网络生成而言,高温的反应系统能够兼容低温的反应系统,温度设置越高,反应网络越详细,但单个反应网络的计算耗时也越长。基于此,反应系统的温度优选设置为800~850℃,更优选设置为820~850℃。During the automatic generation of the reaction network of the single molecule, the temperature of the reaction system can be set to 780-900°C, which belongs to the normal operating range of the steam cracking furnace. For automatic reaction network generation, high-temperature reaction systems can be compatible with low-temperature reaction systems. The higher the temperature setting, the more detailed the reaction network is, but the calculation time of a single reaction network is also longer. Based on this, the temperature of the reaction system is preferably set to 800 to 850°C, more preferably 820 to 850°C.

单分子的反应网络自动生成过程中,反应系统的压力可设置为0.1~0.3MPa,此压力范围属于常规的蒸汽裂解炉压力操作范围。During the automatic generation of the single-molecule reaction network, the pressure of the reaction system can be set to 0.1-0.3 MPa, which belongs to the conventional steam cracking furnace pressure operating range.

单分子的反应网络自动生成过程中,进料组成优选为对应烃类组成分子或杂原子组成分子和水分子,其中水分子仅作为进料组成分子,不具有反应性。对应烃类组成分子或杂原子组成分子和水分子的质量比可以为1~2:1,此稀释比范围属于常规的蒸汽裂解炉稀释比操作范围。In the process of automatic generation of a single-molecule reaction network, the feed composition is preferably the corresponding hydrocarbon constituent molecules or heteroatom constituent molecules and water molecules, wherein the water molecules only serve as the feed constituent molecules and have no reactivity. The mass ratio of the corresponding hydrocarbon constituent molecules or heteroatom constituent molecules and water molecules can be 1-2:1, and this dilution ratio range belongs to the conventional steam cracking furnace dilution ratio operation range.

终止条件设置的摩尔转化率越高,反应网络越详细,但计算耗时越长。单分子的反应网络自动生成过程中,终止条件优选为对应烃类组成分子或杂原子组成分子的摩尔转化率大于85%,进一步优选为对应烃类组成分子或杂原子组成分子的摩尔转化率为90%~95%。The higher the molar conversion of the termination conditions, the more detailed the reaction network, but the longer the calculation time. In the process of automatically generating the reaction network of the single molecule, the termination condition is preferably that the molar conversion rate of the corresponding hydrocarbon constituent molecule or heteroatom constituent molecule is greater than 85%, and more preferably the molar conversion ratio of the corresponding hydrocarbon constituent molecule or heteroatom constituent molecule is. 90% to 95%.

用户自定义容差因子是区分被包含在反应网络中的核心反应和被剔除的边缘反应的判据。该值对反应网络规模、计算时长的影响都很大。容差因子越小,反应网络越详细,但单个反应网络的计算耗时越长。单分子的反应网络自动生成过程中,用户自定义容差因子优选设置为0.5~0.01。进一步优选设置为0.1~0.01,更进一步优选设置为0.05~0.03。The user-defined tolerance factor is a criterion for distinguishing the core reactions included in the reaction network from the marginal reactions that are excluded. This value has a great influence on the scale of the reaction network and the calculation time. The smaller the tolerance factor, the more detailed the reaction network, but the longer the computation time of a single reaction network. In the process of automatic generation of single molecule reaction network, the user-defined tolerance factor is preferably set to 0.5~0.01. It is more preferable to set it as 0.1-0.01, and it is still more preferable to set it as 0.05-0.03.

考虑到先合并的网络在合并过程中具有优先权,即相同的反应路径将以先合并的网络为准,步骤(3)中,总反应网络的合并规则为含硫化合物反应网络和含氮化合物反应网络先合并成网络1,目的是将含硫化合物和含氮化合物的反应网络完整保留,在网络1基础上合并芳烃反应网络得到网络2,目的是将芳烃反应网络尽可能保留,在网络2基础上合并环烷烃反应网络得到网络3,目的是将环烷烃反应网络尽可能保留,在网络3基础上合并直链烷烃反应网络得到网络4,直链烷烃反应网络会包含一部分芳烃、环烷烃的反应路径,故放置于网络3后再合并,在网络4基础上合并异构烷烃反应网络得到网络5,异构烷烃反应网络会包含一部分芳烃、环烷烃、直链烷烃的反应路径,故放置于网络4后再合并,最后在网络5基础上合并烯烃反应网络得到柴油蒸汽裂解的总反应网络,烯烃既是裂解原料,同时也是烃类物质的重要裂解产物,芳烃、环烷烃、直链烷烃、异构烷烃的反应网络已包含了部分重要的烯烃裂解路径,故将烯烃反应网络放置于最后合并,使得其他类型的碳氢化合物分子的烯烃裂解路径保持完整。Considering that the first merged network has priority in the merging process, that is, the same reaction path will be subject to the first merged network, in step (3), the merging rule of the total reaction network is the sulfur-containing compound reaction network and the nitrogen-containing compound reaction network. The reaction network is first merged into network 1, the purpose is to keep the reaction network of sulfur-containing compounds and nitrogen-containing compounds intact, and the aromatic hydrocarbon reaction network is merged on the basis of network 1 to obtain network 2, the purpose is to keep the aromatic hydrocarbon reaction network as much as possible, in network 2. On the basis of combining the naphthenic reaction network to obtain the network 3, the purpose is to keep the naphthenic reaction network as much as possible. On the basis of the network 3, the straight-chain alkane reaction network is combined to obtain the network 4. The reaction path is placed in network 3 and then merged. On the basis of network 4, the isoparaffin reaction network is combined to obtain network 5. The isoparaffin reaction network will contain a part of the reaction paths of aromatic hydrocarbons, naphthenes and linear alkanes, so it is placed in the network 4. Network 4 is then merged, and finally the olefin reaction network is combined on the basis of network 5 to obtain the overall reaction network of diesel steam cracking. The reaction network of paraffins already contains some important olefin cracking paths, so the olefin reaction network is placed in the last merge, so that the olefin cracking paths of other types of hydrocarbon molecules remain intact.

本发明与现有技术相比,主要优点包括:Compared with the prior art, the main advantages of the present invention include:

(1)可以低成本、短时间内获取柴油蒸汽裂解自由基机理水平的反应网络及相应动力学参数,所需时间仅为RMG程序运行时长,无需额外的人工梳理工作;(1) The reaction network and the corresponding kinetic parameters of the diesel steam cracking radical mechanism level can be obtained at low cost and in a short time, and the time required is only the running time of the RMG program, and no additional manual carding work is required;

(2)采用色谱分析结果作为挑选柴油代表性分子的依据,分别为烃类组成和杂原子组成设定最低质量含量阈值作为选取分子的标准,近乎真实地描述参与蒸汽裂解反应的柴油组成;(2) The chromatographic analysis results are used as the basis for selecting representative molecules of diesel oil, and the minimum mass content thresholds are respectively set for hydrocarbon composition and heteroatom composition as the standard for selecting molecules, and the composition of diesel oil participating in the steam cracking reaction is almost truly described;

(3)将杂原子化合物分子的反应网络作为RMG网络合并的第一步,避免了与含硫化合物和含氮化合物相关的基元反应在网络合并过程中被覆盖。(3) Taking the reaction network of heteroatom compound molecules as the first step of RMG network merging, it avoids that the elementary reactions related to sulfur-containing compounds and nitrogen-containing compounds are covered during the network merging process.

附图说明Description of drawings

图1为本发明提出的一种构建柴油蒸汽裂解反应网络的流程图。Fig. 1 is a flow chart of constructing a diesel steam cracking reaction network proposed by the present invention.

具体实施方式Detailed ways

下面结合附图及具体实施例,进一步阐述本发明。应理解,这些实施例仅用于说明本发明而不用于限制本发明的范围。下列实施例中未注明具体条件的操作方法,通常按照常规条件,或按照制造厂商所建议的条件。The present invention will be further described below with reference to the accompanying drawings and specific embodiments. It should be understood that these examples are only used to illustrate the present invention and not to limit the scope of the present invention. The operation method without specifying the specific conditions in the following examples is usually in accordance with the conventional conditions, or in accordance with the conditions suggested by the manufacturer.

如图1所示,将柴油样品送入色谱分析仪进行成分分析,根据色谱结果筛选具有代表性的碳氢化合物分子作为柴油的烃类组成,以及具有代表性的含硫化合物分子和含氮化合物分子作为柴油的杂原子组成;采用反应网络生成工具RMG对每一种柴油的烃类组成和杂原子组成进行单分子的反应网络自动生成;根据特定的合并规则将生成的所有柴油烃类组成分子和杂原子组成分子的反应网络进行合并,得到柴油蒸汽裂解的总反应网络。烃类组成分子包括直链烷烃、异构烷烃、烯烃、环烷烃和芳烃。合并规则为含硫化合物反应网络和含氮化合物反应网络先合并成网络1,在网络1基础上合并芳烃反应网络得到网络2,在网络2基础上合并环烷烃反应网络得到网络3,在网络3基础上合并直链烷烃反应网络得到网络4,在网络4基础上合并异构烷烃反应网络得到网络5,最后在网络5基础上合并烯烃反应网络得到柴油蒸汽裂解的总反应网络。As shown in Figure 1, the diesel sample is sent to a chromatographic analyzer for component analysis. According to the chromatographic results, representative hydrocarbon molecules are screened as the hydrocarbon composition of diesel, as well as representative sulfur-containing compound molecules and nitrogen-containing compounds. Molecules are used as the heteroatom composition of diesel; the reaction network generation tool RMG is used to automatically generate a single molecule reaction network for the hydrocarbon composition and heteroatom composition of each diesel; all diesel hydrocarbons are composed of molecules according to specific merging rules. Combined with the reaction network of heteroatom constituent molecules to obtain the overall reaction network of diesel steam cracking. The hydrocarbon constituent molecules include linear paraffins, isoparaffins, olefins, naphthenes and aromatics. The merging rule is that the reaction network of sulfur-containing compounds and the reaction network of nitrogen-containing compounds are first merged into network 1, the aromatic hydrocarbon reaction network is merged on the basis of network 1 to obtain network 2, the cycloalkane reaction network is merged on the basis of network 2 to obtain network 3, and the network 3 On the basis of merging the linear alkane reaction network to obtain network 4, merging the isoparaffin reaction network on the basis of network 4 to obtain network 5, and finally merging the olefin reaction network on the basis of network 5 to obtain the total reaction network of diesel steam cracking.

实施例1Example 1

将柴油样品送入色谱分析仪进行成分分析,该色谱分析仪具有烃类分子、含硫化合物分子和氮化合物分子分析功能。依据得到的色谱分析结果,对所有检测到的柴油组分质量分数进行归一化,将质量分数不低于0.3%的碳氢化合物分子作为柴油的烃类组成,将质量分数不低于0.05%的含硫化合物分子和含氮化合物分子作为柴油的杂原子组成,共同作为代表性分子描述柴油的组分情况。总计筛选出121种碳氢化合物分子,碳原子数目范围为10~22;9种含硫化合物分子,分别为硫醇类、硫化物类、噻吩类、苯并噻苯类等;4种含氮化合物分子,分别为吡啶类、吡咯类、四氢吡咯类等。The diesel sample is sent to a chromatographic analyzer for component analysis. The chromatographic analyzer has the functions of analyzing hydrocarbon molecules, sulfur-containing compound molecules and nitrogen compound molecules. According to the obtained chromatographic analysis results, the mass fractions of all detected diesel components are normalized, and the hydrocarbon molecules with a mass fraction of not less than 0.3% are taken as the hydrocarbon composition of diesel oil, and the mass fraction of not less than 0.05% The sulfur-containing compound molecules and nitrogen-containing compound molecules are composed of heteroatoms of diesel fuel, and together they are used as representative molecules to describe the composition of diesel fuel. A total of 121 kinds of hydrocarbon molecules were screened, with the number of carbon atoms ranging from 10 to 22; 9 kinds of sulfur-containing compound molecules, namely mercaptans, sulfides, thiophenes, benzothiophenes, etc.; 4 kinds of nitrogen-containing compounds Compound molecules are pyridines, pyrroles, tetrahydropyrroles, etc.

采用反应网络生成工具Reaction Mechanism Generator为上述134种柴油代表性分子进行单分子的反应网络自动生成。所有单分子反应系统的温度统一设置为900℃,压力设置为0.2MPa,进料组成为对应柴油烃类组成分子或杂原子组成分子和水分子,二者的质量比设置为1:1,用户自定义容差因子设置为0.01,终止条件设置为对应柴油烃类组成分子或杂原子组成分子的摩尔转化率达到99%。启动反应网络生成工具Reaction MechanismGenerator,执行每一个单分子反应系统的自动反应网络生成。134个单分子反应网络生成的平均耗时为12.1小时,反应网络的平均规模为316个物种,6894个反应。The reaction network generation tool Reaction Mechanism Generator was used to automatically generate single-molecule reaction networks for the above 134 representative molecules of diesel. The temperature of all single-molecule reaction systems is uniformly set to 900°C, the pressure is set to 0.2MPa, the feed composition is the corresponding diesel hydrocarbon molecules or heteroatom molecules and water molecules, and the mass ratio of the two is set to 1:1. The custom tolerance factor was set to 0.01, and the termination condition was set to achieve 99% molar conversion of the corresponding diesel hydrocarbon constituent molecules or heteroatom constituent molecules. Start the reaction network generation tool Reaction MechanismGenerator to perform automatic reaction network generation for each single-molecule reaction system. The average time taken to generate the 134 single-molecule reaction networks was 12.1 hours, and the average size of the reaction networks was 316 species with 6894 reactions.

将上述得到的134个单分子反应网络按照如下合并规则进行反应网络合并:9种含硫化合物分子和4种含氮化合物分子的反应网络之间先合并成网络1,网络1的规模为3898个物种,60156个反应;在网络1的基础上合并碳氢化合物分子中的8种芳烃分子反应网络,得到网络2,网络2规模为6011个物种,98995个反应;在网络2的基础上合并碳氢化合物分子中的14种环烷烃分子反应网络,得到网络3,网络3规模为10231个物种,113754个反应;在网络3的基础上合并碳氢化合物分子中的13种直链烷烃分子反应网络,得到网络4,网络4规模为13131个物种,147565个反应;在网络4的基础上合并碳氢化合物分子中的79种异构烷烃分子反应网络,得到网络4,网络4规模为16523个物种,171322个反应;在网络5的基础上合并碳氢化合物分子中的7种烯烃分子反应网络最终得到柴油蒸汽裂解的总反应网络,总反应网络规模为17344个物种,174325个反应。The 134 single-molecule reaction networks obtained above were merged according to the following merging rules: the reaction networks of 9 kinds of sulfur-containing compound molecules and 4 kinds of nitrogen-containing compound molecules were first merged into network 1, and the scale of network 1 was 3898. Species, 60,156 reactions; 8 kinds of aromatic hydrocarbon molecules in hydrocarbon molecules were merged on the basis of network 1. Reaction network was obtained to obtain network 2, and the scale of network 2 was 6011 species, 98,995 reactions; on the basis of network 2, carbon The reaction network of 14 kinds of cycloalkane molecules in hydrogen compound molecules is obtained, and network 3 is obtained. The scale of network 3 is 10,231 species and 113,754 reactions; on the basis of network 3, the reaction network of 13 kinds of linear alkane molecules in hydrocarbon molecules is merged , obtain network 4, the scale of network 4 is 13131 species, 147565 reactions; on the basis of network 4, the reaction network of 79 isoalkane molecules in hydrocarbon molecules is merged, and network 4 is obtained, and the scale of network 4 is 16523 species , 171322 reactions; on the basis of network 5, 7 kinds of olefin molecular reaction networks in hydrocarbon molecules were merged and finally the total reaction network of diesel steam cracking was obtained. The total reaction network scale was 17344 species and 174325 reactions.

上述得到的柴油蒸汽裂解总反应网络采用了较低的质量分数阈值来筛选代表性分子,同时采用了较高的反应温度、较低的用户自定义容差因子、较高的目标转化率,故反应网络规模庞大,反应网络中物种数目达到约1.7万,反应数目高达约17万,能够非常详细地描述柴油蒸汽裂解自由基反应过程。The overall reaction network of diesel steam cracking obtained above uses a lower mass fraction threshold to screen representative molecules, and at the same time adopts a higher reaction temperature, a lower user-defined tolerance factor, and a higher target conversion rate, so The scale of the reaction network is huge, the number of species in the reaction network reaches about 17,000, and the number of reactions is as high as about 170,000, which can describe the diesel steam cracking radical reaction process in great detail.

实施例2Example 2

采用与实施例1相同的柴油样品送入色谱分析仪进行烃类分子、含硫化合物分子和氮化合物分子含量分析。依据得到的色谱分析结果,对所有检测到的柴油组分质量分数进行归一化,将质量分数不低于0.5%的碳氢化合物分子作为柴油的烃类组成,将质量分数不低于0.1%的含硫化合物分子和含氮化合物分子作为柴油的杂原子组成,共同作为代表性分子描述柴油的组分情况。总计92种碳氢化合物分子,碳原子数目范围为10~22;5种含硫化合物分子,分别为硫醇类、硫化物类、噻吩类、苯并噻苯类等;2种含氮化合物分子,分别为吡啶类、吡咯类等。The same diesel sample as in Example 1 was used to send the chromatographic analyzer to analyze the content of hydrocarbon molecules, sulfur-containing compound molecules and nitrogen compound molecules. According to the obtained chromatographic analysis results, the mass fractions of all detected diesel components are normalized, and the hydrocarbon molecules with a mass fraction of not less than 0.5% are taken as the hydrocarbon composition of diesel oil, and the mass fraction of not less than 0.1% The sulfur-containing compound molecules and nitrogen-containing compound molecules are composed of heteroatoms of diesel fuel, and together they are used as representative molecules to describe the composition of diesel fuel. A total of 92 kinds of hydrocarbon molecules, the number of carbon atoms ranges from 10 to 22; 5 kinds of sulfur-containing compound molecules, namely mercaptans, sulfides, thiophenes, benzothiophenes, etc.; 2 kinds of nitrogen-containing compound molecules , respectively, pyridines, pyrroles, etc.

采用反应网络生成工具Reaction Mechanism Generator为上述99种柴油代表性分子进行单分子的反应网络自动生成。所有单分子反应系统的温度统一设置为850℃,压力设置为0.2MPa,进料组成为对应柴油烃类组成分子或杂原子组成分子和水分子,二者的质量比设置为1:1,用户自定义容差因子设置为0.01,终止条件设置为对应柴油烃类组成分子或杂原子组成分子的摩尔转化率达到99%。启动反应网络生成工具Reaction MechanismGenerator,执行每一个单分子反应系统的自动反应网络生成。99个单分子反应网络生成的平均耗时为11.9小时,反应网络的平均规模为325个物种,6822个反应。The reaction network generation tool Reaction Mechanism Generator was used to automatically generate single-molecule reaction networks for the above 99 representative molecules of diesel. The temperature of all single-molecule reaction systems is uniformly set to 850°C, the pressure is set to 0.2MPa, the feed composition is the corresponding diesel hydrocarbon molecules or heteroatom molecules and water molecules, and the mass ratio of the two is set to 1:1. The custom tolerance factor was set to 0.01, and the termination condition was set to achieve 99% molar conversion of the corresponding diesel hydrocarbon constituent molecules or heteroatom constituent molecules. Start the reaction network generation tool Reaction MechanismGenerator to perform automatic reaction network generation for each single-molecule reaction system. The average time taken to generate the 99 single-molecule reaction networks was 11.9 hours, and the average size of the reaction networks was 325 species and 6822 reactions.

将上述得到的99个单分子反应网络按照如下合并规则进行反应网络合并:5种含硫化合物分子和2种含氮化合物分子的反应网络之间先合并成网络1,网络1的规模为2101个物种,32076个反应;在网络1的基础上合并碳氢化合物分子中的5种芳烃分子反应网络,得到网络2,网络2规模为3799个物种,60655个反应;在网络2的基础上合并碳氢化合物分子中的10种环烷烃分子反应网络,得到网络3,网络3规模为6569个物种,99231个反应;在网络3的基础上合并碳氢化合物分子中的13种直链烷烃分子反应网络,得到网络4,网络4规模为9469个物种,133042个反应;在网络4的基础上合并碳氢化合物分子中的64种异构烷烃分子反应网络,得到网络4,网络4规模为12754个物种,149952个反应;在网络5的基础上合并碳氢化合物分子中的7种烯烃分子反应网络最终得到柴油蒸汽裂解的总反应网络,总反应网络规模为13365个物种,152134个反应。The 99 single-molecule reaction networks obtained above were merged according to the following merging rules: the reaction networks of 5 kinds of sulfur-containing compound molecules and 2 kinds of nitrogen-containing compound molecules were first merged into network 1, and the scale of network 1 was 2101. Species, 32,076 reactions; 5 kinds of aromatic hydrocarbon molecules in hydrocarbon molecules were merged on the basis of network 1. Reaction network was obtained, and network 2 was obtained. The scale of network 2 was 3,799 species and 60,655 reactions; on the basis of network 2, carbon The reaction network of 10 kinds of cycloalkane molecules in hydrogen compound molecules was obtained, and the scale of network 3 was 6569 species and 99231 reactions; on the basis of network 3, the reaction network of 13 kinds of linear alkane molecules in hydrocarbon molecules was merged , obtain network 4, the scale of network 4 is 9469 species, 133042 reactions; on the basis of network 4, the reaction network of 64 isoalkane molecules in hydrocarbon molecules is merged to obtain network 4, the scale of network 4 is 12754 species , 149952 reactions; on the basis of network 5, 7 kinds of olefin molecular reaction networks in hydrocarbon molecules were merged and finally the total reaction network of diesel steam cracking was obtained. The total reaction network scale was 13365 species and 152134 reactions.

相比于实施例1,本实施例中得到的柴油蒸汽裂解总反应网络采用了相对较高的质量分数阈值来筛选代表性分子,使得代表性分子的数目从134降低至99,最终总反应网络中物种数目降低至约1.3万,反应数目降低至约15万,与试验结果相符。该网络同样能够详细地描述柴油蒸汽裂解自由基反应过程。Compared with Example 1, the overall reaction network of diesel steam cracking obtained in this example adopts a relatively high mass fraction threshold to screen representative molecules, so that the number of representative molecules is reduced from 134 to 99, and the final overall reaction network The number of medium species was reduced to about 13,000, and the number of reactions was reduced to about 150,000, which was consistent with the experimental results. The network can also describe the diesel steam cracking radical reaction process in detail.

实施例3Example 3

采用与实施例2相同的柴油样品、相同的质量分数阈值筛选代表性分子,即将质量分数不低于0.5%的碳氢化合物分子作为柴油的烃类组成,将质量分数不低于0.1%的含硫化合物分子和含氮化合物分子作为柴油的杂原子组成。总计92种碳氢化合物分子,碳原子数目范围为10~22;5种含硫化合物分子,分别为硫醇类、硫化物类、噻吩类、苯并噻苯类等;2种含氮化合物分子,分别为吡啶类、吡咯类等。The same diesel sample and the same mass fraction threshold as in Example 2 are used to screen representative molecules, that is, hydrocarbon molecules with a mass fraction of not less than 0.5% are taken as the hydrocarbon composition of diesel oil, and the mass fraction of not less than 0.1% of the hydrocarbon molecules Sulfur compound molecules and nitrogen-containing compound molecules are composed as heteroatoms of diesel fuel. A total of 92 kinds of hydrocarbon molecules, the number of carbon atoms ranges from 10 to 22; 5 kinds of sulfur-containing compound molecules, namely mercaptans, sulfides, thiophenes, benzothiophenes, etc.; 2 kinds of nitrogen-containing compound molecules , respectively, pyridines, pyrroles, etc.

采用反应网络生成工具Reaction Mechanism Generator为上述99种柴油代表性分子进行单分子的反应网络自动生成。所有单分子反应系统的温度统一设置为850℃,压力设置为0.2MPa,进料组成为对应柴油烃类组成分子或杂原子组成分子和水分子,二者的质量比设置为1:1,用户自定义容差因子设置为0.05,终止条件设置为对应柴油烃类组成分子或杂原子组成分子的摩尔转化率达到90%。启动反应网络生成工具Reaction MechanismGenerator,执行每一个单分子反应系统的自动反应网络生成。99个单分子反应网络生成的平均耗时为9.3小时,反应网络的平均规模为239个物种,4821个反应。The reaction network generation tool Reaction Mechanism Generator was used to automatically generate single-molecule reaction networks for the above 99 representative molecules of diesel. The temperature of all single-molecule reaction systems is uniformly set to 850°C, the pressure is set to 0.2MPa, the feed composition is the corresponding diesel hydrocarbon molecules or heteroatom molecules and water molecules, and the mass ratio of the two is set to 1:1. The custom tolerance factor was set to 0.05, and the termination condition was set to achieve 90% molar conversion of the corresponding diesel hydrocarbon constituent molecules or heteroatom constituent molecules. Start the reaction network generation tool Reaction MechanismGenerator to perform automatic reaction network generation for each single-molecule reaction system. The average time taken to generate the 99 single-molecule reaction networks was 9.3 hours, and the average size of the reaction networks was 239 species and 4821 reactions.

将上述得到的99个单分子反应网络按照如下合并规则进行反应网络合并:5种含硫化合物分子和2种含氮化合物分子的反应网络之间先合并成网络1,网络1的规模为1203个物种,22345个反应;在网络1的基础上合并碳氢化合物分子中的5种芳烃分子反应网络,得到网络2,网络2规模为2210个物种,41523个反应;在网络2的基础上合并碳氢化合物分子中的10种环烷烃分子反应网络,得到网络3,网络3规模为4021个物种,69231个反应;在网络3的基础上合并碳氢化合物分子中的13种直链烷烃分子反应网络,得到网络4,网络4规模为6112个物种,93326个反应;在网络4的基础上合并碳氢化合物分子中的64种异构烷烃分子反应网络,得到网络4,网络4规模为8044个物种,104252个反应;在网络5的基础上合并碳氢化合物分子中的7种烯烃分子反应网络最终得到柴油蒸汽裂解的总反应网络,总反应网络规模为8116个物种,105713个反应。The 99 single-molecule reaction networks obtained above were merged according to the following merging rules: the reaction networks of 5 kinds of sulfur-containing compound molecules and 2 kinds of nitrogen-containing compound molecules were first merged into network 1, and the scale of network 1 was 1203. Species, 22345 reactions; merging 5 kinds of aromatic hydrocarbon molecular reaction networks in hydrocarbon molecules on the basis of network 1, obtaining network 2, the scale of network 2 is 2210 species, 41523 reactions; on the basis of network 2, merging carbon The 10 kinds of cycloalkane molecules in the hydrogen compound molecules reacted to the network, and the network 3 was obtained, and the scale of the network 3 was 4021 species and 69,231 reactions; on the basis of the network 3, the 13 kinds of linear alkane molecules in the hydrocarbon molecules were merged. The reaction network , obtain network 4, the scale of network 4 is 6112 species, 93326 reactions; on the basis of network 4, the reaction network of 64 isoalkane molecules in hydrocarbon molecules is merged, and network 4 is obtained, and the scale of network 4 is 8044 species , 104252 reactions; on the basis of network 5, 7 kinds of olefin molecular reaction networks in hydrocarbon molecules were merged, and finally the total reaction network of diesel steam cracking was obtained, and the total reaction network scale was 8116 species and 105713 reactions.

相比于实施例2,本实施例中得到的柴油蒸汽裂解总反应网络采用了中等的反应温度、中等的用户自定义容差因子、较低的目标转化率,在代表性分子的数目不变的基础上,使得最终总反应网络中物种数目进一步降低至约8000,反应数目进一步降低至约10万,与试验结果相符。该网络依旧能够详细地描述柴油蒸汽裂解自由基反应过程。Compared with Example 2, the overall reaction network of diesel steam cracking obtained in this example adopts a moderate reaction temperature, a moderate user-defined tolerance factor, and a low target conversion rate, and the number of representative molecules remains unchanged. On the basis of , the number of species in the final total reaction network was further reduced to about 8,000, and the number of reactions was further reduced to about 100,000, which was consistent with the experimental results. The network is still able to describe the diesel steam cracking radical reaction process in detail.

此外应理解,在阅读了本发明的上述描述内容之后,本领域技术人员可以对本发明作各种改动或修改,这些等价形式同样落于本申请所附权利要求书所限定的范围。In addition, it should be understood that after reading the above description of the present invention, those skilled in the art can make various changes or modifications to the present invention, and these equivalent forms also fall within the scope defined by the appended claims of the present application.

Claims (10)

1.一种柴油蒸汽裂解反应网络的构建方法,其特征在于,包括步骤:1. a construction method of diesel steam cracking reaction network, is characterized in that, comprises the steps: (1)对柴油进行成分分析,筛选具有代表性的碳氢化合物分子作为柴油的烃类组成,具有代表性的含硫化合物分子和含氮化合物分子作为柴油的杂原子组成;(1) Carry out component analysis on diesel oil, and screen representative hydrocarbon molecules as the hydrocarbon composition of diesel fuel, and representative sulfur-containing compound molecules and nitrogen-containing compound molecules as the heteroatom composition of diesel fuel; (2)采用反应网络生成工具Reaction Mechanism Generator对烃类组成和杂原子组成中的每一种分子进行单分子的反应网络自动生成;(2) Using the reaction network generation tool Reaction Mechanism Generator to automatically generate a single-molecule reaction network for each molecule in the hydrocarbon composition and heteroatom composition; (3)将生成的所有烃类组成分子和杂原子组成分子的反应网络进行合并,构建柴油蒸汽裂解的总反应网络。(3) The reaction networks of all the generated hydrocarbon constituent molecules and heteroatom constituent molecules are combined to construct the overall reaction network of diesel steam cracking. 2.根据权利要求1所述的构建方法,其特征在于,步骤(1)中,所述碳氢化合物分子包括直链烷烃、异构烷烃、烯烃、环烷烃和芳烃。2. construction method according to claim 1, is characterized in that, in step (1), described hydrocarbon molecule comprises straight chain alkane, isoalkane, alkene, cycloalkane and aromatic hydrocarbon. 3.根据权利要求1所述的构建方法,其特征在于,步骤(1)中:3. construction method according to claim 1, is characterized in that, in step (1): 所述具有代表性的碳氢化合物分子为柴油中质量占比不低于0.3%的碳氢化合物分子;The representative hydrocarbon molecules are hydrocarbon molecules whose mass ratio in diesel is not less than 0.3%; 所述具有代表性的含硫化合物分子和含氮化合物分子为柴油中质量占比不低于0.05%的含硫化合物分子和含氮化合物分子。The representative sulfur-containing compound molecules and nitrogen-containing compound molecules are sulfur-containing compound molecules and nitrogen-containing compound molecules whose mass ratio in diesel fuel is not less than 0.05%. 4.根据权利要求1所述的构建方法,其特征在于,步骤(2)中,单分子的反应网络自动生成过程为指定对应单分子反应系统的温度、压力、反应物分子种类及比例、终止条件和用户自定义容差因子,启动反应网络生成工具Reaction Mechanism Generator执行该反应系统的自动反应网络生成。4. construction method according to claim 1 is characterized in that, in step (2), the reaction network automatic generation process of monomolecular is to specify temperature, pressure, reactant molecular species and ratio, termination of corresponding monomolecular reaction system Conditions and user-defined tolerance factors, start the reaction network generation tool Reaction Mechanism Generator to perform automatic reaction network generation for the reaction system. 5.根据权利要求4所述的构建方法,其特征在于,单分子的反应网络自动生成过程中,反应系统的温度设置为780~900℃。5 . The construction method according to claim 4 , wherein, during the automatic generation of the reaction network of the single molecule, the temperature of the reaction system is set to 780-900° C. 6 . 6.根据权利要求4所述的构建方法,其特征在于,单分子的反应网络自动生成过程中,反应系统的压力设置为0.1~0.3MPa。6 . The construction method according to claim 4 , wherein, during the automatic generation of the reaction network of the single molecule, the pressure of the reaction system is set to 0.1-0.3 MPa. 7 . 7.根据权利要求4所述的构建方法,其特征在于,单分子的反应网络自动生成过程中,进料组成为对应烃类组成分子或杂原子组成分子和水分子,二者的质量比为1~2:1。7. construction method according to claim 4 is characterized in that, in the automatic generation process of the reaction network of monomolecular, feed is composed of corresponding hydrocarbon composition molecule or heteroatom composition molecule and water molecule, and the mass ratio of the two is 1 to 2:1. 8.根据权利要求4所述的构建方法,其特征在于,单分子的反应网络自动生成过程中,终止条件为对应烃类组成分子或杂原子组成分子的摩尔转化率大于85%。8 . The construction method according to claim 4 , wherein, in the process of automatically generating the reaction network of the single molecule, the termination condition is that the molar conversion rate of the corresponding hydrocarbon constituent molecule or heteroatom constituent molecule is greater than 85%. 9 . 9.根据权利要求4所述的构建方法,其特征在于,单分子的反应网络自动生成过程中,用户自定义容差因子设置为0.5~0.01。9 . The construction method according to claim 4 , wherein, in the process of automatically generating the reaction network of the single molecule, a user-defined tolerance factor is set to 0.5-0.01. 10 . 10.根据权利要求2所述的构建方法,其特征在于,步骤(3)中,总反应网络的合并规则为含硫化合物反应网络和含氮化合物反应网络先合并成网络1,在网络1基础上合并芳烃反应网络得到网络2,在网络2基础上合并环烷烃反应网络得到网络3,在网络3基础上合并直链烷烃反应网络得到网络4,在网络4基础上合并异构烷烃反应网络得到网络5,最后在网络5基础上合并烯烃反应网络得到柴油蒸汽裂解的总反应网络。10. construction method according to claim 2 is characterized in that, in step (3), the merging rule of total reaction network is that sulfur-containing compound reaction network and nitrogen-containing compound reaction network merge into network 1 first, in network 1 basis. On the basis of network 2, combining the cycloalkane reaction network to obtain network 3, combining the linear alkane reaction network on the basis of network 3 to obtain network 4, and combining the isoparaffin reaction network on the basis of network 4 to obtain network 2 Network 5. Finally, the olefin reaction network is combined on the basis of network 5 to obtain the overall reaction network of diesel steam cracking.
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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20160369190A1 (en) * 2013-07-02 2016-12-22 Andrew Mark Ward Method of producing aromatics and light olefins from a hydrocarbon feedstock
CN109698014A (en) * 2018-09-25 2019-04-30 中国石油天然气股份有限公司 Prediction method for catalytic reforming products
CN111892953A (en) * 2020-06-12 2020-11-06 中国石油天然气股份有限公司 Method, system, equipment and storage medium for determining crude oil molecular conversion path
CN112662423A (en) * 2019-10-16 2021-04-16 中国石油天然气股份有限公司 Process simulation method for catalytic gasoline hydro-upgrading process
CN113223625A (en) * 2021-05-07 2021-08-06 中国石油化工股份有限公司 Catalytic cracking reaction process modeling method and device
CN113903405A (en) * 2021-09-26 2022-01-07 清华大学 Simulation system, prediction method and medium for predicting diesel autothermal reforming reaction

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20160369190A1 (en) * 2013-07-02 2016-12-22 Andrew Mark Ward Method of producing aromatics and light olefins from a hydrocarbon feedstock
CN109698014A (en) * 2018-09-25 2019-04-30 中国石油天然气股份有限公司 Prediction method for catalytic reforming products
CN112662423A (en) * 2019-10-16 2021-04-16 中国石油天然气股份有限公司 Process simulation method for catalytic gasoline hydro-upgrading process
CN111892953A (en) * 2020-06-12 2020-11-06 中国石油天然气股份有限公司 Method, system, equipment and storage medium for determining crude oil molecular conversion path
CN113223625A (en) * 2021-05-07 2021-08-06 中国石油化工股份有限公司 Catalytic cracking reaction process modeling method and device
CN113903405A (en) * 2021-09-26 2022-01-07 清华大学 Simulation system, prediction method and medium for predicting diesel autothermal reforming reaction

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
AL JAMRI, MO等HAMED: "Molecular Modeling of Coprocessing Biomass Fast Pyrolysis Oil in Fluid Catalytic Cracking Unit", 《 INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH》, 25 February 2020 (2020-02-25) *
侯亚洲;魏晓丽;毛安国;: "直馏柴油催化裂化生产轻质芳烃的研究", 石油炼制与化工, no. 10, 12 October 2017 (2017-10-12) *
杜志国;王国清;李蔚;张永刚;张兆斌;张利军;: "烃类蒸汽裂解反应动力学模型进展", 《乙烯工业》, no. 01, 25 March 2010 (2010-03-25) *

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