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双语推荐:费托合成

建立了铁基催化剂费托合成反应水相产物中低碳(C1~C8)醇、醛、酮的气相色谱测定方法。对色谱分离条件进行了优化,确立了以乙醇为基准物质并结合各组分校正因子的定量方法;考察了方法的精密度和准确度,并对费托合成反应水相产物样品进行了测定。结果表明,乙醇在不同的含量范围内呈现良好的线性关系,相关系数均大于0.99。费托合成水相产物中的加标回收率在93.4%~109.6%之间,准确性可以满足实际分析的需要。实际费托合成水相产物的分析结果表明,费托合成水相产物中主要的低碳醇、醛、酮的总质量分数约为3%~12%,乙醇含量最高(约为1.7%~7.3%),且正构醇、异构醇和醛酮类化合物所占的总比率依次降低。该方法简单、快速,对费托合成水相产物中重要组分的分析有重要意义。
A method for the determination of low-carbon(C1-C8)alcohols,aldehydes and ketones in aqueous products of Fischer-Tropsch synthesis was developed by gas chromatogra-phy. It included the optimization of separation conditions,the precision and accuracy of deter-mination,and the use of correction factors of the analytes to ethanol for quantification. The aqueous products showed that the correlation coefficients for ethanol in different content ranges were above 0. 99,which means it had good linear correlations. The spiked recoveries in the aqueous samples of Fischer-Tropsch synthesis were from 93. 4% to 109. 6%. The accuracy of the method can satisfy the requirement for the analysis of the aqueous samples of Fischer-Tropsch synthesis. The results showed that the total mass fractions of the major low-carbon alcohols, aldehydes,ketones in aqueous products of Fischer-Tropsch synthesis were about 3%-12%,and the contents of ethanol were the highest( about 1. 7%-7. 3%). The largest sha

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费托合成反应器是间接液化的核心技术之一,该文介绍了费托合成反应器的种类、特点及其主要开发过程,对固定床、流化床和浆态床三种反应器的特点进行了分析对比。因浆态床具有生产能力大、传热效率高、可在线更新催化剂、制造成本低等优点,也是费托合成工业开发的主要发展方向。浆态床反应器开发的关键是固液、分离、反应热移取、气体分布器的研究和开发。
Fischer-Tropsch synthesis (FTS) reactor is one of the key technologies in indirect liquefaction.This paper introduces the types and characteristics of FTS reactors and its development process,The three-type reactors of fixed bed,fluidized bed and slurry bed reactor are analyzed and compared.Slurry bed reactor has great capacity of production, high heat transfer efficiency,online catalyst makeup, and low manufacturing cost,so it is also the development direction for FTS industrial development.The key research to develop slurry bed reactor is solid-liquid separation,heat transfer and gas distributor.

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费托合成通常被认为是个动力学控制的反应过程,因此对其热力学平衡的研究很少报道。本文基于 Aspen Plus 软件建立了费托合成产物物性数据库和热力学平衡分析模型,对费托合成的全局和局部热力学平衡进行了详细研究。结果表明:热力学上乙烯较其它长链烯烃更难生成,是解释实验观察乙烯偏低的重要原因;热力学平衡预测的总产物分布及烯烃、烷烃、醇的各组分分布均符合 ASF 分布规律,与实验观察的产物分布非常相似;若假定反应处于局部热力学平衡,则预测的产物分布链增长因子和烯烷比很接近实验观察值;热力学预测的反应条件对产物分布的影响也与实验结果基本一致。由此可见,热力学平衡是影响费托合成产物分布的重要因素,对反应机理研究至关重要。
Fischer-Tropsch synthesis (FTS) has been generally considered as a kinetic-controlled reaction and thus its thermodynamic equilibrium investigations were seldom reported. Based on Aspen Plus software, a physical properties database and a thermodynamic equilibrium model for FTS were established in this study. The simulated results show that ethylene formation is not favored in thermodynamics compared to other long chainα-olefins, which may be a reason to explain the lower ethylene content in experimental product distribution. The estimated product distributions of total hydrocarbons, olefins, paraffins and alcohols are similar to experimental ones and essentially follow Anderson-Schulz-Flory distribution pattern. As a local thermodynamic equilibrium is assumed for the formation of hydrocarbon product, the chain growth parameter and olefin/paraffin ratio are very close to their experimental values under same reaction conditions. Accordingly, thermodynamic equilibrium is highly important

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评述了近年来有关费-托合成中的水煤气变换反应的研究进展,着重介绍了费-托反应条件下发生的水煤气变换反应的热力学分析、反应机理和动力学.同时介绍了催化剂制备、操作参数等因素对水煤气变换反应的影响.
In this paper, the development of research on the water gas shift(WGS) reaction in the Fischer-Tropsch synthesis (FTS) was reviewed. The WGS reaction is important when synthesis gas with nonstoichiometric amounts of hydrogen is used, whereas CO efficiency is decreased accordingly. Its thermodynamic analysis, reaction mechanism and kinetics in conjunction with the FTS are presented. The WGS reaction is equilibrium or close to equilibrium reaction under Fischer-Tropsch conditions on catalysts with a high water gas shift activity such as iron-based FTS catalysts, which may operate via a mechanism with a formate species or via a direct oxidation mechanism. The kinetic studies assumed that the WGS reaction proceeds on a different catalytic site than the FTS. The effects of catalyst preparation and operation parameters on the WGS reaction activity are also summarized. The importance and prospect of research on the WGS reaction under the Fischer-Tropsch conditions are proposed.

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利用Benson基团贡献法和ABWY法计算了费托合成油品的标准摩尔生成焓、标准熵及摩尔定压热容等基础数据,在298—750 K,对费托合成油品加氢裂化异构化反应体系的反应焓、吉布斯自由能以及平衡常数等热力学数据进行了计算;对体系中各反应的热力学可能性与生成顺序进行了判断以及各反应的热力平衡与限度进行了分析。结果表明:费托合成油品加氢裂化异构化反应是放热反应,低温时大部分反应在热力学上均能够自发的进行,且平衡常数均较大,能够进行到较高的程度;从热力学上看,升高温度不利于加氢裂化异构化反应的进行,适宜反应温度的选择应兼顾各种反应的进行;烯烃比烷烃更容易发生加氢裂化异构化反应;所获得的热力学数据可为费托合成油品加氢裂化异构化工艺研究、反应器开发以及新型催化剂研制等提供理论依据。
The standard molar enthalpy of formation,the standard entropy and isobaric molar heat capacity of Fischer-Tropsch syncrude were estimated by Benson group contribution method and ABWY method.The enthalpy change,Gibbs free energy change and equilibrium constant of hydrocracking and isomerization reaction of Fischer-Tropsch syncrude were calculated as a function of the temperature from 298 K to 750 K.The thermodynamic possibility and formation sequences of hydrocracking and isomerization reaction of Fischer-Tropsch syncrude were judged.Meanwhile,the thermodynamic equilibrium and the limit of different reaction steps were also analyzed. The results show that the hydrocracking and isomerization reaction of Fischer-Tropsch syncrude is an exothermic reaction,most of which are spontaneous at low temperature and can reach to a deep extent.Improving the temperature is not good for hydrocracking and isomerization reaction from a thermodynamic point of view.The choice of the suitable temperature s

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费托合成(Fischer-Tropsch synthesis,FTS)反应是煤、甲烷和生物质等非油基碳资源转化制高品质液体燃料或化学品的重要途径。以生物质基合成气为原料,利用传统的Fe、Co催化剂制备生物燃料引起普遍关注。本文简要总结了近年来高性能Fe基和Co基费托合成催化剂的发展,以及近年来新型材料和核壳结构的双功能催化剂在费托合成中的应用。重点关注了生物质合成气方面的应用,比较了Fe、Co催化剂在该应用中的特点。虽然Co基催化剂较Fe基催化剂有更好的活性,但在BTL(Biomass-To-Liquid)过程中需要考虑多种因素,Fe基催化剂可能更具优势,开发廉价高性能的Fe基催化剂可能成为BTL-FT催化剂的发展方向。
Fischer-Tropsch synthesis (FTS) is an important route to produce various high quality hydrocarbon fuels or chemicals for different applications from synthesis gas (CO + H2), which can be derived from nonpetroleum feedstocks such as natural gas, coal, or biomass. FTS processes from biomass derived syngas using the traditionally Fe, Co catalysts have received a great deal of interest in recent years. In this perspective, the latest developments in the preparation of high performance FTS catalysts are presented, including an overview of mesoporous materials and core-shell materials for FTS. The application of high performance FTS catalysts are highlighted for hydrocarbon production from biomass, including a comparative overview of the Fe-and Co-based catalysts performance. The productivity of cobalt-based catalysts at high conversion level is currently higher than that of iron-based catalysts. Nevertheless, it is argued that iron-based catalysts may be an attractive option for the Biomass

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采用水热法在Co/Al2O3球形催化剂外表面原位包裹了一层SAPO-34分子筛膜,制备了具有核(Co/Al2O3)-壳(SAPO-34)结构的复合型催化剂.用X-射线衍射和扫描电镜对其结构进行了表征,并考察了其费-托合成直接制取低碳烯烃的反应性能.结果表明:此复合型催化剂外层的SAPO-34膜对核心Co/Al2O3球形催化剂上的费-托合成反应提供了特殊的限域环境、孔道择型选择性和酸性,显著地改变了费-托合成产物分布,抑制了重质烃的生成,极大地提高了低碳烯烃的选择性.
A well-designed zeolite capsule catalyst with a Core (Co/Al2O3)-Shell (SAPO-34) structure was prepared by zeolite shell growing via in situ hydrothermal method. XRD and SEM were used to investigate the structure of the capsule catalyst. The catalyst was used to directly synthesize light alkenes from syngas via Fischer-Tropsch synthesis ( FTS ) reaction. The cesults indicated that the core-shell structure provided a tailor-made confined reaction environment with spatially confined effect, shape selectivity of channels and acidity. Thus the distribution of products from FTS was altered, the formation of long-chain hydrocarbons was suppressed, and the selectivity of light alkenes was significantly improved.

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以γ-Al2O3为原料制备Ni-γ-Al2O3、Zn-γ-Al2O3和Al2O3载体,并采用等容浸渍法制备了钴基费-托合成用催化剂。结果表明:高温焙烧使氧化铝晶型和孔结构发生较大变化;镍添加后在载体表面形成高分散的氧化镍物种;而锌添加后与载体发生反应生成了铝酸锌;负载型催化剂中,四氧化三钴粒径大小主要取决于载体孔结构。CoPt/γ-Al2O3、CoPt/Zn-γ-Al2O3、CoPt/Ni-γ-Al2O3具有相近的费-托合成催化性能,而CoPt/Al2O3呈现出最高的催化活性和最低的甲烷选择性。表明,钴物种粒径和载体结构是影响催化剂费-托合成催化性能的主要因素。
Three materials (Ni-γ-Al2 O3 ,Zn-γ-Al2 O3 and Al2 O3 )were prepared fromγ-Al2 O3 and used as supports for cobalt-based Fischer-Tropsch catalysts.Addition of Ni toγ-Al2 O3 resulted in highly dispersed NiO,while addition of ZnO led to the formation of ZnAl2 O4 .In the supported catalysts,cobalt particle size was mostly determined by support pore structure.It was found that CoPt/γ-Al2 O3 ,CoPt/Zn-γ-Al2 O3 and CoPt/Ni-γ-Al2 O3 possessed comparable catalytic performance,while CoPt/Al2 O3 exhibited the highest catalytic activity and the lowest CH4 selectivity,which confirmed that support texture and cobalt particle size seem to be major catalyst parameters affecting the catalytic performance of the final catalysts.

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分别采用一步合成法和常规共沉淀法制备了Fe/SiO2催化剂,通过N2物理吸附、X射线衍射、透射电镜、傅里叶变换红外光谱和程序升温还原等方法对催化剂进行了表征,并在固定床反应器中对其费托合成制低碳烯烃的催化性能进行了评价。结果表明,与共沉淀铁基催化剂不同,采用一步合成法制备的纳米复合物主要由Fe3O4相构成,形貌呈规则球形,平均粒径为30 nm,尺寸分布窄,更容易还原。一步合成法制得的Fe/SiO2催化剂对费托合成反应具有较高的活性和低碳烯烃选择性、较低的甲烷选择性和良好的稳定性。
A series of Fe / SiO2 catalysts were prepared by one-pot synthesis and conventional co-precipitationmethods; they were characterized by N2 physisorption, X-ray diffraction, Fourier transform infrared spectroscopy, transmission electron microscopy, and temperature-programmed reduction. The performances ofthe Fe / SiO of light olefins from syngas. The results showed that in the Fe / SiO 2 catalysts in Fischer-Tropsch synthesis (FTS) were evaluated in a fixed-bed reactor for the production 2 catalyst prepared by one-pot synthesis method, the iron oxide is present as iron-silica nanocomposite in the form of Fe3 O4(magnetite). Compared withthe catalyst prepared by conventional co-precipitation method , the magnetite-silica nanocomposite by one-pot synthesis exhibits a more uniform spherical-like morphology, narrower size distribution (30 nm in average) andbetter reducibility. In FTS and selectivity to light olefin as well as lower selectivity to methane and better stability. , the Fe / SiO2

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详细动力学模型是费托合成(Fischer-Tropsch Synthesis,FTS)反应技术从实验室走向工业化过程中最关键的基础研究项目之一.对动力学模型的参数估算一直采用传统的无约束优化算法LM(Levenberg-Marquardt)算法,在计算中容易因参数越界而使计算失败,计算结果强烈依赖于初值,且容易限于局部最优.运用遗传算法来解决费托合成反应详细动力学模型的参数优化问题是一种全新的尝试,通过系统的实验获得了三组比较满意的参数估算结果,证明遗传算法用于解决该参数优化问题是适宜的.
Detailed kinetic model is one of the most important basic research items for Fischer-Tropsch Synthesis(FTS). LM(Levenberg-Marquardt) algorithm is used a lot in estimating parameters of the kinetic model. However, as an unlimited algorithm, LM often makes an inaccurate conclusion because of parameters exceeding the limit. Its computation greatly depends on the initial point, and easily falls into non-global optima. It is a new attempt to apply Genetic Algorithm(GA) to the solutions of optimization problems of FTS parameters. The conclusion comes that GA can be applied to such problems, which having obtained three-comparatively-satisfying-group results of parameter-estimating through a number of systemic tests.

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