共查询到19条相似文献,搜索用时 125 毫秒
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介绍了几种丙烷脱氢制丙烯技术:催化脱氢、氧化脱氢、膜反应器脱氢。综述了丙烷催化脱氢制丙烯催化剂的研究现状,虽然丙烷催化脱氢生产丙烯虽已实现了工业化,但其催化剂的性能需进一步提高;综述了丙烷氧化脱氢制丙烯反应催化剂的研究现状及膜反应器在丙烷脱氢反应上所具有的优越性,认为研发具有高稳定性和高透氢性能的氢分离膜,将有望能大幅度提高丙烯的收率。 相似文献
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介绍了催化脱氢、氧化脱氢、膜反应器脱氢等几种丙烷脱氢制丙烯技术,综述了丙烷催化脱氢制丙烯催化剂的研究现状,虽然丙烷催化脱氢生产丙烯已实现了工业化,但其催化剂的性能需进一步提高;对丙烷氧化脱氢制丙烯反应催化剂的研究现状及膜反应器在丙烷脱氢反应上所具有的优越性进行了描述,认为研发具有高稳定性和高透氢性能的氢分离膜,将有望能大幅度提高丙烯的收率。 相似文献
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杨瑞云 《中国石油和化工标准与质量》2023,(6):164-166
丙烯是一种重要的有机化工原料和石油化工原料中间体。由于能源结构的改变,近年来在国内外市场的需求量持续增长。丙烷直接脱氢制丙烯技术具有收率高、技术成熟、经济环保等优势,成为当前丙烯生产工艺研究的焦点。本文列举了几种常用的丙烷直接脱氢制丙烯的工艺,对技术方法进行了对比,并对催化剂进行了简述。在此基础上,对丙烷催化脱氢新技术以及催化剂发展前景进行了展望。 相似文献
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丙烷脱氢是一个可逆强吸热反应,这制约了现有丙烷脱氢工艺过程的效率.本工作提出采用膜反应器耦合丙烷脱氢和氢燃烧过程,一方面产物氢气的移除可使丙烷脱氢反应正向移动,另一方面氢气燃烧放出大量的热可用于驱动丙烷脱氢反应.为此建立了二维非等温膜反应器数学模型,对膜反应器中丙烷脱氢和氢燃烧耦合过程进行了模拟,比较了膜反应器与普通固... 相似文献
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介绍了丙烷脱氢制丙烯工艺的开发情况,根据反应器类型的不同,丙烷脱氢制丙烯工艺可以分为固定床工艺、移动床工艺和流化床工艺,其中固定床工艺中的Catofin工艺和移动床工艺中的Oleflex工艺得到了广泛应用。随着装置规模化、大型化的不断推进,流化床工艺受到了各大机构的青睐,FBD-3、FCDh、K-PROTM和ADHO等工艺相继涌现,为增产丙烯提供了可靠的支撑。未来可以通过采用绿色环保的非贵金属催化剂和新型反应器,克服现有丙烷脱氢工艺存在的问题,降低丙烯生产成本和碳排放,提高装置运行稳定性。 相似文献
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卜婷婷杨利斌孔维杰周金波 《工业催化》2021,29(9):21-28
丙烯作为仅次于乙烯的重要化工原料,需求量非常大,丙烷氧化脱氢反应可克服热力学平衡限制,延长催化剂使用寿命,备受关注.综述了丙烷氧化脱氢制丙烯催化剂的研究进展情况,重点介绍了不同金属组分掺杂/负载的多孔材料催化剂对丙烷氧化脱氢制丙烯反应的催化性能,并对催化剂的发展方向进行了展望.指出开发性能更加优异的催化剂,从催化剂的微... 相似文献
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Kaihu Hou Ronald Hughes 《Journal of chemical technology and biotechnology (Oxford, Oxfordshire : 1986)》2003,78(1):35-41
Propane dehydrogenation has been simulated for a composite membrane reactor and a microporous membrane reactor using plug‐flow reactor models, in which both were packed with Pt/Al2O3 catalyst in the tube‐side. The reaction kinetics employed in the analysis were obtained from experimental data produced in an integral fixed bed reactor with the same catalyst. Comparative studies were carried out to analyse the performances of reactors containing the different membranes in terms of contact time, flow pattern and flow rate of sweep gas, and pressure. In general, the composite membrane reactors gave the better performance for all cases investigated. © 2002 Society of Chemical Industry 相似文献
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Material properties and operating configurations of membrane reactors for propane dehydrogenation 下载免费PDF全文
Seung‐Won Choi Christopher W. Jones Sankar Nair David S. Sholl Jason S. Moore Yujun Liu Ravindra S. Dixit John G. Pendergast 《American Institute of Chemical Engineers》2015,61(3):922-935
A modeling‐based approach is presented to understand physically realistic and technologically interesting material properties and operating configurations of packed‐bed membrane reactors (PBMRs) for propane dehydrogenation (PDH). PBMRs composed of microporous or mesoporous membranes combined with a PDH catalyst are considered. The influence of reaction and membrane transport parameters, as well as operating parameters such as sweep flow and catalyst placement, are investigated to determine desired “operating windows” for isothermal and nonisothermal operation. Higher Damköhler (Da) and lower Péclet (Pe) numbers are generally helpful, but are much more beneficial with highly H2‐selective membranes rather than higher‐flux, lower‐selectivity membranes. H2‐selective membranes show a plateau region of conversion that can be overcome by a large sweep flow or countercurrent operation. The latter shows a complex trade‐off between kinetics and permeation, and is effective only in a limited window. H2‐selective PBMRs will greatly benefit from the fabrication of thin (~1 µm or less) membranes. © 2014 American Institute of Chemical Engineers AIChE J, 61: 922–935, 2015 相似文献
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Modeling and process simulation of hollow fiber membrane reactor systems for propane dehydrogenation 下载免费PDF全文
Seung‐Won Choi David S. Sholl Sankar Nair Jason S. Moore Yujun Liu Ravindra S. Dixit John G. Pendergast 《American Institute of Chemical Engineers》2017,63(10):4519-4531
We report a detailed modeling analysis of membrane reactor systems for propane dehydrogenation (PDH), by integrating a two‐dimensional (2‐D) nonisothermal model of a packed bed membrane reactor (PBMR) with ASPEN process simulations for the overall PDH plant including downstream separations processes. PBMRs based on ceramic hollow fiber membranes—with catalyst placement on the shell side—are found to be a viable route, whereas conventional tubular membranes are prohibitively expensive. The overall impact of the PBMR on the PDH plant (e.g., required dimensions, catalyst amount, overall energy use in reaction and downstream separation) is determined. Large savings in overall energy use and catalyst amounts can be achieved with an appropriate configuration of PBMR stages and optimal sweep/feed ratio. Overall, this work determines a viable design of a membrane reactor‐based PDH plant and shows the potential for miniaturized hollow‐fiber membrane reactors to achieve substantial savings. © 2017 American Institute of Chemical Engineers AIChE J, 63: 4519–4531, 2017 相似文献
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Zhentao Wu Irfan M.D. Hatim Benjamin F.K. Kingsbury Ejiro Gbenedio K. Li 《American Institute of Chemical Engineers》2009,55(9):2389-2398
A novel inorganic hollow fiber membrane reactor (iHFMR) has been developed and applied to the catalytic dehydrogenation of propane to propene. Alumina hollow fiber substrates, prepared by a phase inversion/sintering method, possess a unique asymmetric structure that can be characterized by a very porous inner surface from which finger-like voids extend across ∼80% of the fiber cross-section with the remaining 20% consisting of a denser sponge-like outer layer. In contrast to other existing Pd/Ag composite membranes, where an intermediate γ-Al2O3 layer is often used to bridge the Pd/Ag layer and the substrate, the Pd/Ag composite membrane prepared in this study was achieved by coating the Pd/Ag layer directly onto the outer surface of the asymmetric substrate. After depositing submicron-sized Pt (0.5 wt %)/γ-alumina catalysts in the finger-like voids of the substrates, a highly compact multifunctional iHFMR was developed. Propane conversion as high as 42% was achieved at the initial stage of the reaction at 723 K. In addition, the space-time yields of the iHFMR were ∼60 times higher than that of a fixed bed reactor, demonstrating advantages of using iHFMR for dehydrogenation reactions. © 2009 American Institute of Chemical Engineers AIChE J, 2009 相似文献
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Oliver Czuprat Steffen Werth Jürgen Caro Thomas Schiestel 《American Institute of Chemical Engineers》2010,56(9):2390-2396
A membrane reactor incorporating a hollow fiber with successive parts of oxygen permeable and passivated surface segments has been developed and was used for the oxidative dehydrogenation (DH) of propane. This membrane geometry allows a controlled oxygen feeding into the reactor over its axial length. In the oxidative DH, the thermodynamic limitation of propane DH can be overcome. By using this novel hollow fiber membrane reactor with a Pt/Sn/K DH catalyst, oxygen separation and propene formation could be established even at temperatures as low as 625°C with long‐term stability. Combining the hollow fiber membrane and the DH catalyst, the highest propene selectivity of 75% was observed at a propane conversion of 26% and 625°C whereas the best propene yield of 36% was obtained at 675°C (48% propene selectivity). The performance of this reactor is evaluated by applying various reaction conditions. © 2010 American Institute of Chemical Engineers AIChE J, 2010 相似文献
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为确立丙烷脱氢制丙烯工艺中低温分离单元的最佳制冷流程,采用PRO/Ⅱ8.2化工流程模拟软件,对低温分离单元进行模拟计算,考察了温度和压力对低温分离效果的影响,分析并确立了最佳分离温度和压力范围;在分离效果相同的前提下,分别比较了丙烯+乙烯级联制冷、丙烯预冷+混合制冷和丙烯预冷+富氢气膨胀制冷3种制冷流程的公用工程消耗以及各自的优缺点。结果表明:产品压缩机出口压力对分离效果影响较小,在确保下游装置能够正常操作的情况下,分离压力应尽可能低;分离温度是影响分离效果的主要因素,较为经济的分离温度为-90—-100℃;相对于其他2种流程,丙烯+乙烯级联制冷流程具有技术成熟、能耗低和操作简单等优点,更适合于丙烷脱氢制丙烯工艺。 相似文献