期刊文献+
共找到7篇文章
< 1 >
每页显示 20 50 100
羰基合成高碳醇工艺进展及费托烯烃产品氢甲酰化 被引量:7
1
作者 石博文 刘素丽 +1 位作者 袁华 孙向前 《化工科技》 CAS 2020年第1期59-64,共6页
开发煤制高碳伯醇技术,对煤炭的清洁利用和国家能源安全有重要意义。煤制油项目的试车成功为羰基合成高碳醇提供了丰富的α-烯烃原料。概述羰基合成催化剂体系的工业发展历程和低压液相循环氢甲酰化工艺生产应用,介绍了费托产品为主要... 开发煤制高碳伯醇技术,对煤炭的清洁利用和国家能源安全有重要意义。煤制油项目的试车成功为羰基合成高碳醇提供了丰富的α-烯烃原料。概述羰基合成催化剂体系的工业发展历程和低压液相循环氢甲酰化工艺生产应用,介绍了费托产品为主要原料制备高碳醇国内外相关的技术发展现状。同时对开发水/有机两相体、氟两相、超临界流体等液/液两相催化体系应用费托的高碳α-烯烃氢甲酰化作了系统阐述,并对其应用前景进行了评价。对打破国外技术壁垒,自主研发高碳醇羰基合成工艺应用费托产品寄予展望。 展开更多
关键词 高碳醇 羰基合成 氢甲酰化 低压铑法 低压液相循环 费托α-
下载PDF
煤基费托α-烯烃均相氢甲酰化反应的规律
2
作者 齐慧敏 金政伟 +3 位作者 何雨航 杨自玲 金欣 海红莲 《应用化工》 CAS CSCD 北大核心 2022年第S02期13-17,共5页
研究了均相催化体系下费托α-烯烃氢甲酰化反应的规律。首先油溶性Rh-TPP催化剂被制备,^(31)P NMR证明了活性物种HRh(CO)(PPh_(3))_(3)的生成。溶剂、反应温度、合成气压力、膦铑比和反应时间等因素对氢甲酰化反应的影响被考察,反应条... 研究了均相催化体系下费托α-烯烃氢甲酰化反应的规律。首先油溶性Rh-TPP催化剂被制备,^(31)P NMR证明了活性物种HRh(CO)(PPh_(3))_(3)的生成。溶剂、反应温度、合成气压力、膦铑比和反应时间等因素对氢甲酰化反应的影响被考察,反应条件被优化。在循环过程中,铑催化剂表现出较好的稳定性,总TON值达到85529,催化剂失活的机理被探讨。该均相催化体系被扩展至不同碳链的费托α-烯烃和混合费托α-烯烃,具有较好的普适性。 展开更多
关键词 费托烯烃 氢甲酰化 三苯基膦
下载PDF
调控Co_(2)C局域浸润环境实现高碳效合成气直接制烯烃 被引量:1
3
作者 刘培功 林铁军 +5 位作者 郭磊 刘晓哲 龚坤 尧泰真 安芸蕾 钟良枢 《Chinese Journal of Catalysis》 SCIE EI CAS CSCD 2023年第5期150-163,共14页
合成气转化是实现煤、天然气、生物质、固体废弃物及CO_(2)等非石油含碳资源清洁高效利用的关键过程,可合成多种清洁液体燃料和高附加值化学品,如汽油、柴油、航空煤油、固体石蜡、烯烃、芳烃和含氧化合物等.其中,合成气直接制烯烃(STO... 合成气转化是实现煤、天然气、生物质、固体废弃物及CO_(2)等非石油含碳资源清洁高效利用的关键过程,可合成多种清洁液体燃料和高附加值化学品,如汽油、柴油、航空煤油、固体石蜡、烯烃、芳烃和含氧化合物等.其中,合成气直接制烯烃(STO)具有流程短、能耗低和经济性高等优点,备受学术界和工业界关注.近年来,合成气直接制烯烃取得了突破性进展,发展了基于氧化物-分子筛的双功能路线法以及改性费托路线法.然而,由于目前STO体系所使用的氧化物或者碳化物活性相同时也是水煤气变换(WGS)活性位点,导致反应过程产生30%-50%的CO_(2)副产物,造成较低的碳原子利用效率和烯烃收率,以及尾气产品分离能耗的增加.如何通过催化剂界面和局域环境的调控,创新反应路径,提高烯烃选择性和收率,降低C1副产物选择性已成为重大挑战.本文提出通过发展界面浸润性调控策略,将CoMnAl复合氧化物(CMA)衍生的CO_(2)C活性相与疏水SiO_(2)进行一定尺度的物理耦合,能够将CO_(2)选择性从47.8%降到16.8%,同时催化剂的活性提高30%,总产物中烯烃选择性也提高了~65%,体现出较高的碳效.FI-IR光谱和接触角测试结果表明,疏水基团成功引入到SiO_(2)载体上,并且通过粉末混合的方式获得了同样具备疏水特性的CoMnAl复合催化剂(CMASc).热重(TG-DTG)结果表明,即使样品经过300℃的高温处理,其疏水性仍然能得到保持.X射线衍射(XRD)和高分辨率透射电镜(HRTEM)表征结果表明,复合氧化物的活性中心仍是棱柱状Co_(2)C.进一步表征和探针实验解释了催化剂浸润性调变对Co_(2)C基催化剂FTO性能的影响.CO/H_(2)O-TPSR-MS实验表明,往体系中引入H_(2)O蒸气,CMASc催化剂产生的CO_(2)信号强度远低于单独CMA催化剂的.CO/H_(2)-TPSR-MS实验结果表明,在相同的温度下,CMASc催化剂上产生的H_(2)O信号强度高于CMA,而相应的CO_(2)信号强度则要低很多.在250-400℃,将产生的CO_(2)信号峰面积进行积分,发现CMA产生的CO_(2)浓度是CMASc的2.3倍.利用固定床开展CO/H_(2)和CO/H_(2)O探针切换实验,结果表明,在典型FTO反应条件下引入水蒸气到CMA催化剂体系后,CO转化率和尾气H_(2)/CO比大幅度提高,而CMASc上则出现相反趋势.这些实验证实了H_(2)O分子容易吸附在CMA上发生WGS反应,而在Co_(2)C活性位界面构建局域疏水环境有利于水分子快速转移,并防止其再次吸附.利用CO-DRIFTS和烯烃-H_(2)脉冲实验研究活性和烯烃选择性提高的原因.相比于CMA,CO更容易吸附在疏水CMASc上.H_(2)O的引入会导致CO在两个催化剂的强度变弱,但CMASc上吸附的CO强度仍要高于CMA.这说明活性位点存在水会阻碍CO的吸附,而CMASc上相对干燥的表面更有利于CO吸附及后续活化.调控H_(2)O分压探针实验也在宏观层面上验证了该结论,说明活性中心吸附的H_(2)O会抑制催化活性.丙烯加氢脉冲实验发现,浸润环境可以极大地影响烯烃的吸附和加氢能力.在H_(2)O存在的情况下,丙烯更容易在CMA上发生加氢生成丙烷,而疏水CMASc上丙烯更容易直接脱落,从而提高了烯烃选择性.综上,通过调控Co_(2)C活性位局域疏水环境,可以降低表面H_(2)O的吸附,抑制CO_(2)副产物生成,同时强化CO吸附和烯烃脱附,提高烯烃选择性和收率,这为高碳效Co_(2)C基催化剂的理性设计提供借鉴. 展开更多
关键词 费托合成制 合成气转化 碳化钴 疏水性 低CO_(2)选择性
下载PDF
费托合成制低碳烯烃中碱金属对CoMn催化剂催化性能的影响 被引量:2
4
作者 杨若欧 孙凡飞 +2 位作者 赵子昂 赵景泰 姜政 《核技术》 CAS CSCD 北大核心 2018年第10期8-13,共6页
碳化钴(Co2C)在费托合成制低碳烯烃(Fischer-Tropsch to Olefin, FTO)中起着重要的催化作用。通过X射线衍射(X-ray Diffraction, XRD)、X射线吸收精细结构(X-ray Absorption Fine Structure, XAFS)等表征与方法,对碱金属在CoMn催化FTO... 碳化钴(Co2C)在费托合成制低碳烯烃(Fischer-Tropsch to Olefin, FTO)中起着重要的催化作用。通过X射线衍射(X-ray Diffraction, XRD)、X射线吸收精细结构(X-ray Absorption Fine Structure, XAFS)等表征与方法,对碱金属在CoMn催化FTO中形成碳化钴的影响进行了研究。在钠(Na)、钾(K)元素的影响下,CoMn催化剂在活性评测中,低碳非饱和烃与低碳饱和烃的比例高达17.4与9.4,且仅有较低的甲烷(CH4)产生,而锂(Li)对CoMn催化剂的选择性影响较弱。通过XRD表征,发现Na、K对CoMn催化剂形成Co2C有很好的促进效果。XAFS揭示了CoMn催化剂的电子结构,催化反应后形成碳化钴的配位结构,为研究CoMn催化剂微观结构提供了基础理论。 展开更多
关键词 费托合成制低碳 碳化钴 碱金属 X射线吸收精细结构谱
下载PDF
Effects of zinc on Fe-based catalysts during the synthesis of light olefins from the Fischer-Tropsch process 被引量:10
5
作者 高新华 张建利 +4 位作者 陈宁 马清祥 范素兵 赵天生 椿范立 《Chinese Journal of Catalysis》 SCIE EI CAS CSCD 北大核心 2016年第4期510-516,共7页
Fe‐based catalysts for the production of light olefins via the Fischer‐Tropsch synthesis were modi‐fied by adding a Zn promoter using both microwave‐hydrothermal and impregnation methods. The physicochemical prope... Fe‐based catalysts for the production of light olefins via the Fischer‐Tropsch synthesis were modi‐fied by adding a Zn promoter using both microwave‐hydrothermal and impregnation methods. The physicochemical properties of the resulting catalysts were determined by scanning electron mi‐croscopy, the Brunauer‐Emmett‐Teller method, X‐ray diffraction, H2 temperature‐programed re‐duction and X‐ray photoelectron spectroscopy. The results demonstrate that the addition of a Zn promoter improves both the light olefin selectivity over the catalyst and the catalyst stability. The catalysts prepared via the impregnation method, which contain greater quantities of surface ZnO, exhibit severe carbon deposition following activity trials. In contrast, those materials synthesized using the microwave‐hydrothermal approach show improved dispersion of Zn and Fe phases and decreased carbon deposition, and so exhibit better CO conversion and stability. 展开更多
关键词 Zn promoter Fe-based catalyst Light olefin Fischer-Tropsch synthesis Microwave-hydrothermal method
下载PDF
Effect of the support on cobalt carbide catalysts for sustainable production of olefins from syngas 被引量:4
6
作者 Xinxing Wang Wen Chen +7 位作者 Tiejun Lin Jie Li Fei Yu Yunlei An Yuanyuan Dai Hui Wang Liangshu Zhong Yuhan Sun 《Chinese Journal of Catalysis》 SCIE EI CAS CSCD 北大核心 2018年第12期1869-1880,共12页
Co2C‐based catalysts with SiO2,γ‐Al2O3,and carbon nanotubes(CNTs)as support materials were prepared and evaluated for the Fischer‐Tropsch to olefin(FTO)reaction.The combination of catalytic performance and structu... Co2C‐based catalysts with SiO2,γ‐Al2O3,and carbon nanotubes(CNTs)as support materials were prepared and evaluated for the Fischer‐Tropsch to olefin(FTO)reaction.The combination of catalytic performance and structure characterization indicates that the cobalt‐support interaction has a great influence on the Co2C morphology and catalytic performance.The CNT support facilitates the formation of a CoMn composite oxide during calcination,and Co2C nanoprisms were observed in the spent catalysts,resulting in a product distribution that greatly deviates from the classical Anderson‐Schulz‐Flory(ASF)distribution,where only 2.4 C%methane was generated.The Co3O4 phase for SiO2‐andγ‐Al2O3‐supported catalysts was observed in the calcined sample.After reduction,CoO,MnO,and low‐valence CoMn composite oxide were generated in theγ‐Al2O3‐supported sample,and both Co2C nanospheres and nanoprisms were identified in the corresponding spent catalyst.However,only separated phases of CoO and MnO were found in the reduced sample supported by SiO2,and Co2C nanospheres were detected in the spent catalyst without the evidence of any Co2C nanoprisms.The Co2C nanospheres led to a relatively high methane selectivity of 5.8 C%and 12.0 C%of theγ‐Al2O3‐and SiO2‐supported catalysts,respectively.These results suggest that a relatively weak cobalt‐support interaction is necessary for the formation of the CoMn composite oxide during calcination,which benefits the formation of Co2C nanoprisms with promising catalytic performance for the sustainable production of olefins via syngas. 展开更多
关键词 Fischer‐Tropsch to olefins Cobalt carbide Supported catalyst OLEFIN SYNGAS
下载PDF
Full life cycle characterization strategies for spatiotemporal evolution of heterogeneous catalysts 被引量:1
7
作者 Renyang Zheng Zaiku Xie 《Chinese Journal of Catalysis》 SCIE EI CAS CSCD 2021年第12期2141-2148,共8页
The sustainable development of the chemical industry requires novel and efficient catalysts and catalytic processes,especially eco-friendly and intrinsically safe processes.The idea is to improve the selectivity,activ... The sustainable development of the chemical industry requires novel and efficient catalysts and catalytic processes,especially eco-friendly and intrinsically safe processes.The idea is to improve the selectivity,activity,and stability of the catalyst in an appropriate reactor.Therefore,it is of great academic and industrial significance to conduct in-situ characterization of a working catalyst while testing its catalytic performance.This is beneficial for a comprehensive study on the dynamic evolution of the catalyst structure under real conditions,deepening the understanding of the structure-performance relationship of catalysts,and providing a scientific basis for the development of future generation catalytic technology.Thus far,it is still a great challenge to realize full life cycle characterization of heterogeneous catalysts from catalyst formation and function to deactivation under real world conditions.In this mini review,we summarize the characterization strategies for heterogeneous catalysts,using zeolite,metal,and metal oxide catalysts as typical examples.The research strategies for the approximation of industrial conditions,multi-scale in-situ characterization devices,and computational modeling of realistic conditions should provide insight for the research and development of industrial catalysis. 展开更多
关键词 Heterogeneous catalysis In-situ characterization Methanol-to-olefins Fischer-Tropsch synthesis Propane dehydrogenation
下载PDF
上一页 1 下一页 到第
使用帮助 返回顶部