Development of Low-temperature-liquid-phase-methanol-synthesis
Development of Low-temperature-liquid-phase-methanol-synthesis
批准号:
11450305
负责人:
AIKA Ken-ichi
金额:
$9.41万
依托单位国家:
日本
项目类别:
Grant-in-Aid for Scientific Research (B).
财政年份:
1999
资助国家:
日本
项目状态:
已结题
起止时间:
1999 至 2000
中文摘要
由于低温燃烧,甲醇被期望用作不产生任何NOx的燃料。甲醇还可作为燃料电池能源的氢源和化工中间体。有望开发出经济的生产方法。低温甲醇合成是一项有待开发的新技术。提出了两步反应机理:CH_3OH +CO→HCOOCH_3(醇盐催化剂)(1)HCOOCH_3+2H_2→2CH_3OH(镍催化剂)(2)反应机理及催化剂的作用。众所周知,第一步是用Na醇盐催化剂的容易反应。我们使用Co、Fe、Cu、Pd和Ni进一步研究了第二步。其中Ni的效果最好,A和Fe的效果较好.在Co金属上发生另一反应,甲烷化。醇钠的存在导致第二步反应生成甲醇,否则发生分解(HCOOCH_3→CH_3OH+CO)。迄今为止,只有活化H_2的金属表面被认为是第二反应的催化剂。然而,在这项研究中,钠醇盐和金属(特别是镍)的组合被发现是一个重要因素的选择性形成甲醇。Ni颗粒尺寸发生变化。变更甲醇钠的量。变更甲醇钠的量。最后,甲醇钠的比例和表面原子量的镍被发现是重要的。甲醇可导致形成一些中间体(可能是HCHO),其可进一步氢化得到甲醇。镍和甲醇钠的最佳组合可获得99%的产率和98%的甲醇选择性。这些结果表明,该催化剂体系是一种有前途的第二代甲醇合成催化剂体系。
英文摘要
Methanol is expected to be used as a fuel which does not yield any NOx because of low temperature combustion. Methanol also be used as a hydrogen source of fuel cell energy and as an intermediate of chemical industry. Economical production method is expected to be developed. Low temperature methanol synthesis as a new technology to be developed. The two step mechanism has been proposed.CH_3OH+CO→HCOOCH_3 (alkoxide catalyst) (1)HCOOCH_3+2H_2→2CH_3OH (nickel catalyst) (2)The mechanism and the role of catalyst was studied. The first step is well known to be an easy reaction with Na alkoxide catalyst. We studied further the second step using Co, Fe, Cu, Pd, and Ni. Ni was the best and a and Fe showed a good function. On Co metal the other reaction, methanation occurred. Co existence of Na alkoxide leaded the second reaction to methanol synthesis, otherwise the decomposition occurred (HCOOCH_3→CH_3OH+CO). So far only metal surface which activate H_2 is acknowledged as a role of catalyst for the second reaction. However, in this study, the combination of Na alkoxide and metal (especially Ni) was found to be an important factor for the selective formation of methanol. Ni particle size was changed. Amount of Na methoxide was changed. Amount of Na methoxide was changed. Finally the ratio of Na methoxide and the surface atom amount of Ni was found to be important. Methoxide may lead the formation of some intermediate (possibly HCHO), which further may be hydrogenated to give methanol. The best combination of Ni and Na methoxide gave 99% yield and 98% methanol selectivity. These results suggested that this catalyst system be a promising system of second generation methanol synthesis.
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Yasuo Izumi,Takehiro Shimizu,Takaaki Kobayashi and Ken-ich Aika: "Nitrous Oxide Dicomposition Active Site on Ni-MgO Catalysts Characterized by X-ray Absorption Fine Structure Spectroscopy"Chem.Commun.. 1053-1054 (2000)
Yasuo Izumi、Takehiro Shimizu、Takaaki Kobayashi 和 Ken-ich Aika:“通过 X 射线吸收精细结构光谱表征 Ni-MgO 催化剂上的一氧化二氮分解活性位点”Chem.Commun. 1053-1054 (2000)
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通讯作者:
Ken-ichi AIKA and Yusuke NIWA: "Basic Concepts and Properties of New Generation Ammonia Synthesis Catalysts for Industrial Use"Science and Technology in Catalysis 1998. 327-332 (1999)
Ken-ichi AIKA 和 Yusuke NIWA:“工业用新一代氨合成催化剂的基本概念和性能”催化科学与技术 1998. 327-332 (1999)
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Ryoichi Kojima,Ken-ich Aika: "Cobalt Rhenium Binary Catalyst for Ammonia Synthesis"Chemistry Letters. 912-913 (2000)
Ryoichi Kojima、Ken-ich Aika:“用于氨合成的钴铼二元催化剂”化学快报。
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Katsutoshi Nagaoka,Kulathuiyer Seshan,Johannes A.Lercher and Ken-ichi Aika: "Activation Mechanism of Methane-Derived-Coke (CHx) by CO_2 during Dry Reforming of Methane - Comparison for Pt/Al_2O_3 and Pt/ZrO_2"Catal.Lett.. 70. 109 (2000)
Katsutoshi Nagaoka,Kulathuiyer Seshan,Johannes A.Lercher和Ken-ichi Aika:“甲烷干重整过程中CO_2对甲烷衍生焦(CHx)的活化机制 - Pt/Al_2O_3和Pt/ZrO_2的比较”Catal.Lett。
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Katsudoshi Nagaoka, Takashi Karasuda, and Ken-ichi Aika: "The Effect of SnO2 Addition to Li/MgO Catalysts for for the Oxidative Coupling of Methane"J. Catal.. 181. 160-164 (1999)
Katsudoshi Nagaoka、Takashi Karasuda 和 Ken-ichi Aika:“Li/MgO 催化剂中添加 SnO2 对甲烷氧化偶联的影响”J。
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共 16 条
Research and development of nano-sized metal catalysts whose metal crystal surface are controlled
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批准号:14205115
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项目类别:Grant-in-Aid for Scientific Research (A)
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资助金额:$34.61万
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财政年份:2002
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负责人:AIKA Ken-ichi
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依托单位:
Development of New Generation Ammonia Synthesis Catalyst Process
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批准号:10355032
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项目类别:Grant-in-Aid for Scientific Research (A)
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资助金额:$17.41万
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财政年份:1998
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负责人:AIKA Ken-ichi
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依托单位:
海外基金