Effect of Different Chelating Agents on the Physicochemical Properties of Cu/ZnO Catalysts for Low-temperature Methanol Synthesis from Syngas Containing CO 2

IF 0.6 4区 工程技术 Q4 ENERGY & FUELS
Fei Chen, W. Gao, Baizhang Zhang, Heng Zhao, Liwei Xiao, Y. Araki, Xiao Yong, Wei Zhang, Tiejian Zhao, Zhongshan Guo, Yingluo He, Peipei Zhang, N. Tsubaki
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引用次数: 2

Abstract

Methanol is the simplest primary alcohol manufactured worldwide in large quantities with an annual production of 40-60 million tons1). Methanol is a clean liquid fuel which can be used for fuel cells2). Methanol is extensively used for the production of dimethoxymethane (DMM), formic acid, dimethyl ether (DME), and other industrial chemicals3),4). More importantly, methanol is an intermediate for the synthesis of aromatics from syngas (CO+H2) or mixtures of carbon dioxide and hydrogen (CO2 +H2). These many applications emphasize the desirability of the development of highly active catalysts for methanol synthesis. The conventional high-temperature methanol synthesis process was developed by Imperial Chemical Industries Limited (ICI)2). However, the process achieves one-pass CO conversion of only 20-30 % because methanol synthesis is an exothermic reaction2). Therefore, recycling of unreacted feed gas is essential to increase conversion, leading to increased production costs. Consequently, methanol synthesis processes operating at low temperatures are very desirable. We previously proposed a novel reaction path of low-temperature methanol synthesis over Cu/ZnO catalyst using various alcohols as both promoters and solvents, which produced methanol at low temperatures (130-170 °C) in a slurry-phase reactor7),8). This new process can use syngas containing both CO2/H2O directly without further purification, since CO2 and H2O in the feed gas are both byproducts and reactants, so are recycled in-situ in [Regular Paper]
不同螯合剂对含co2合成气低温甲醇Cu/ZnO催化剂理化性能的影响
甲醇是世界上大量生产的最简单的原醇,年产量为4000万至6000万吨。甲醇是一种清洁的液体燃料,可用于燃料电池。甲醇广泛用于生产二甲氧基甲烷(DMM)、甲酸、二甲醚(DME)和其他工业化学品。更重要的是,甲醇是合成气(CO+H2)或二氧化碳和氢的混合物(CO2 +H2)合成芳烃的中间体。这些应用强调了开发高活性甲醇合成催化剂的必要性。传统的高温甲醇合成工艺是由帝国化学工业有限公司(ICI)开发的。然而,由于甲醇合成是一种放热反应,该工艺的一次CO转化率仅为20- 30%。因此,回收未反应的原料气对于提高转化率至关重要,从而导致生产成本增加。因此,在低温下操作的甲醇合成工艺是非常可取的。我们之前提出了一种新的Cu/ZnO催化剂上的低温甲醇合成反应途径,使用各种醇作为促进剂和溶剂,在浆相反应器中低温(130-170°C)下合成甲醇7),8)。这种新工艺可以直接使用含有CO2/H2O的合成气,而无需进一步净化,因为原料气中的CO2和H2O都是副产品和反应物,因此可以在【常规纸张】中就地回收。
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来源期刊
Journal of The Japan Petroleum Institute
Journal of The Japan Petroleum Institute 工程技术-工程:石油
CiteScore
1.70
自引率
10.00%
发文量
29
审稿时长
>12 weeks
期刊介绍: “Journal of the Japan Petroleum Institute”publishes articles on petroleum exploration, petroleum refining, petrochemicals and relevant subjects (such as natural gas, coal and so on). Papers published in this journal are also put out as the electronic journal editions on the web. Topics may range from fundamentals to applications. The latter may deal with a variety of subjects, such as: case studies in the development of oil fields, design and operational data of industrial processes, performances of commercial products and others
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