帮助 关于我们

返回检索结果

合成气直接制取低碳烯烃的铁基负载型催化剂的制备与性能
Preparation and Performance of Supported Iron-based Catalysts for Conversion of Synthesis Gas to Light Olefins

查看参考文献23篇

沈兴 1   王蕾 1   张永锋 2   李增喜 3   张香平 1   张锁江 1 *  
文摘 采用浸渍法制备了合成气直接制取低碳烯烃的铁基负载型催化剂,在固定床反应器中考察了载体、助剂、焙烧温度及反应温度与压力、原料气空速对催化性能的影响,并对其进行了表征.结果表明,焙烧温度对催化剂活性有重要影响,FeK/ZSM-5催化剂经500℃焙烧3 h后具有最佳的催化活性,提高反应压力可明显提高活性,而增加原料气空速活性明显降低;添加助剂K和Mn明显提高了催化剂的低碳烯烃选择性,在H_2/CO=2(φ)、反应温度380℃、压力1.0 MPa、原料气空速4400 h~(-1)条件下,FeMnK/ZSM-5可将CO转化率从Fe/ZSM-5催化剂的18.7%升至63.8%, C_2~=~C_3~=选择性从4.8%升至14.1%.
其他语种文摘 The supported iron-based catalysts for the conversion of synthesis gas to light olefins were prepared by impregnation method and the effects of parameters, such as carrier, promoter, calcination temperature, reaction temperature, reaction pressure and space velocity, on the reaction were investigated in a fixed-bed reactor. The catalysts were characterized by XRD, N_2 physisorption, thermo gravimetric analysis and Raman spectroscopy. The results indicated that FeK/ZSM-5 catalyst prepared by calcination at 500℃ after 3 h had the best catalytic activity. Increasing reaction pressure and decreasing space velocity, the activity of catalyst was all obviously improved. Using ZSM-5 as the carrier, the comparable catalytic performance of adding K and Mn promoters were studied. The results showed that FeMnK/ZSM-5 catalyst improved the CO conversion rate from 18.7% to 63.8%, and C_2~=~C_3~= selectivity from 4.8% to 14.1% contrast to Fe/ZSM-5 catalyst under the conditions of volume ratio of H_2 to CO_2, reaction temperature 380℃, reaction pressure 1.0 MPa and space velocity 4400 h~(-1).
来源 过程工程学报 ,2009,9(6):1178-1185 【核心库】
关键词 合成气 ; 低碳烯烃 ; 铁基催化剂 ; 载体 ; 助剂
地址

1. 中国科学院过程工程研究所, 多相复杂国家重点实验室, 北京, 100190  

2. 内蒙古工业大学化工学院, 内蒙古, 呼和浩特, 010051  

3. 中国科学院研究生院, 北京, 100049

语种 中文
文献类型 研究性论文
ISSN 1009-606X
学科 化学
基金 中国科学院知识创新工程领域前沿项目 ;  中国科学院知识创新工程青年人才领域前沿项目
文献收藏号 CSCD:3763599

参考文献 共 23 共2页

1.  任诚. 非石油路线制取低碳烯烃的生产技术及产业前景. 精细化工中间体,2007,37(5):6-9 被引 11    
2.  余皎. 丙烯市场供需现状及发展趋势. 当代石油石化,2004,12(9):35-38 被引 10    
3.  Mirzaei A A. Preparation and Optimization of Mixed Iron Cobalt Oxide Catalysts for Conversion of Synthesis Gas to Light Olefins. Applied Catalysis A:General,2005,296(2):222-231 被引 12    
4.  周俊. 铁含量对合成低碳烯烃用铁锰基催化剂的影响. 天然气化工,2007,32(6):17-20 被引 3    
5.  Kang S H. Fischer-Tropsch Synthesis Using Zeolite-supported Iron Catalysts for Production of Light Hydrocarbons. Catalysis Letters,2008,125(3/4):264-270 被引 9    
6.  Okuhara T. Microporous Heteropoly Compounds and Their Shape Selective Catalysis. Applied Catalysis A:General,2003,256(1/2):213-224 被引 7    
7.  Hayakawa H. Studies on Catalytic Performance of Precipitated Iron/Silica Catalysts for Fischer-Tropsch Synthesis. Applied Catalysis A:General,2007,328(2):117-123 被引 3    
8.  Ma W P. Potassium Effects on Activated-carbon-supported Iron Catalysts for Fischer-Tropsch Synthesis. Energy and Fuels,2007,21(4):1832-1842 被引 4    
9.  Yang Y. Effect of Potassium Promoter on Precipitated Iron-Manganese Catalyst for Fisher-Tropsch Synthesis. Applied Catalysis A:General,2004,226(2):181-194 被引 67    
10.  Zhang C H. Effects of Cu and K on Co-precipitated FeMn/SiO_2 Catalysts for Fischer-Tropsch Synthesis. Acta Physico-Chimica Sinica,2006,22(11):1310-1316 被引 2    
11.  Nattaporn L. Effect of K Promotion of Fe and FeMn Fischer-Tropsch Synthesis Catalysts:Analysis at the Site Level Using SSITKA. Journal of Catalysis,2008,260(1):7-16 被引 1    
12.  Tao Z C. Effect of Manganese on a Potassium-promoted Iron-based Fischer-Tropsch Synthesis Catalyst. Catalysis Letters,2007,114(3/4):161-168 被引 8    
13.  Bai L. Slurry Phase Fischer-Tropsch Synthesis over Manganese-promoted Iron Ultrafine Particle Catalyst. FUEL,2002,81(11/12):1577-1581 被引 27    
14.  Mirzaei A A. Effect of Preparation Conditions on the Catalytic Performance of Cobalt Manganese Oxide Catalysts for Conversion of Synthesis Gas to Light Olefins. Applied Catalysis A:General,2006,306(7):98-107 被引 12    
15.  Tao Z C. Study of Manganese Promoter on a Precipitated Iron-based Catalyst for Fischer-Tropsch Synthesis. Journal of Natural Gas Chemistry,2007,16(3):278-285 被引 6    
16.  Li T Z. Effect of Manganese on an Iron-based Fischer-Tropsch Synthesis Catalyst Prepared from Ferrous Sulfate. FUEL,2007,86(7/8):921-928 被引 4    
17.  Martinez A. The Application of Zeolites and Periodic Mesoporous Silicas in the Catalytic Conversion of Synthesis Gas. Topics in Catalysis,2009,52(1/2):75-90 被引 5    
18.  Liu S T. Synthesis of Gasoline-range Hydrocarbons over Mo/HZSM-5 Catalysts. Applied Catalysis A:General,2009,357(1):18-25 被引 3    
19.  Zhao T S. Direct Synthesis of Propylene and Light Olefins from Dimethyl Ether Catalyzed by Modified H-ZSM-5. CATALYSIS COMMUNICATIONS,2006,7(9):647-650 被引 32    
20.  Tetsuya K. Synthesis of Large Silicalite-1 Single Crystals from Two Different Silica Sources. CERAMICS INTERNATIONAL,2004,30(5):727-732 被引 1    
引证文献 6

1 杨学萍 合成气直接制低碳烯烃技术进展与经济性分析 化工进展,2012,31(8):1726-1731
被引 10

2 董丽 合成气直接制低碳烯烃技术发展前景 石油化工,2012,41(10):1201-1206
被引 10

显示所有6篇文献

论文科学数据集
PlumX Metrics
相关文献

 作者相关
 关键词相关
 参考文献相关

iAuthor 链接
李增喜 0000-0003-2973-4748
版权所有 ©2008 中国科学院文献情报中心 制作维护:中国科学院文献情报中心
地址:北京中关村北四环西路33号 邮政编码:100190 联系电话:(010)82627496 E-mail:cscd@mail.las.ac.cn 京ICP备05002861号-4 | 京公网安备11010802043238号