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高温煤气中氨的脱除——Ⅱ-氨催化分解动力学的研究 被引量:1

AMMONIA REMOVALIN HOTCOAL GAS——Ⅱ- KINETICSTUDYONAMMONIACATALYTIC DECOMPOSITION
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摘要 研究了Ni- 3催化剂分解氨的动力学。考察了各种反应条件如温度、空速以及气体中的氨和氢的浓度对反应的影响,确立了氨催化分解动力学方程式。当操作空速为3000h- 1 时,在580 ~630℃的温度区间内,反应主要受化学反应控制;在630~700℃的温度区间内,反应受扩散影响较为严重;在700℃以上的温度区间内,反应在一定程度上受平衡的影响。随着空速的增大反应速率增大,但转化率却有所减小;气体中氨浓度的增大对反应转化率没有什么影响,氢浓度的增大使反应转化率明显减小。在580~630℃的温度范围内,空速3000h- 1 的操作条件下动力学方程式如下:R= 3.423×1013e- 276 .45 ×103RT CNH3·C- In this article the results of further research work about Ni - 3 catalyst screened for ammonia catalytic decomposition are reported- The effects of various reaction conditions such asreaction temperature,space velocity and the concentration ofreactants on reaction have been studied- The conversion ofammonia decomposition increases with increas ing reactiontemperaturein a certaintemperaturerange- Underthespace velocity of3000h -1 , when the reaction temperature is from 580 ℃to 630 ℃,the reaction rate is controlled by chemicalreaction , While it is affected by diffusion in temperature ranging from 630 ℃to 700℃- Above 700 ℃the reaction is influenced by reaction equilibrium to a certain extent- Withincreasing space velocity,reaction rate increases while the conversion decreases- The concentration ofammoniain gas has no effecton conversion ,whileincreasing concentration of hydrogen will markedly decrease the conversion- In temperature range of 580 ~630 ℃and 3000h -1 ofspace velocity,thefollowing kinetic equation is obtained : R= 3.423×1013e- 276 .45 ×103 RT CNH3·C- 1-5H2
出处 《燃料化学学报》 EI CAS CSCD 北大核心 1999年第5期462-466,共5页 Journal of Fuel Chemistry and Technology
基金 国家自然科学基金
关键词 NI基催化剂 分解 转化率 高温 煤气 催化 脱氨 Ni- based catalyst,kinetic equation of NH3 decomposition ,comversion of ammonia decomposition
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参考文献5

  • 1陈敏恒 谢声礼.化学反应工程基本原理[M].上海:华东化工学院出版社,1991.. 被引量:2
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  • 5申文琴,高温煤气中的氨的脱除 (Ⅰ) 氨催化分解催化剂的筛选 被引量:1

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