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柴油机冷启动HC在LTA沸石中吸附的分子模拟 被引量:2

Molecular simulation of diesel cold start emissions adsorption in LTA zeolite
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摘要 为了对柴油机冷启动过程产生的碳氢化合物(HC)进行吸附处理,需要对冷启动过程中的HC吸附过程进行研究。以乙烯(C2H4)和丙烯(C3H6)为探针分子,利用巨正则蒙特卡罗法(GCMC)对LTA型分子筛的HC吸附性能进行分子模拟研究,获得特定温度下的纯组分和混合组分吸附等温线以及吸附粒子云分布。研究结果表明:在柴油机冷启动条件下,C3H6和C2H4在LTA型分子筛上的吸附量显示出类似的趋势,均随着压力的升高而增加,随着温度的升高而减少;当二者同时存在时会发生了竞争行为,C2H4受到的影响比C3H6要大,LTA型分子筛对C3H6的吸附效果要好于对C2H4的吸附效果;C3H6在LTA型分子筛的α笼和β笼中均有分布,而C2H4在LTA型分子筛中的分布主要集中在分子筛的α笼中,只有少量分布在分子筛的β笼中。 The adsorption behaviors of diesel cold starting emissions in LTA zeolite was studied by grand canonical Monte Carlo (GCMC) simulation. Ethylene and propylene were used as probe molecules for HC. Adsorption isotherms under special temperatures for pure component, binary mixtures and mass cloud of the adsorbates were obtained. The results show that the average loading of ethylene and propylene has the similar trend, and both of them increase with the increase of pressure and decrease significantly with the increase of temperature. The binary mixtures show competitive adsorption behavior, and the adsorption effect of propylene in LTA zeolite is better than adsorption effect of ethylene in LTA zeolite. From the mass clouds of the simulation, it can be found that propylene distributes in the α cage and β cage of the LTA zeolite. But ethylene distributes mainly in the a cage, and only a few distribute mainly in the β cage of the LTA zeolite.
出处 《中南大学学报(自然科学版)》 EI CAS CSCD 北大核心 2013年第6期2591-2595,共5页 Journal of Central South University:Science and Technology
基金 国家自然科学基金资助项目(51176045)
关键词 柴油机 冷启动 碳氢吸附 分子模拟 蒙特卡洛 diesel cold start hydrocarbon molecular simulation Monte Carlo
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参考文献13

  • 1Bielaczyc P, Merkisz J, Pielecha J. Investigation of exhaust emissions from DI diesel engine during cold and warm start[J]. SAE Paper, 2001-01-1260.
  • 2高梦熊.耐特技术公司新型净化器及其应用[J].工程机械,2003,34(3):15-16. 被引量:1
  • 3ZHAOFuquan(Frank).汽油机近零排放技术[M].帅石金,译.北京:机械工业出版社,2010:243-255.
  • 4Sampara C S, Bissett E J, Chmielewski M. Global kinetics for a commercial diesel oxidation catalyst with two exhaust hydrocarbons[J]. Ind Eng Chern Res, 2008, 47(2): 311-322.
  • 5Tanaka Y, Hihara T, Nagata M, et al. Modeling of diesel oxidation catalyst[J]. Ind Eng Chern Res, 2005, 44(22): 8205-8212.
  • 6孙万臣,刘忠长,刘巽俊,宫本登,小川英之,河辺隆夫.燃料特性对小型压燃式发动机增负荷工况燃烧及HC排放的影响[J].吉林大学学报(工学版),2005,35(2):131-135. 被引量:7
  • 7成志明,尤丽,鄂加强,龚金科.江南风光车排气系统设计研究[J].现代车用动力,2006(1):30-33. 被引量:1
  • 8Tomazic D, Tatur M, Thornton M. Development of a diesel passenger car meeting Tier 2 emissions levels[J]. SAE Paper, 2004-01-058l.
  • 9Sampara C S, Bissett E J, Assanisa D. Hydrocarbon storage modeling for diesel oxidation catalysts[J]. Chemical Engineering Science, 2008, 63(21): 5179-5192.
  • 10Burke N R, Trimm D L, Howe R F. The effect of silica: Alumina ratio and hydrothermal ageing on the adsorption characteristics of BEA zeolites for cold start emission control[J]. Applied Catalysis B: Environmental, 2003, 46: 97-104.

二级参考文献9

  • 1刘忠长,朱昌吉,张振东.车用柴油机排气再循环控制系统[J].吉林大学学报(工学版),2004,34(3):337-341. 被引量:18
  • 2钟绍华,金国栋,张选国,章鸿.消声器优化设计及其性能分析方法的研究[J].内燃机工程,2005,26(1):55-58. 被引量:40
  • 3[2]Takaaki Kanazawa,Kazuhiro Sakurai.Development of the Automotive Exhaust Hydrocarbon Adsorbent[C].SAE 2001-01-0660.
  • 4[3]Suresh T,Gub.Design Considerations for Advanced Ceramic Catalyzator Supportor[C].SAE 2000-01-04.
  • 5刘巽俊.内燃机的排放与控制[M].北京:机械工业出版社,2002..
  • 6MIYAMOTO Noboru.Cycle-to-cycle Transient Characteristics of Diesel Emissions During Starting [C]∥ SAE Paper 1999-01-3495.
  • 7RAIHAN K A,TAKIMOTO F,OGAWA H,MIYAMOTO N. Time-Resolved Behavior of Unburned Hydrocarbon Components in Diesel Exhaust under Transient Operations[C]∥SAE Paper 2001-01-1259.
  • 8FUJIMOTO H,SENDA J. Combustion in a Small DI Diesel[C]∥SAE Paper 920697.
  • 9MIYAMOTO N. Cycle-to-cycle Transient Characte-ristics of Exhaust Gas Emissions from a Diesel Engine with Different Increasing and Decreasing Load Patterns[C]∥SAE Paper 970750.

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