欢迎登录材料期刊网

材料期刊网

高级检索

考虑了烯烃、醇与酸的再吸附及其非本征效应(烯烃、醇与酸在催化剂孔道中的扩散作用、物理吸附及溶解度效应)对产物分布的影响,推导了基于详细反应机理的亚甲基插入的烷基机理F-T合成校正综合动力学模型.利用文献数据对动力学模型进行了回归,获得了与文献报道结果相一致的动力学参数.由校正动力学模型计算的烷烃、烯烃、醇与酸产物分布及烯烃比、醇烃比及酸烃比与实验数据较好地吻合.动力学计算结果表明,在铁锰催化剂上,烷烃、烯烃、醇与酸生成的反应是平行竞争反应,烯烃、醇与酸在催化剂表面的再吸附及二次反应导致产物分布偏离了ASF分布.动力学研究还表明,相同碳数的醇与酸产物在催化剂表面上再吸附及二次反应的机会比相同碳数的烯烃大.通过比较相同碳数的烯烃、醇与酸的分子体积及沸点,指出了在铁锰催化剂上,低碳数的烯烃、醇与酸的再吸附及二次反应对产物分布影响的非本征效应中,烯烃、醇与酸的扩散阻力不是主导效应.

参考文献

[1] Dry M E .[J].Catalysis Today,2002,71(3-4):227.
[2] Yamashita K;Barreto L .[J].ENERGY,2005,30(13):2453.
[3] Dry M E .[J].Applied Catalysis A:General,1996,138(02):319.
[4] Yang Y;Xiang H W;Xu Y Y;Bai L Li Y W .[J].Applied Catalysis A:General,2004,266(02):181.
[5] Teng B T;Zhang Ch H;Yang J;Cao D B Chang J Xiang H W Li Y W .[J].FUEL,2005,84(7-8):791.
[6] Dry M E .[J].Applied Catalysis A:General,2004,276(1-2):1.
[7] 滕波涛,常杰,刘颖,张成华,杨骏,郑洪岩,张荣乐,白亮,相宏伟,李永旺.工业Fe-Mn催化剂上基于详细反应机理的F-T合成动力学模型Ⅰ.烯烃再吸附动力学研究[J].催化学报,2005(08):693-700.
[8] 滕波涛,常杰,王刚,张成华,刘颖,郑洪岩,杨骏,张荣乐,白亮,相宏伟,李永旺.工业Fe-Mn催化剂上基于详细反应机理的F-T合成动力学模型Ⅱ.不同校正方法的动力学模型分析[J].催化学报,2005(08):701-706.
[9] Teng B T;Chang J;Yang J;Wang G Zhang Ch H Xu Y Y Xiang H W Li Y W .[J].FUEL,2005,84(7-8):917.
[10] Teng B T;Chang J;Zhang Ch H;Cao D B Yang J Liu Y Guo X H Xiang H W Li Y W .[J].Applied Catalysis A:General,2006,301(01):39.
[11] Wojciechowski B W .[J].Catalysis Review:Science and Engineering,1988,30(04):629.
[12] Santilli D S;Castner D G .[J].Energy and Fuels,1989,3(01):8.
[13] Lox E S;Marin G B;De Grave E;Bussiere P .[J].Applied Catalysis,1988,40:197.
[14] Zhang H B;Schrader G L .[J].Journal of Catalysis,1985,95(01):325.
[15] Komaya T;Bell A T .[J].Journal of Catalysis,1994,146(01):237.
[16] Iglesia E;Reyes S C;Madon R J .[J].Journal of Catalysis,1991,129(01):238.
[17] Jordan D S;Bell A T .[J].Journal of Physical Chemistry,1986,90(20):4797.
[18] Nowicki L;Ledakowicz S;Bukur D B .[J].Chemical Engineering Science,2001,56(03):1175.
[19] Kuipers EW.;Wilson JH.;Vinkenburg IH.;Oosterbeek H.;Scheper C. .NON-ASF PRODUCT DISTRIBUTIONS DUE TO SECONDARY REACTIONS DURING FISCHER-TROPSCH SYNTHESIS[J].Journal of Catalysis,1996(1):288-300.
[20] Van Der Laan G P;Beenackers A A C M .[J].Catalysis Review:Science and Engineering,1999,41(3-4):255.
[21] Wang G;Wang Y N;Yang J;Xu Y Y,Bai L,Xiang H W,Li Y W .[J].Industrial and Engineering Chemistry Research,2004,43(10):2330.
[22] Van Der Laan G P;Beenackers A A C M .[J].Industrial and Engineering Chemistry Research,1999,38(04):1277.
[23] Yang J;Liu Y;Chang J;Wang Y N,Bai L,Xu Y Y,Xiang H W,Li Y W,Zhong B .[J].Industrial and Engineering Chemistry Research,2003,42(21):5066.
[24] Vandenbussche KM.;Froment GF. .A STEADY-STATE KINETIC MODEL FOR METHANOL SYNTHESIS AND THE WATER GAS SHIFT REACTION ON A COMMERCIAL CU/ZNO/AL2O3 CATALYST[J].Journal of Catalysis,1996(1):1-10.
[25] Graaf G H;Winkelman J G M;Stamhuis E J;Beenackers A A C M .[J].Chemical engineering science,1988,43(08):2161.
[26] Dry M E .[J].Industrial and Engineering Chemistry:product Research and Development,1976,15(04):282.
[27] Zimmerman W H;Bukur D B .[J].Canadian Journal of Chemical Engineering,1990,68(02):292.
[28] Van Der Laan G P;Beenackers A A C M .[J].Applied Catalysis A:General,2000,193(1-2):39.
[29] Stephenson R M;Malanowski S.Handbook of the Thermodynamics of Organic Compounds[M].New York:Elsevier,1987
[30] McCabe W L;Smith J C;Harriott P.Unit Operations of Chemical Engineering[M].New York:McGraw-Hill,1993:521.
上一张 下一张
上一张 下一张
计量
  • 下载量()
  • 访问量()
文章评分
  • 您的评分:
  • 1
    0%
  • 2
    0%
  • 3
    0%
  • 4
    0%
  • 5
    0%