Citation: YAO Min, HU Si, WANG Jian, DOU Tao, WU Yong-Ping. Size Effect of HZSM-5 Zeolite on Catalytic Conversion of Methanol to Propylene[J]. Acta Physico-Chimica Sinica, doi: 10.3866/PKU.WHXB201206211
甲醇催化转化制丙烯中HZSM-5分子筛的尺寸效应
甲醇催化制丙烯(MTP)是一个具有重要工业应用的研究课题, 目前普遍采用的催化剂是HZSM-5 分子筛. 通过调节分子筛合成原料的配比、晶化温度和晶化时间等参数, 对所制备的不同晶粒尺寸的HZSM-5 分子筛, 综合利用X射线衍射(XRD)、扫描电镜(SEM)、N2吸附和氨气程序升温脱附(NH3-TPD)等手段表征了其晶格结构、表观形貌、孔结构以及酸性质. 利用固定床反应装置对HZSM-5 分子筛甲醇催化制丙烯的活性和稳定性进行了评价, 并采用热重(TG)分析技术对催化剂的积炭性能进行了考察. 实验结果表明, HZSM-5 分子筛粒度的减小可以增加分子筛比表面积、孔体积, 同时有更多开放的孔口及短的孔道长度, 有利于反应物分子的吸附和传质,并降低了产物分子在孔道中的扩散距离及发生二次反应的几率, 提高了催化剂的抗积炭能力和容炭能力以及稳定性; 而且所合成的小尺寸分子筛单位质量的总酸量及强酸量均有不同程度的下降, 有利于提高目标产物丙烯的选择性.
English
Size Effect of HZSM-5 Zeolite on Catalytic Conversion of Methanol to Propylene
Catalytic conversion of methanol to propylene (MTP) by HZSM-5 zeolite is of great importance in industrial applications. In this paper, a series of HZSM-5 zeolites with different crystal sizes were synthesized by adjusting the initial gel composition, crystallization temperature, and crystallization time. The crystal structure, size, morphology, pore structure, and acidity of HZSM-5 were investigated by X-ray diffraction (XRD), scanning electron microscopy (SEM), nitrogen adsorption, and temperature-programmed desorption of ammonia (NH3-TPD). The catalytic activity and stability of HZSM-5 with different crystal sizes for MTP were evaluated on a continuous flowing fixed-bed reactor. Coke deposited on HZSM-5 was analyzed by thermogravimetric (TG) analyzer. Results indicated that with smaller crystal size, HZSM-5 zeolite had larger surface area and pore volume, higher density of pore openings, and shorter path length of micropore channels that prevent side reactions. For MTP reaction, smaller crystal sizes of HZSM-5 showed a higher resistance and better tolerance to coke, and longer catalytic lifetime. The lowering of both the total and strong acidity on HZSM-5 with smaller crystal size favored a higher selectivity of target product, propylene.
-
Key words:
-
HZSM-5 zeolite
- / Crystal size
- / Methanol
- / Propylene
- / Acid property
- / Coke deposition
-
-
[1]
(1) Zhu, J.; Cui, Y.; Nawaz, Z.;Wang, Y.;Wei, F. Chin. J. Chem. Eng. 2010, 18, 979. doi: 10.1016/S1004-9541(09)60156-7
(1) Zhu, J.; Cui, Y.; Nawaz, Z.;Wang, Y.;Wei, F. Chin. J. Chem. Eng. 2010, 18, 979. doi: 10.1016/S1004-9541(09)60156-7
-
[2]
(2) Hao, Z. X.; Zhao, H. T.;Wang, L. J.; Xie, L. L.; Tian, Z.; Li, Q.H. Acta Phys. -Chim. Sin. 2009, 25, 829. [郝志显, 赵海涛,王利军, 解丽丽, 田震, 李庆华. 物理化学学报, 2009, 25,829.] doi: 10.3866/PKU.WHXB20090513(2) Hao, Z. X.; Zhao, H. T.;Wang, L. J.; Xie, L. L.; Tian, Z.; Li, Q.H. Acta Phys. -Chim. Sin. 2009, 25, 829. [郝志显, 赵海涛,王利军, 解丽丽, 田震, 李庆华. 物理化学学报, 2009, 25,829.] doi: 10.3866/PKU.WHXB20090513
-
[3]
(3) Dubois, D. R.; Obrzut, D. L.; Liu, J.; Thundimadathil, J.;Adekkanattu, P. M.; Guin, J. A.; Punnoose, A.; Seehra, M. S.Fuel Process. Technol. 2003, 83, 203. doi: 10.1016/S0378-3820(03)00069-9(3) Dubois, D. R.; Obrzut, D. L.; Liu, J.; Thundimadathil, J.;Adekkanattu, P. M.; Guin, J. A.; Punnoose, A.; Seehra, M. S.Fuel Process. Technol. 2003, 83, 203. doi: 10.1016/S0378-3820(03)00069-9
-
[4]
(4) Lee, Y. J.; Baek, S. C.; Jun, K.W. Appl. Catal. A: Gen. 2007,329, 130. doi: 10.1016/j.apcata.2007.06.034(4) Lee, Y. J.; Baek, S. C.; Jun, K.W. Appl. Catal. A: Gen. 2007,329, 130. doi: 10.1016/j.apcata.2007.06.034
-
[5]
(5) Yuan, C. Y.;Wei, Y. X.; Li, J. Z.; Xu, S. T.; Chen, J. R.; Zhou,Y.;Wang, Q. Y.; Xu, L.; Liu, Z. M. Chin. J. Catal. 2012, 33,367. [袁翠峪, 魏迎旭, 李金哲, 徐舒涛, 陈景润, 周游,王全义, 许磊, 刘中民. 催化学报, 2012, 33, 367.](5) Yuan, C. Y.;Wei, Y. X.; Li, J. Z.; Xu, S. T.; Chen, J. R.; Zhou,Y.;Wang, Q. Y.; Xu, L.; Liu, Z. M. Chin. J. Catal. 2012, 33,367. [袁翠峪, 魏迎旭, 李金哲, 徐舒涛, 陈景润, 周游,王全义, 许磊, 刘中民. 催化学报, 2012, 33, 367.]
-
[6]
(6) Lee, Y. J.; Kim, Y.W.; Viswanadham, N.; Jun, K.W.; Bae, J.W.Appl. Catal. A: Gen. 2010, 374, 18. doi: 10.1016/j.apcata.2009.11.019(6) Lee, Y. J.; Kim, Y.W.; Viswanadham, N.; Jun, K.W.; Bae, J.W.Appl. Catal. A: Gen. 2010, 374, 18. doi: 10.1016/j.apcata.2009.11.019
-
[7]
(7) Mao, D. S.; Guo, Q. S.; Meng, T. Acta Phys. -Chim. Sin. 2010,26, 2242. [毛东森, 郭强胜, 孟涛. 物理化学学报, 2010,26, 2242.] doi: 10.3866/PKU.WHXB20100814(7) Mao, D. S.; Guo, Q. S.; Meng, T. Acta Phys. -Chim. Sin. 2010,26, 2242. [毛东森, 郭强胜, 孟涛. 物理化学学报, 2010,26, 2242.] doi: 10.3866/PKU.WHXB20100814
-
[8]
(8) Mao, D. S.; Guo, Q. S.; Meng, T.; Lu, G. Z. Acta Phys. -Chim. Sin. 2010, 26, 338. [毛东森, 郭强胜, 孟涛, 卢冠忠. 物理化学学报, 2010, 26, 338.] doi: 10.3866/PKU.WHXB20100208(8) Mao, D. S.; Guo, Q. S.; Meng, T.; Lu, G. Z. Acta Phys. -Chim. Sin. 2010, 26, 338. [毛东森, 郭强胜, 孟涛, 卢冠忠. 物理化学学报, 2010, 26, 338.] doi: 10.3866/PKU.WHXB20100208
-
[9]
(9) Lu, J. Y.; Zhao, Z.; Xu, C. M.; Duan, A. J.; Zhang, P. Catal. Lett.2006, 109, 65. doi: 10.1007/s10562-006-0058-2(9) Lu, J. Y.; Zhao, Z.; Xu, C. M.; Duan, A. J.; Zhang, P. Catal. Lett.2006, 109, 65. doi: 10.1007/s10562-006-0058-2
-
[10]
(10) Firoozi, M.; Baghalha, M.; Asadi, M. Catal. Commun. 2009, 10,1582. doi: 10.1016/j.catcom.2009.04.021(10) Firoozi, M.; Baghalha, M.; Asadi, M. Catal. Commun. 2009, 10,1582. doi: 10.1016/j.catcom.2009.04.021
-
[11]
(11) Zhao, T. S.; Takemoto, T.; Yoneyama, Y.; Tsubaki, N. Chem. Lett. 2005, 34, 970. doi: 10.1246/cl.2005.970(11) Zhao, T. S.; Takemoto, T.; Yoneyama, Y.; Tsubaki, N. Chem. Lett. 2005, 34, 970. doi: 10.1246/cl.2005.970
-
[12]
(12) Zeng, Z. H. Shape-Selective Catalysis; China PetrochemicalPress: Beijing, 1994; pp 91-98. [曾昭槐. 择形催化. 北京:中国石化出版社, 1994: 91-98.](12) Zeng, Z. H. Shape-Selective Catalysis; China PetrochemicalPress: Beijing, 1994; pp 91-98. [曾昭槐. 择形催化. 北京:中国石化出版社, 1994: 91-98.]
-
[13]
(13) Wang, Y.; Zhao, B. Y.; Xie, Y. C. Acta Phys. -Chim. Sin. 2001,17, 966. [王钰, 赵碧英, 谢有畅. 物理化学学报, 2001, 17,966.] doi: 10.3866/PKU.WHXB20011102(13) Wang, Y.; Zhao, B. Y.; Xie, Y. C. Acta Phys. -Chim. Sin. 2001,17, 966. [王钰, 赵碧英, 谢有畅. 物理化学学报, 2001, 17,966.] doi: 10.3866/PKU.WHXB20011102
-
[14]
(14) Damodaran, K.;Wiench, J.W.; Cabral de Menezes, S. M.; Lam,Y. L.; Trebosc, J.; Amoureux, J. P.; Pruski, M. Microporous Mesoporous Mat. 2006, 95, 296. doi: 10.1016/j.micromeso.2006.05.034(14) Damodaran, K.;Wiench, J.W.; Cabral de Menezes, S. M.; Lam,Y. L.; Trebosc, J.; Amoureux, J. P.; Pruski, M. Microporous Mesoporous Mat. 2006, 95, 296. doi: 10.1016/j.micromeso.2006.05.034
-
[15]
(15) Kaarsholm, M.; Joensen, F.; Nerlov, J.; Cenni, R.; Chaouki, J.;Patience, G. S. Chem. Eng. Sci. 2007, 62, 5527. doi: 10.1016/j.ces.2006.12.076(15) Kaarsholm, M.; Joensen, F.; Nerlov, J.; Cenni, R.; Chaouki, J.;Patience, G. S. Chem. Eng. Sci. 2007, 62, 5527. doi: 10.1016/j.ces.2006.12.076
-
[16]
(16) Yang, Y.; Sun, C.; Du, J.; Yue, Y.; Hua,W.; Zhang, C.; Shen,W.;Xu, H. Catal. Commun. 2012, 24, 44. doi: 10.1016/j.catcom.2012.03.013(16) Yang, Y.; Sun, C.; Du, J.; Yue, Y.; Hua,W.; Zhang, C.; Shen,W.;Xu, H. Catal. Commun. 2012, 24, 44. doi: 10.1016/j.catcom.2012.03.013
-
[17]
(17) Li, J.; Xiong, G.; Feng, Z.; Liu, Z.; Xin, Q.; Li, C. Microporous Mesoporous Mat. 2000, 39, 275. doi: 10.1016/S1387-1811(00)00204-3(17) Li, J.; Xiong, G.; Feng, Z.; Liu, Z.; Xin, Q.; Li, C. Microporous Mesoporous Mat. 2000, 39, 275. doi: 10.1016/S1387-1811(00)00204-3
-
[18]
(18) Wei, R.; Li, C.; Yang, C.; Shan, H. J. Nat. Gas Chem. 2011, 20,261. doi: 10.1016/S1003-9953(10)60198-3(18) Wei, R.; Li, C.; Yang, C.; Shan, H. J. Nat. Gas Chem. 2011, 20,261. doi: 10.1016/S1003-9953(10)60198-3
-
[19]
(19) Reddy, J. K.; Motokura, K.; Koyama, T.; Miyaji, A.; Baba, T.J. Catal. 2012, 289, 53. doi: 10.1016/j.jcat.2012.01.014(19) Reddy, J. K.; Motokura, K.; Koyama, T.; Miyaji, A.; Baba, T.J. Catal. 2012, 289, 53. doi: 10.1016/j.jcat.2012.01.014
-
[20]
(20) Kim, S. H.; Komarneni, S.; Heo, N. H. Microporous Mesoporous Mat. 2011, 143, 243. doi: 10.1016/j.micromeso.2011.02.010(20) Kim, S. H.; Komarneni, S.; Heo, N. H. Microporous Mesoporous Mat. 2011, 143, 243. doi: 10.1016/j.micromeso.2011.02.010
-
[21]
(21) Gao, Z.; He, M. Y.; Dai, Y. Y. Zeolite Catalysis and Separation Technology; China Petrochemical Press: Beijing, 1999; pp45-56. [高滋, 何鸣元, 戴逸云. 沸石催化与分离技术.北京: 中国石化出版社, 1999: 45-56.](21) Gao, Z.; He, M. Y.; Dai, Y. Y. Zeolite Catalysis and Separation Technology; China Petrochemical Press: Beijing, 1999; pp45-56. [高滋, 何鸣元, 戴逸云. 沸石催化与分离技术.北京: 中国石化出版社, 1999: 45-56.]
-
[22]
(22) Mei, C. S.;Wen, P. Y.; Liu, Z. C.; Liu, H. X.;Wang, Y. D.; Yang,W. M.; Xie, Z. C.; Hua,W. M.; Gao, Z. J. Catal. 2008, 258,243. doi: 10.1016/j.jcat.2008.06.019(22) Mei, C. S.;Wen, P. Y.; Liu, Z. C.; Liu, H. X.;Wang, Y. D.; Yang,W. M.; Xie, Z. C.; Hua,W. M.; Gao, Z. J. Catal. 2008, 258,243. doi: 10.1016/j.jcat.2008.06.019
-
[23]
(23) Wen, P. Y.; Mei, C. S.; Liu, H. X.; Yang,W. M.; Chen, Q. L.Chem. React. Eng. Technol. 2007, 23, 386. [温鹏宇, 梅长松,刘红星, 杨为民, 陈庆龄. 化学反应工程与工艺, 2007, 23,386.]
(23) Wen, P. Y.; Mei, C. S.; Liu, H. X.; Yang,W. M.; Chen, Q. L.Chem. React. Eng. Technol. 2007, 23, 386. [温鹏宇, 梅长松,刘红星, 杨为民, 陈庆龄. 化学反应工程与工艺, 2007, 23,386.]
-
[1]
-
扫一扫看文章
计量
- PDF下载量: 1322
- 文章访问数: 3925
- HTML全文浏览量: 62

下载: