采用连续固定床反应器,考察了几种具有不同酸性和孔道尺寸的分子筛催化剂上丁烯-2齐聚反应的性能,并与固体磷酸(SPA)催化剂进行了对比. 结果表明,分子筛催化剂的酸性和孔道尺寸是影响丁烯-2齐聚反应活性和选择性的重要因素. 具有八元环孔道的分子筛的扩散阻力大,反应活性很低; 十二元环分子筛的孔道降低了扩散阻力,有利于提高催化剂的低温活性和C=9+选择性; 十元环分子筛的孔道尺寸和强酸中心可以提高催化剂的活性,促进C=9+生成. SPA催化剂上C=9+选择性低于30%, 而具有强酸中心的十元环ZSM-5和ZSM-22分子筛,以及十二元环β分子筛催化剂上可高达50%以上,这说明分子筛催化剂具有更好的齐聚催化性能.
参考文献
[1] | 白尔铮.费托合成燃料的经济性及发展前景[J].化工进展,2004(04):370-374. |
[2] | O'Connor C T;Kojima M .[J].Catalysis Today,1990,6(03):329. |
[3] | Yang X;Dai L Y;Shan Y K;He M Y .[J].Chinese Journal of Catalysis,2003,24(12):895. |
[4] | Hong Q Y;Xie H X;Gai Y T;Guo H .[J].Journal of Petroleum Technology,2001,30(12):899. |
[5] | 单炜军,贺民,蔡天锡.以NiSO4/γ-Al2O3为催化剂丙烯齐聚制十二烯和十八烯工艺的研究[J].石油化工,2005(03):233-236. |
[6] | Mantilla A;Ferrat G;Lopez-Ortega A;Romero E;Tzompantzi F;Torres M;Ortiz-Islas E;Gomez R .Catalytic behavior of sulfated TiO2 in light olefins oligomerization[J].Journal of molecular catalysis, A. Chemical,2005(1/2):333-338. |
[7] | Mantilla A;Tzompantzi F;Ferrat G;Lopez-Ortega A Alfaro S Gomez R Torres M .[J].Catalysis Today,2005,107-108:707. |
[8] | Alcantara R;Alcantara E;Canoira L;Franco M J Herrera M Navarro A .[J].Reactive & Functional Polymers,2000,45(01):19. |
[9] | Yoon J W;Chang J-S;Lee H-D;Kim T-J Jhung S H .[J].Journal of Molecular Catalysis A:Chemical,2006,260(1-2):181. |
[10] | Peratello S;Molinari M;Bellussi G;Perego C .[J].Catalysis Today,1999,52(2-3):271. |
[11] | Occelli M L;Hsu J T;Galya L G .[J].Journal of Molecular Catalysis,1985,32(03):377. |
[12] | Miller S J .[J].Studies in surface science and catalysis,1987,38:187. |
[13] | Wilshier K G;Smart P;Western R;Mole T Behrsing T .[J].Applied Catalysis,1987,31(02):339. |
[14] | Schwarz S;Kojima M;O'Connor C T .[J].Applied Catalysis,1989,56(01):263. |
[15] | Wang D Zh;Lu X D;Dou X Y;Li W B Yang C H .[J].Applied Catalysis,1990,59(01):75. |
[16] | O'Connor C T;Schwarz S;Kojima M .[J].Studies in Surface Science and Catalysis,1991,65:491. |
[17] | Ngandjui L M T;Thyrion F C .[J].Industrial and Engineering Chemistry Research,1996,35(04):1269. |
[18] | Nkosi B;Ng F T T;Rempel G L .[J].Applied Catalysis A:General,1997,161(1-2):153. |
[19] | Chiche B.;Di Renzo F.;Ivanova II.;Fajula F.;Sauvage E. .Butene oligomerization over mesoporous MTS-type aluminosilicates[J].Journal of molecular catalysis, A. Chemical,1998(1/3):145-157. |
[20] | Martens J A;Ravishankar R;Mishin T E;Jacobs P A .[J].Angewandte Chemie International Edition,2000,39(23):4376. |
[21] | Yoon J W;Chang J-S;Lee H-D;Kim T-J Jhung S H .[J].Journal of Catalysis,2007,245(01):253. |
[22] | Martens J A;Verrelst W H;Mathys G M;Brown S H,Jacobs P A .[J].Angewandte Chemie International Edition,2005,44(35):5687. |
[23] | Tabak S A;Krambeck F J .[J].Hydrocarbon Process Int Ed,1985,64(09):72. |
[24] | Tabak S A;Krambeck F J;Garwood W E .[J].AICHE Journal,1986,32(09):1526. |
[25] | Quann R J;Green L A;Tabak S A;Krambeck F J .[J].Industrial & Engineering Chemistry Research,1988,27(04):465. |
[26] | 温陵生.固体磷酸催化剂的活性相[J].高等学校化学学报,1994(03):428. |
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