[1] J. A. Brydson, Plastics materials. Elsevier, 1999.
[2] M. R. Sakha, S. Soltanali, D. Salari, M. Rashidzadeh, and P. H. Tabrizi, “Synergistic effect of micro-meso-macroporous system and structural Al amount of ZSM-5 for intensification of light olefins production in n-hexane cracking,” J. Solid State Chem., vol. 301, pp. 122342, 2021.
[3] M. Monai, M. Gambino, S. Wannakao, and B. M. Weckhuysen, “Propane to olefins tandem catalysis: a selective route towards light olefins production,” Chem. Soc. Rev., 2021.
[4] Y. Yoshimura et al., “Catalytic cracking of naphtha to light olefins,” Catal. Surv. from Japan, vol. 4, no. 2, pp. 157–167, 2001.
[5] H. Abrevaya, “Cracking of naphtha range alkanes and naphthenes over zeolites,” in Studies in surface science and catalysis, vol. 170, Elsevier, pp. 1244–1251, 2007.
[6] B. Siddiqui, A. M. Aitani, M. R. Saeed, and S. Al-Khattaf, “Enhancing the production of light olefins by catalytic cracking of FCC naphtha over mesoporous ZSM-5 catalyst,” Top. Catal., vol. 53, no. 19, pp. 1387–1393, 2010.
[7] S. Soltanali, R. Halladj, A. Rashidi, and M. Bazmi, “Mixed templates application in ZSM-5 nanoparticles synthesis: effect on the size, crystallinity, and surface area,” Adv. Powder Technol., vol. 25, no. 6, pp. 1767–1771, 2014.
[8] R. Taj, E. Pervaiz, and A. Hussain, “Synthesis and catalytic activity of IM-5 zeolite as naphtha cracking catalyst for light olefins: a review,” J Chem Soc Pak, vol. 42, no. 2, pp. 305–316, 2020.
[9] R. Sadeghbeigi, Fluid catalytic cracking handbook: An expert guide to the practical operation, design, and optimization of FCC units. Butterworth-Heinemann, 2020.
[10] F. C. Jentoft and B. C. Gates, “Solid-acid-catalyzed alkane cracking mechanisms: evidence from reactions of small probe molecules,” Top. Catal., vol. 4, no. 1, pp. 1–13, 1997.
[11] J.-H. Kim, A. Ishida, M. Okajima, and M. Niwa, “Modification of HZSM-5 by CVD of various silicon compounds and generation of para-selectivity,” J. Catal., vol. 161, no. 1, pp. 387–392, 1996.
[12] R. K. Dubey et al., “Role of plant growth-promoting microorganisms in sustainable agriculture and environmental remediation,” Adv. PGPR Res., pp. 75–124, 2017.
[13] G. C. Smith, “Catalytic Cracking of n-Alkanes and n-Alkylbenzenes over H-ZSM-5 Zeolite.” Massachusetts Institute of Technology, 1993.
[14] J. S. Buchanan, J. G. Santiesteban, and W. O. Haag, “Mechanistic considerations in acid-catalyzed cracking of olefins,” J. Catal., vol. 158, no. 1, pp. 279–287, 1996.
[15] H. Krannila, W. O. Haag, and B. C. Gates, “Monomolecular and bimolecular mechanisms of paraffin cracking: n-butane cracking catalyzed by HZSM-5,” J. Catal., vol. 135, no. 1, pp. 115–124, 1992.
[16] A. Ahmad, S. R. Naqvi, M. Rafique, H. Nasir, and A. Sarosh, “Synthesis, characterization and catalytic testing of MCM-22 derived catalysts for n-hexane cracking,” Sci. Rep., vol. 10, no. 1, pp. 1–11, 2020.
[17] E. T. C. Vogt and B. M. Weckhuysen, “Fluid catalytic cracking: recent developments on the grand old lady of zeolite catalysis,” Chem. Soc. Rev., vol. 44, no. 20, pp. 7342–7370, 2015.
[18] T. F. Degnan, G. K. Chitnis, and P. H. Schipper, “History of ZSM-5 fluid catalytic cracking additive development at Mobil,” Microporous Mesoporous Mater., vol. 35, pp. 245–252, 2000.
[19] G. A. Somorjai and Y. Li, Introduction to surface chemistry and catalysis. John Wiley & Sons, 2010.
[20] A. A. Lappas, C. S. Triantafillidis, Z. A. Tsagrasouli, V. A. Tsiatouras, I. A. Vasalos, and N. P. Evmiridis, “Development of new ZSM-5 catalyst-additives in the fluid catalytic cracking process for the maximization of gaseous alkenes yield,” in Studies in Surface Science and Catalysis, vol. 142, Elsevier, 2002, pp. 807–814.
[21] J. M. Arandes, I. Torre, M. J. Azkoiti, J. Erena, M. Olazar, and J. Bilbao, “HZSM-5 zeolite as catalyst additive for residue cracking under FCC conditions,” Energy & fuels, vol. 23, no. 9, pp. 4215–4223, 2009.
[22] R. H. Harding, A. W. Peters, and J. R. D. Nee, “New developments in FCC catalyst technology,” Appl. Catal. A Gen., vol. 221, no. 1–2, pp. 389–396, 2001.
[23] I. Torre, J. M. Arandes, M. J. Azkoiti, M. Olazar, and J. Bilbao, “Cracking of coker naphtha with gas− oil. Effect of HZSM-5 zeolite addition to the catalyst,” Energy & fuels, vol. 21, no. 1, pp. 11–18, 2007.
[24] M. R. Sakha, S. Soltanali, D. Salari, M. Rashidzadeh, and P. Halimitabrizi, “Synergistic effect of Fe and Ga incorporation into ZSM-5 to increase propylene production in the cracking of n-hexane utilizing a microchannel reactor,” New J. Chem., vol. 45, no. 31, pp. 13833–13846, 2021.
[25] L. Zoubida and B. Hichem, “The nanostructure zeolites MFI-type ZSM5,” Nanocrystals and Nanostructures, pp. 43–62, 2018.
[26] J. S. Jung, T. J. Kim, and G. Seo, “Catalytic cracking of n-octane over zeolites with different pore structures and acidities,” Korean J. Chem. Eng., vol. 21, no. 4, pp. 777–781, 2004.
[27] S. Altwasser, C. Welker, Y. Traa, and J. Weitkamp, “Catalytic cracking of n-octane on small-pore zeolites", Microporous mesoporous Mater., vol. 83, no. 1–3, pp. 345–356, 2005.
[28] S. M. Al Wahabi, Conversion of methanol to light olefins on SAPO-34 kinetic modeling and reactor design. Texas A&M University, 2003.
[29] M. Kim, H.-J. Chae, T.-W. Kim, K.-E. Jeong, C.-U. Kim, and S.-Y. Jeong, “Attrition resistance and catalytic performance of spray-dried SAPO-34 catalyst for MTO process: Effect of catalyst phase and acidic solution,” J. Ind. Eng. Chem., vol. 17, no. 3, pp. 621–627, 2011.
[30] K. Y. Lee, H.-J. Chae, S.-Y. Jeong, and G. Seo, “Effect of crystallite size of SAPO-34 catalysts on their induction period and deactivation in methanol-to-olefin reactions,” Appl. Catal. A Gen., vol. 369, no. 1–2, pp. 60–66, 2009.
[31] D. Yuan et al., “Assembly of Sub‐Crystals on the Macroscale and Construction of Composite Building Units on the Microscale for SAPO‐34,” Chem. Asian J., vol. 13, no. 20, pp. 3063–3072, 2018.
[32] A. Z. Varzaneh, J. Towfighi, and A. Mohamadalizadeh, “Comparative study of naphtha cracking over SAPO-34 and HZSM-5: Effects of cerium and zirconium on the catalytic performance,” J. Anal. Appl. Pyrolysis, vol. 107, pp. 165–173, 2014.
[33] J. Pastvova et al., “Effect of enhanced accessibility of acid sites in micromesoporous mordenite zeolites on hydroisomerization of n-hexane,” Acs Catal., vol. 7, no. 9, pp. 5781–5795, 2017.
[34] B. W. Burbidge, I. M. Keen, and M. K. Eyles, “Physical and catalytic properties of the zeolite mordenite,” ACS Publications, 1971.
[35] A. Corma et al., “Determination of the pore topology of zeolite IM-5 by means of catalytic test reactions and hydrocarbon adsorption measurements,” J. Catal., vol. 189, no. 2, pp. 382–394, 2000.
[36] M. H. M. Ahmed et al., “Stability assessment of regenerated hierarchical ZSM-48 zeolite designed by post-synthesis treatment for catalytic cracking of light naphtha,” Energy & Fuels, vol. 31, no. 12, pp. 14097–14103, 2017.