Catalytic Cracking of n-Hexane and n-Heptane over ZSM-5 Zeolite: Influence of Si[O.sub.2]/[Al.sub.2][O.sub.3] Ratio
The performance of two types of ZSM-5 zeolite catalysts (MFI-type zeolite, Si[O.sub.2]/[Al.sub.2][O.sub.3] = 50 and 300) was studied in the catalytic cracking of n-hexane and n-heptane as a model compound of light naphtha for production of light olefins at 500, 550, and 600[degrees]C. The physicoche...
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| Veröffentlicht in: | Petroleum chemistry 2018-05, Vol.58 (5), p.457 |
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| creator | Afroukhteh-Langaroudi, N Tarighi, S Khonakdar, H.A |
| description | The performance of two types of ZSM-5 zeolite catalysts (MFI-type zeolite, Si[O.sub.2]/[Al.sub.2][O.sub.3] = 50 and 300) was studied in the catalytic cracking of n-hexane and n-heptane as a model compound of light naphtha for production of light olefins at 500, 550, and 600[degrees]C. The physicochemical properties of ZSM-5 catalysts were characterized by means of XRD, BET, SEM and NH3-TPD. The influence of Si[O.sub.2]/[Al.sub.2][O.sub.3] molar ratio was investigated on conversion and product selectivity. ZSM-5 zeolite yielded higher conversion in the cracking of n-hexane compared to n-heptane and maximum conversion was achieved over ZSM-5(50) at 600[degrees]C. ZSM-5(50) showed higher alkane selectivity rather than olefins. It was found that ZSM-5(300) was more desirable in terms of having significant selectivity to light olefins as well as producing high propylene to ethylene ratio. The maximum propylene to ethylene ratio of 2.7 and 2.48 was observed over ZSM-5(300) at 500[degrees]C for n-hexane and n-heptane cracking, respectively. Keywords: catalytic cracking, ZSM-5 zeolite, n-alkane, light olefins DOI: 10.1134/S096554411805002X |
| doi_str_mv | 10.1134/S096554411805002X |
| format | Article |
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The physicochemical properties of ZSM-5 catalysts were characterized by means of XRD, BET, SEM and NH3-TPD. The influence of Si[O.sub.2]/[Al.sub.2][O.sub.3] molar ratio was investigated on conversion and product selectivity. ZSM-5 zeolite yielded higher conversion in the cracking of n-hexane compared to n-heptane and maximum conversion was achieved over ZSM-5(50) at 600[degrees]C. ZSM-5(50) showed higher alkane selectivity rather than olefins. It was found that ZSM-5(300) was more desirable in terms of having significant selectivity to light olefins as well as producing high propylene to ethylene ratio. The maximum propylene to ethylene ratio of 2.7 and 2.48 was observed over ZSM-5(300) at 500[degrees]C for n-hexane and n-heptane cracking, respectively. 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The physicochemical properties of ZSM-5 catalysts were characterized by means of XRD, BET, SEM and NH3-TPD. The influence of Si[O.sub.2]/[Al.sub.2][O.sub.3] molar ratio was investigated on conversion and product selectivity. ZSM-5 zeolite yielded higher conversion in the cracking of n-hexane compared to n-heptane and maximum conversion was achieved over ZSM-5(50) at 600[degrees]C. ZSM-5(50) showed higher alkane selectivity rather than olefins. It was found that ZSM-5(300) was more desirable in terms of having significant selectivity to light olefins as well as producing high propylene to ethylene ratio. The maximum propylene to ethylene ratio of 2.7 and 2.48 was observed over ZSM-5(300) at 500[degrees]C for n-hexane and n-heptane cracking, respectively. 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The physicochemical properties of ZSM-5 catalysts were characterized by means of XRD, BET, SEM and NH3-TPD. The influence of Si[O.sub.2]/[Al.sub.2][O.sub.3] molar ratio was investigated on conversion and product selectivity. ZSM-5 zeolite yielded higher conversion in the cracking of n-hexane compared to n-heptane and maximum conversion was achieved over ZSM-5(50) at 600[degrees]C. ZSM-5(50) showed higher alkane selectivity rather than olefins. It was found that ZSM-5(300) was more desirable in terms of having significant selectivity to light olefins as well as producing high propylene to ethylene ratio. The maximum propylene to ethylene ratio of 2.7 and 2.48 was observed over ZSM-5(300) at 500[degrees]C for n-hexane and n-heptane cracking, respectively. Keywords: catalytic cracking, ZSM-5 zeolite, n-alkane, light olefins DOI: 10.1134/S096554411805002X</abstract><pub>Springer</pub><doi>10.1134/S096554411805002X</doi></addata></record> |
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| subjects | Alkenes Ammonia Petroleum refining Zeolites |
| title | Catalytic Cracking of n-Hexane and n-Heptane over ZSM-5 Zeolite: Influence of Si[O.sub.2]/[Al.sub.2][O.sub.3] Ratio |
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