2012
DOI: 10.1134/s0965544112060059
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Catalytic cracking of vegetable oils for production of high-octane gasoline and petrochemical feedstock

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Cited by 33 publications
(8 citation statements)
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“…There are two possible reasons for the low oil flowing speed during catalytic cracking of carinata oil over regenerated Zn/Na-ZSM-5. Firstly, the size of vegetable oil triglyceride molecules is known to reach 4.37 nm [42]. Compared to fresh Zn/Na-ZSM-5, the lower pore size of regenerated Zn/Na-ZSM-5 might inhibit more carinata oil triglyceride molecules to flow through the catalyst pore channels for cracking, which increased the aggregation of triglyceride molecules on the catalyst.…”
Section: Resultsmentioning
confidence: 99%
“…There are two possible reasons for the low oil flowing speed during catalytic cracking of carinata oil over regenerated Zn/Na-ZSM-5. Firstly, the size of vegetable oil triglyceride molecules is known to reach 4.37 nm [42]. Compared to fresh Zn/Na-ZSM-5, the lower pore size of regenerated Zn/Na-ZSM-5 might inhibit more carinata oil triglyceride molecules to flow through the catalyst pore channels for cracking, which increased the aggregation of triglyceride molecules on the catalyst.…”
Section: Resultsmentioning
confidence: 99%
“…For processing of the lignocellulose feedstock dur ing pyrolysis, it is proposed that zeolite catalysts based on ZSM 5 should be used [196,197], which increase the yield of light alkenes. Sequential combination of pyrolysis, hydrodeoxygenation, and catalytic cracking provides an increase in the yield of light alkenes to 37 wt % or more [198].…”
Section: Preparation Of Propylene From Biological Raw Materialsmentioning
confidence: 99%
“…Doronin et al (Doronin et al, 2012) evaluated the properties of two zeolite catalysts, HZSM-5 and HY with varied composition matrix al 2 O 3 , si-al rate and siO 2 . it was studied cracking of sunflower oil using an mixture HY:HZSM-5 catalyst.…”
Section: Cracking and Deoxygenation Of Molecules Modelsmentioning
confidence: 99%