Method for preparing low carbon number olefin by catalytic pyrolysis
A technology of catalytic cracking and carbon number, applied in the direction of hydrocarbon cracking to produce hydrocarbons, etc., can solve the problems of low conversion rate of raw materials and low propylene yield, and achieve the effects of low reaction temperature, high propylene yield and long service life
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Embodiment 1
[0040] Embodiment 1 preparation catalyst A
[0041] With 50g ZRP molecular sieve (provided by Beijing Wanshuyuan Economic Technology Trade Center, SiO 2 / Al 2 o 3 >200), 50g silicon oxide (specific surface area >200m 2 / g of high-purity silicon oxide), 2g of scallop powder and mix; add 80ml of 5% nitric acid after mixing, extrude into 2mm cylindrical shape after mixing, and cut into 2-3mm; respectively at 80°C and 120°C Dry for 10 hours, then calcined at 580°C for 6 hours, take it out and cool to room temperature, and put it in a desiccator for later use. The catalyst prepared in this way is designated Catalyst A.
Embodiment 2
[0042] Example 2 Preparation of Catalyst B
[0043] 45g ZRP molecular sieve (SiO 2 / Al 2 o 3 >200), 45g of silicon oxide, 10g of magnesium oxide and 2g of turnip powder were mixed, and after mixing, 80ml of 5% nitric acid was added. Other operating methods are the same as in Example 1. The catalyst prepared in this way is designated Catalyst B.
Embodiment 3
[0044] Example 3 Preparation of Catalyst C
[0045] 45g ZRP molecular sieve (SiO 2 / Al 2 o 3 >200), 45g of silicon oxide, 10g of zirconia and 2g of turnip powder were mixed, and after mixing, 80ml of 5% nitric acid was added. Other operating methods are the same as in Example 1. The catalyst prepared in this way is designated Catalyst C.
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