Method for preparing and using cracking catalyst for oil production by lightening coal-tar pitch
A technology of coal tar pitch and cracking catalyst, which is applied in the direction of catalyst activation/preparation, chemical instruments and methods, physical/chemical process catalysts, etc. It can solve the problems of easy coking and deactivation of catalysts, low oil yield, etc., and achieve considerable economic benefits , good oil quality and low operating costs
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Embodiment 1
[0020] The preparation of the third-stage cracking catalyst of the fixed-bed reactor for direct production of various types of fuel oil by lightening coal tar pitch: immerse 100 parts by weight of commercial USY zeolite with a silicon-aluminum ratio of 3 into 100 parts by weight of an aqueous solution of 2.8 wt% metal ferric nitrate , impregnated at 80°C for 2 hours, left to stand after impregnated and poured out the supernatant, dried at 120°C for 4 hours, and then activated at 500°C for 5 hours to obtain the cracking catalyst of the present invention. The measured metal iron oxide content is 1.2wt% of the modified zeolite weight,
[0021] The cracking catalyst obtained by the above method is used in the third-stage coal tar pitch lightening process to produce fuel oil: coal tar is used as a solvent and mixed with coal tar pitch in advance, and heated to 108 ° C and stirred to dissolve, and then filtered to remove insoluble solids After the impurity, the raw material of the r...
Embodiment 2
[0023] The preparation of the third-stage cracking catalyst of the fixed-bed reactor for direct production of various fuel oils from the lightening of coal tar pitch: immerse 100 parts of commercial ZSM-5 zeolite with a silicon-aluminum ratio of 50 into 100 parts of 9.5wt% aqueous solution of metal lanthanum nitrate, at 80 ℃ for 2 hours, after immersion, let stand and pour out the supernatant, dry at 120 ℃ for 4 hours, and then activate at 500 ℃ for 5 hours to obtain the cracking catalyst of the present invention. After determination, the metal lanthanum oxide content is 5.3wt% of the modified zeolite weight,
[0024] The cracking catalyst obtained by the above method is used in the third-stage coal tar pitch lightening process to produce fuel oil: coal tar is used as a solvent and mixed with coal tar pitch in advance, heated to 120°C, stirred and dissolved, and then filtered to remove insoluble solid impurities After being heated by heat exchange, it enters the first fixed-be...
Embodiment 3
[0026] The preparation of the third stage cracking catalyst of fixed bed reactor: with 100 parts by weight, the commodity MCM-22 zeolite that silicon-alumina ratio is 32 is immersed in 100 parts by weight concentration and is 20.8wt% metal molybdenum nitrate aqueous solution, soaks 2 hours in 80 ℃, After immersion, let stand and pour out the supernatant, dry at 120°C for 4 hours, and then activate at 500°C for 5 hours to obtain the cracking catalyst of the present invention. It is determined that the content of the metal molybdenum oxide is 11.1wt% of the weight of the modified zeolite.
[0027] The cracking catalyst obtained by the above method is used in the third-stage coal tar pitch lightening process to produce fuel oil: coal tar is used as a solvent and mixed with coal tar pitch in advance, heated to 143°C, stirred and dissolved, and then filtered to remove insoluble solid impurities After being heated by heat exchange, it enters the first fixed-bed reactor. At a tempera...
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