The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.
The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.
Patent No.:
Date of Patent:
Dec. 19, 2017
Filed:
Apr. 13, 2012
Xionghou Gao, Beijing, CN;
Haitao Zhang, Beijing, CN;
Zhengguo Tan, Beijing, CN;
Di LI, Beijing, CN;
Dong Ji, Beijing, CN;
Hongchang Duan, Beijing, CN;
Chenxi Zhang, Beijing, CN;
Xionghou Gao, Beijing, CN;
Haitao Zhang, Beijing, CN;
Zhengguo Tan, Beijing, CN;
Di Li, Beijing, CN;
Dong Ji, Beijing, CN;
Hongchang Duan, Beijing, CN;
Chenxi Zhang, Beijing, CN;
PetroChina Company Limited, Beijing, CN;
Abstract
The present invention relates to a heavy oil catalytic cracking catalyst and preparation method thereof. The catalyst comprises 2 to 50% by weight of an ultra-stable rare earth type Y molecular sieve, 0.5 to 30% by weight of one or more other molecular sieves, 0.5 to 70% by weight of clay, 1.0 to 65% by weight of high-temperature-resistant inorganic oxides, and 0.01 to 12.5% by weight of rare earth oxide. The ultra-stable rare earth type Y molecular sieve is obtained as follows: the raw material, NaY molecular sieve, is subjected to a rare earth exchange and a dispersing pre-exchange, and the molecular sieve slurry is filtered, washed and subjected to a first calcination to produce a 'one-exchange one-calcination' rare earth sodium Y molecular sieve, wherein the order of the rare earth exchange and the dispersing pre-exchange is not limited; and the 'one-exchange one-calcination' rare earth sodium Y molecular sieve is further subjected to ammonium salt exchange for sodium reduction and a second calcination. The catalyst provided in the present invention is characteristic in its high heavy-oil-conversion capacity, a high total liquid yield and a high light oil yield.