Catalytic cracking catalyst for high-efficiency conversion of heavy oil and preparation method thereof

Patent metadata

Field	Value
Publication number	US-9968918-B2
Application number	US-201214404776-A
Country	US
Kind code	B2
Filing date	Jul 27, 2012
Priority date	Jun 1, 2012
Publication date	May 15, 2018
Grant date	May 15, 2018

Abstract

The present invention provides a catalytic cracking catalyst for heavy oil and preparation methods thereof. The catalyst comprises 2 to 50% by weight of a phosphorus-containing ultrastable rare earth Y-type 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 a rare earth oxide. The phosphorus-containing ultra-stable rare earth Y-type molecular sieve uses a NaY molecular sieve as a raw material. The raw material is subjected to a rare-earth exchange and a dispersing pre-exchange; the molecular sieve slurry is then filtered, washed with water and subjected to a first calcination to obtain a rare earth sodium Y molecular sieve which has been subjected to such “first-exchange first-calcination”, wherein the steps of rare earth exchange and dispersing pre-exchange are not restricted in sequence; and then the rare earth sodium Y molecular sieve which has been subjected to “one-exchange one-calcination” is subjected to “second exchange and second calcination” including ammonium exchange and a phosphorus modification, wherein the steps of the ammonium exchange and the phosphorus modification are not restricted in sequence. The steps of the ammonium exchange and the phosphorus modification can be conducted continuously or non-continuously, the second calcination is conducted after the ammonium exchange for reducing sodium, the phosphorus modification can be conducted before or after the second calcination. The catalyst provided by the invention has the characteristics of high heavy oil conversion capacity, high total liquid yield, and high yield of light oil.

First claim

What is claimed is:

1. A catalytic cracking catalyst for heavy oil, characterized in that the catalyst composition comprises
2% to 50% by weight of a phosphorus-containing ultrastable rare earth Y-type 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;
wherein the phosphorus-containing ultrastable rare earth Y-type molecular sieve comprises 1% to 20% by weight of rare earth oxide, not more than 1.2% by weight of sodium oxide, and 0.1% to 5% by weight of phosphorus in terms of P, and has a crystallinity of 51% to 69%, and a lattice parameter of 2.449 nm to 2.469 nm;
wherein the phosphorus-containing ultrastable rare earth Y-type molecular sieve is prepared by a process comprising,
(a) treating a NaY-type molecular sieve to a rare-earth exchange, a dispersing pre-exchange, and a first calcination to afford a “one-exchanged one-calcinated” rare earth sodium Y-type molecular sieve, wherein the rare-earth exchange and the dispersing pre-exchange are carried out in an unlimited sequence, and are carried out consecutively without a calcination process therebetween; and
subjecting the “one-exchanged one-calcinated” rare earth sodium Y-type molecular sieve to an ammonium salt exchange, a phosphorus modification and a second calcination to obtain a phosphorous-containing ultrastable rare earth Y-type molecular sieve, wherein the ammonium salt exchange and the phosphorus modification are carried out in an unlimited sequence, and the second calcination is performed after the ammonium salt exchange; and
(b) mixing the phosphorus-containing ultrastable rare earth Y-type molecular sieve, clay, and a precursor of a high-temperature resistant inorganic oxide to obtain a mixture, and homogenizing, spraying, and calcinating the mixture to obtain the catalyst cracking catalyst,
wherein a dispersing agent in the dispersing pre-exchange process is any one or more selected from sesbania powder, boric acid, urea, ethanol, polyacrylamide, acetic acid, oxalic acid, adipic acid, formic acid, hydrochloric acid, nitric acid, citric acid, salicylic acid, tartaric acid, benzoic acid, and starch; and wherein no ammonium salt is used in the rare earth exchange or the dispersing pre-exchange.

2. The catalytic cracking catalyst for heavy oil according to claim 1 , wherein the dispersing pre-exchange comprises adding the dispersing agent in an amount of 0.2% to 5% by weight, an exchange temperature is 60° C. to 95° C., and an exchange duration is 0.1 to 1.5 h.

3. The catalytic cracking catalyst for heavy oil according to claim 1 , wherein the one or more other molecular sieves are selected from one or more of Y-type zeolite or a modification thereof, L zeolite or a modification thereof, ZSM-5 zeolite or a modification thereof, β zeolite or a modification thereof, aluminum phosphate zeolite or a modification thereof, and Ω zeolite or a modification thereof, wherein the modification to the molecular sieves is selected from the group consisting of HY, USY, REY, REHY, REUSY, H-ZSM-5, and Hβ.

4. The catalytic cracking catalyst for heavy oil according to claim 1 , wherein the clay is selected from one or more of kaolin, halloysite, montmorillonite, sepiolite, and perlite.

5. The catalytic cracking catalyst for heavy oil according to claim 1 , wherein the high-temperature-resistant inorganic oxide is selected from one or more of Al 2 O 3 , SiO 2 , SiO 2 —Al 2 O 3 , and AlPO 4 .

6. A preparation method of the catalytic cracking catalyst for heavy oil comprising 2% to 50% by weight of a phosphorus-containing ultrastable rare earth Y-type 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; wherein the phosphorus-containing ultrastable rare earth Y-type molecular sieve comprises 1% to 20% by weight of rare earth oxide, not more than 1.2% by weight of sodium oxide, and 0.1% to 5% by weight of phosphorus in terms of P, and has a crystallinity of 51% to 69%, and a lattice parameter of 2.449 nm to 2.469 nm, wherein the method comprises the steps of:
(1) preparing a phosphorus-containing ultrastable rare earth Y-type molecular sieve from a NaY molecular sieve comprising a rare-earth exchange, a dispersing pre-exchange, and a first calcination to afford a “one-exchanged one-calcinated” rare earth sodium Y-type molecular sieve, wherein the rare-earth exchange and the dispersing pre-exchange are carried out in an unlimited sequence; and
subjecting the “one-exchanged one-calcinated” rare earth sodium Y-type molecular sieve to an ammonium salt exchange, a phosphorus modification and a second calcination to obtain a phosphorous-containing ultrastable rare earth Y-type molecular sieve, wherein the ammonium salt exchange and the phosphorus modification are carried out in an unlimited sequence, and the second calcination is performed after the ammonium salt exchange; and
(2) mixing the phosphorus-containing ultrastable rare earth Y-type molecular sieve, clay, and a precursor of a high-temperature resistant inorganic oxide to obtain a mixture, and homogenizing, spraying, and calcinating the mixture to obtain the catalyst cracking catalyst,
wherein a dispersing agent in the dispersing pre-exchange process is any one or more selected from sesbania powder, boric acid, urea, ethanol, polyacrylamide, acetic acid, oxalic acid, adipic acid, formic acid, hydrochloric acid, nitric acid, citric acid, salicylic acid, tartaric acid, benzoic acid, and starch; and wherein no ammonium salt is used in the rare earth exchange or the dispersing pre-exchange.

7. The preparation method according to claim 6 , wherein the rare-earth exchange comprises
adding a rare earth compound, wherein the mass ratio of the rare earth oxide (RE 2 O 3 ) equivalent of the rare earth compound to Y zeolite is 0.005 to 0.25,
an exchange temperature of 0 to 100° C.,
an exchange pH of 2.5 to 6.0, and
an exchange duration of 0.1 to 2 h.

8. The preparation method according to claim 7 , wherein the mass ratio of RE 2 O 3 to Y zeolite is 0.01 to 0.20, the exchange temperature is 60° C. to 95° C., the exchange pH is 3.5 to 5.5, and the exchange duration is 0.3 to 1.5 h.

9. The preparation method according to claim 6 , wherein the phosphorus modification comprises
adjusting the molecular sieve slurry to a concentration, in terms of a solid content, of 80 to 400 g/L, and
adding 0.1% to 5% by weight of phosphorus-containing compound in terms of P for an exchange at an exchange temperature of 0 to 100° C. for an exchange duration of 0.1 to 1.5 h.

10. The preparation method according to claim 8 , wherein the phosphorus-containing compound is any one or more selected from phosphoric acid, phosphorous acid, phosphoric anhydride, diammonium phosphate, monoammonium phosphate, triammonium phosphate, triammonium phosphite, monoammonium phosphite, and aluminum phosphate.

11. The preparation method according to claim 6 , wherein the rare-earth exchange and the dispersing pre-exchange independently comprises a tank-type exchange, belt-type exchange, filter cake exchange, and combinations thereof.

12. The preparation method according to claim 6 , wherein the rare-earth exchange and the dispersing pre-exchange are multiple exchanges.

13. The preparation method according to claim 6 , wherein the first calcination is carried out at 350° C. to 700° C. under 0 to 100% steam for 0.3 to 3.5 h.

14. The pr

Assignees

• Gao Xionghou
• Zhang Haitao
• Li Di
• Tan Zhengguo
• Duan Hongchang
• Li Xueli
• Liu Chaowei
• Zheng Yunfeng
• Huang Xiaoliang
• Cai Jinjun
• Pan Zhishuang
• Sun Xueqin
• Petrochina Co Ltd

Inventors

• Gao Xionghou
• Zhang Haitao
• Li Di
• Tan Zhengguo
• Duan Hongchang
• Li Xueli
• Liu Chaowei
• Zheng Yunfeng
• Huang Xiaoliang
• Cai Jinjun
• Pan Zhishuang
• Sun Xueqin

Classifications

• B01J37/30

  Ion-exchange · CPC title

• C10G11/05

  Crystalline alumino-silicates, e.g. molecular sieves · CPC title

• B01J35/109

  Operations & Transport · mapped topic

• B01J29/605

  containing rare earth elements, titanium, zirconium, hafnium, zinc, cadmium, mercury, gallium, indium, thallium, tin or lead · CPC title

• B01J29/80

  Mixtures of different zeolites · CPC title