Olefin cracking catalyst resulting in high diesel oil yield and its prepn

A cracking catalyst and catalyst technology, applied in cracking, catalytic cracking, petroleum industry, etc., can solve the problems of reducing the effect of gasoline olefins, low yield of light oil, high yield of coke, etc., to improve coke selectivity and diesel selectivity , Strong heavy oil cracking ability and strong olefin reduction ability

Inactive Publication Date: 2004-06-23
PETROCHINA CO LTD
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  • Abstract
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  • Claims
  • Application Information

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Problems solved by technology

CN1317547 discloses a method for producing active components of olefin-reducing catalysts, which is compounded with 0.5-5% ZSM-5, 0.5-15% rare earth Y zeolite and 2040% phosphorus and rare earth composite modified ultrastable Y zeolite, wherein phosphorus The rare earth content of Y zeolite compound modified with rare earth is 2-12%, the unit cell parameter is 2.445-2.465nm, and the phosphorus content is 0.2-3% (calculated as P). The method is to first carry out rare earth modification, and then carry out phosphorus modification Sexual treatment: CN1217231A discloses the preparation method of phosphorus-containing zeolite molecular sieve. The modified faujasite molecular sieve is impregnated with phosphorus-containing solution, dried, and roasted at 450-600°C for more than 0.5 hours. The catalyst containing this molecular sieve increases the yield of diesel oil. However, the effect of reducing gasoline olefins is not stated
[0005] To sum up, the olefin-reducing catalyst prepared by the prior art has a certain olefin-reducing ability, but the main disadvantages are high coke yield, low light oil yield, especially the obvious drop in diesel yield
The domestic situation is that the demand for diesel oil has increased significantly, and the supply of diesel oil is in short supply. The olefin-reducing catalyst developed by using the existing technology will undoubtedly aggravate the contradiction between supply and demand of diesel oil, and affect the economic benefits of the refinery.

Method used

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  • Olefin cracking catalyst resulting in high diesel oil yield and its prepn
  • Olefin cracking catalyst resulting in high diesel oil yield and its prepn

Examples

Experimental program
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Effect test

Embodiment 1

[0039] In a heated reactor, add 3000 g (dry basis) sodium Y molecular sieve and a certain amount of deionized water to make a slurry with a solid content of 150 g / l, slowly add 2.14 liters of rare earth chloride, and adjust the system pH=3.2, heated to 90°C, exchanged for 0.5 hours, filtered, washed, and the filter cake was roasted at 510°C for 2.0 hours at 10% water vapor. Mix the obtained "one-cross-baked" rare earth sodium Y with a certain amount of deionized water to form a slurry with a solid content of 145 g / l. Slowly add 1.2 liters of rare earth chloride, adjust the pH of the system to 3.5, and increase the temperature to Exchange at 90°C for 1.2 hours, then add 200 grams of ammonium phosphate and 1100 grams of ammonium sulfate, stir evenly, continue at about 75°C for 0.5 hours, filter, wash, and roast the filter cake at 50% moisture and 650°C for 2 hours to prepare The compound modified Y zeolite of phosphorus and rare earth in the present invention, namely ultra-stable ra...

Embodiment 2

[0042] In a heated reactor, add 3000 g (dry basis) sodium Y molecular sieve and a certain amount of deionized water to make a slurry with a solid content of 120 g / l. Slowly add 1.69 liters of rare earth nitrate to adjust the pH of the system =3.8, heat up to 78°C, exchange for 1.0 hour, filter, wash, and roast the filter cake at 80% water vapor and 620°C for 1.0 hour. Mix the obtained "one-cross-one-baking" rare earth sodium Y with a certain amount of deionized water to make a slurry with a solid content of 125 g / l. Slowly add 1.7 liters of rare earth nitrate, adjust the pH of the system to 3.9, and increase the temperature to 85. ℃, exchange for 1.5 hours, then add 120 grams of diammonium hydrogen phosphate and 600 grams of ammonium oxalate, stir evenly, continue at about 70 ℃ for 1.0 hour, filter, wash, the filter cake is roasted at 20% water vapor and 500 ℃ for 1.5 hours, the preparation The modified molecular sieve B described in the present invention is obtained.

[0043] Add...

Embodiment 3

[0045] In a heated reactor, add 3000 g (kilo) sodium Y molecular sieve and a certain amount of deionized water to make a slurry with a solid content of 100 g / l. Slowly add 2.95 liters of rare earth nitrate to adjust the pH of the system =4.0, heat up to 82°C, exchange for 1.5 hours, filter, wash, and roast the filter cake at 50% water vapor and 640°C for 3.0 hours. Then mix with a certain amount of deionized water to make a slurry with a solid content of 160 g / L, slowly add 0.80 liters of rare earth chloride, adjust the system pH = 3.1, heat up to 80 ℃, exchange for 0.6 hours, and then add phosphoric acid diphosphate 250 grams of ammonium hydrogen and 400 grams of ammonium nitrate, stir evenly, continue at about 70°C for 2.0 hours, filter, wash, and roast the filter cake at 85% water vapor and 490°C for 1.0 hour to prepare the high-efficiency olefin-reducing composition of the present invention Score and record it as modified molecular sieve C.

[0046] Add 4.9 liters of water, 10...

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Abstract

The olefin cracking catalyst resulting in high diesel oil yield contains phosphorus and RE compositely modified Y-zeolite, or named superstable RE Y-zeolite, in 5-45 wt%. The superstable RE Y-zeolite is prepared with Na zeolite as material and through RE exchange, the first roasting, reaction with RE, phosphorus containing matter and ammonium salt and the second roasting. The catalyst has the recommended components including superstable RE Y-zeolite 5-45 wt%, one or several kinds of other zeolite 0.5-30 wt%, clay 0.5-70 wt%, and high temperature resisting inorganic oxide 1.0-65 wt%, and contains phosphorus 0.3-2.5 wt% and RE oxide 1.5-6.0. The preparation process of the catalyst includes the mixing of the said components, homogenizing, spraying and post-treatment. The catalyst has powerful olefin cracking capacity, high diesel oil yield, low coke yield and powerful heavy oil cracking capacity.

Description

Technical field [0001] The invention relates to an olefin-reducing cracking catalyst capable of producing more diesel oil and a preparation method thereof, and more specifically, a catalyst for reducing olefin-reducing production of diesel oil suitable for a catalytic cracking process and a preparation method thereof. Background technique [0002] As many as 80% of the total domestic gasoline is cracked gasoline with olefin content between 40-60%, which is far from the new national standard (olefin content does not exceed 35v%), and the high olefin content in gasoline causes automobile exhaust One of the main reasons for high emissions. The development of cracking catalysts with strong olefin reduction capabilities has become the current focus of research in the field of catalysis. [0003] From the perspective of the international FCC catalyst market, the well-known AKZO catalyst company and GRACE company already have corresponding catalyst products. From the analysis of the obt...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G11/02
Inventor 刘丛华高雄厚张海涛孙书红张忠东
Owner PETROCHINA CO LTD
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