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Catalyst composition for preparing low-carbon olefin by using inferior oil and preparation method thereof

A low-carbon olefin and low-quality oil technology, applied in molecular sieve catalysts, chemical instruments and methods, physical/chemical process catalysts, etc., can solve problems such as rising raw material costs, slow activity decay and anti-coking, and achieve high low-carbon olefin yields, Low hydrogen to carbon ratio, reducing the effect of manufacturing

Active Publication Date: 2012-12-12
REZEL CATALYSTS CORP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] With the rapid increase in the cost of raw materials brought about by the rapid development of the industrial economy, it is required to reduce the purchase and use of catalysts while refining heavy and inferior raw materials. Making full use of the high-cost ZSM-5 molecular sieve active components is the key to reducing the cost of catalysis. The catalytic cracking catalysts reported in the prior art are all made of composite ZSM-5 and Y molecular sieves on a catalyst microsphere particle. The method of making the composition of the catalyst uniform by the active components has the disadvantages that it cannot solve the mismatch problem of the two main active components well, and fails to make full use of the high-value ZSM-5 molecular sieve structure and relatively slow activity decay and its unique pore structure. Anti-coking characteristics
Two microsphere compositions with different molecular sieve active components and functions are used, and the ratio is flexibly adjusted according to the production conditions of the catalytic cracking / cracking unit and the difference in the loss rate of the two microspheres, so as to adapt to the process of producing low-carbon olefins from inferior oil raw materials and alleviate heavy metals Pollution and reduction of catalyst usage cost, not reported in the prior art

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0019] With 300 grams of phosphorus-containing HZSM-5 molecular sieves (industrial products, Catalyst Factory of Nankai University, silicon-aluminum ratio 30, P 2 o 5 3% by weight), and 500 grams of kaolin (industrial product, Suzhou Kaolin Company) and 3 liters of water were added to the gel-forming kettle for beating for 30 minutes, and 1 liter of silica sol (industrial product, Qingdao Jiyida Silicone Reagent Factory, SiO 2 25% by weight) after continuing beating for 10 minutes, use a high-shear mixing emulsifier (MBE-100L type, manufactured by Shanghai Environmental Protection Equipment General Factory) beating and homogenizing after 30 minutes in the laboratory with a small spray dryer (LPG-5 type, Manufactured by Changzhou Jianda Drying Equipment Co., Ltd.), the microsphere A of Example 1 is made, its average particle diameter is 65 microns, and the abrasion strength is 1.5% by weight.

[0020] With 150 grams of rare earth USY molecular sieves (the same as above, unit c...

Embodiment 2

[0022] With 250 grams of phosphorus-containing rare earth ZSM-5 molecular sieves (same as above, silicon-aluminum ratio 50, P 2 o 5 2% by weight, rare earth oxide 2% by weight), 550 grams of kaolin (same as above) and 3 liters of water for beating for 30 minutes, add 1 liter of silica sol (same as above) for beating for 10 minutes, and beat with a high-shear mixing emulsifier (same as above) After homogenizing for 40 minutes, microspheres A of Example 2 were made in the laboratory with a small spray dryer (same as above), with an average particle diameter of 62 microns and an abrasion strength of 1.4% by weight.

[0023] With 130 grams of USY molecular sieve (same as above, unit cell 2.455 nanometers), 800 grams of kaolin (same as above), 20 grams of carboxymethyl cellulose (industrial product, Xinfeng Cellulose Factory, Dacheng County, Hebei Province, purity 90%) 3 liters of water and 1 Silica sol (same as above) was spray-dried and molded in the same way to obtain microsphe...

Embodiment 3

[0025] 140 g NH 4 ZSM-5 (same as above, silicon-aluminum ratio 25) and 140 grams of rare earth ZSM-5 molecular sieve (same as above, silicon-aluminum ratio 50), 550 grams of kaolin (same as above) and 3 liters of water after beating for 30 minutes, add 1 liter of silica sol (same as above) After beating for 15 minutes, make embodiment 3 microspheres A with high-shear mixing and emulsifying machine (same as above) beating and homogenizing for 50 minutes on laboratory small spray drier (same as above), its average particle diameter is 66 microns, wear Strength 1.5% by weight.

[0026] With 160 grams of rare earth Y molecular sieves (the same as above, 16% by weight of rare earth oxides), 1000 grams of kaolin (same as above), 20 grams of microcrystalline cellulose (industrial products, Wuhan Xianbao Biochemical Technology Co., Ltd., 97%) 3 liters of water and 1 liter Silica sol (same as above) was spray-dried and molded in the same way to obtain microsphere B of Example 3, with ...

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Abstract

The invention discloses a catalyst composition suitable for preparing low-carbon olefin by using inferior oil and a preparation method thereof. The catalyst composition is characterized by consisting of two microspheres A and B, wherein the microsphere A is a shape-selecting cracking microsphere A consisting of 15-60wt% of ZSM-5 molecular sieve, 15-35wt% of silica sol in SiO2 and the balance of kaolin, and the wear strength of the microsphere A is not more than 2.0wt%; the microsphere B is a low-cost inferior oil conversion microsphere B consisting of 5-20wt% of Y molecular sieve, 10-30wt% ofsilica sol in SiO2, 0.5-5 wt% of pore forming agent and the balance of kaolin, the pore volume of the microsphere B is 0.1-0.5 ml / g, and the wear strength of the microsphere B is 2.5-4.5wt%; and the microspheres A and B are respectively shaped as a microsphere with a mean grain size of 50-80 microns by pulping and spray drying, and the adding proportions of the microspheres A and B are adjusted according to the run loss rate difference in the device so as to maintain the weight ratio of the microsphere A to the microsphere B of 1-(5: 1) in a system catalyst inventory. The composition is specifically suitable for the catalytic cracking / splitting process for fecundating low-carbon olefin by using inferior raw oil, and has the advantages of high low-carbon olefin yield, heavy metal pollutionresistance and low catalyst consumption cost.

Description

technical field [0001] The invention relates to a catalyst for catalytic conversion of petroleum hydrocarbons, in particular to a catalyst composition for producing low-carbon olefins from inferior raw material oil under catalytic cracking / cracking conditions and a preparation method thereof, belonging to the field of petrochemical catalysts. Background technique [0002] Low-carbon olefins such as ethylene, propylene and butene are important organic chemical raw materials, which are widely used in the manufacture of polyolefins and as raw materials for the production of bulk chemical products. With the further development of the chemical industry and the plastic products industry, the demand for low-carbon olefins has grown rapidly, and a process route for the production of low-carbon olefins by catalytic cracking of paraffin-based vacuum gas oil has been developed, which provides a solid foundation for the production of low-carbon olefins from heavy raw materials An effect...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/80C10G11/05
Inventor 卓润生
Owner REZEL CATALYSTS CORP