Preparation and application of heavy metal pollution-resisting dual functional solid cocatalyst

A co-catalyst and dual-function technology, which is applied in the preparation and application of dual-function solid co-catalysts, can solve the problems of insufficient equilibrium conversion rate of the device system, limited hydrofining capacity, and influence on stable operation, etc. The effect of material cracking conversion performance, non-toxic preparation process, mild and simple conditions

Active Publication Date: 2011-04-20
REZEL CATALYSTS CORP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In this way, it has not really overcome the poisoning problem caused by the use of liquid blunt nickel additives, and due to its own insufficient cracking activity and the introduction of alkaline earth metals, it is easy to cause insufficient equilibrium conversion rate of the device system when adding and using, which affects the operation. proc

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Example Embodiment

[0036] Example 1

[0037] Take 330 grams of REY molecular sieve (produced by Nankai University Catalyst Factory, rare earth oxide 14.0% by weight, solid content 85% by weight), impregnated with 400 ml of 4% by weight lanthanum chloride (chemically pure reagent, Beijing Chemical Reagent Company) solution and mixed Homogeneous, dried at 120°C for 1 hour and then calcined at 500°C for 4 hours.

[0038] Add 150 grams of antimony trioxide (industrial product, produced by Jinan Chenxu Chemical Co., Ltd., with an average particle size of 0.3 to 0.9 microns, 98% by weight) in 500 ml of water. Co., Ltd.) grinding and dispersing into a slurry.

[0039]Add 3 liters of water to a 10-liter gel-forming tank, add the above-mentioned impregnated and roasted REY molecular sieve and the antimony trioxide slurry after grinding and dispersing, and add 660 grams of lanthanum carbonate powder (industrial product, Zibo Rongruida Powder Material Factory, 95% by weight) after beating for 30 minutes,...

Example Embodiment

[0040] Example 2

[0041] Take 340 grams of REUSY molecular sieve (produced by Nankai University Catalyst Factory, rare earth oxide 7.0% by weight, solid content 85% by weight), impregnated with 400 ml of 10% by weight lanthanum chloride (same as above) solution and mixed well, and dried at 110 ° C for 2 hours. It was calcined at 570°C for 1 hour.

[0042] Add 3 liters of water to a 10-liter glue tank, add the above-mentioned rare earth impregnated and roasted USY molecular sieve and 640 grams of lanthanum carbonate (same as above) powder and beat for 15 minutes, add 160 grams of colloidal antimony pentoxide (industrial product, Guangdong Guanghua Technology) Co., Ltd., with a solid content of 30% by weight and an average particle size of 30 nanometers), the colloid continued to be beaten for 15 minutes.

[0043] 250 grams of pseudo-boehmite (industrial products, Al 2 O 3 60% by weight, produced by Chinalco Shandong Aluminum Factory) and 600 ml of water were stirred at 60°C...

Example Embodiment

[0044] Example 3

[0045] Take 120 grams of REHY molecular sieve (produced by Nankai University Catalyst Factory, rare earth oxide 6.0% by weight, solid content 85% by weight), and use 8% by weight of cerium-rich mixed rare earth (industrial product, produced by Baotou Rare Earth Factory, Inner Mongolia, of which CeO 2 50wt%, La 2 O 3 21wt%, Pr 2 O 3 14wt%, Nd 2 O 3 13 wt %) solution in 200 ml and mixed uniformly, dried at 110°C for 2 hours and then calcined at 550°C for 2 hours.

[0046] Add 2 liters of water to a 10-liter glue tank, add the above-mentioned immersion and roasted REHY molecular sieve and 650 grams of lanthanum carbonate powder (same as above) and beat for 15 minutes, then add 470 grams of colloidal antimony pentoxide (same as above) and continue beating for 15 minutes.

[0047] Stir 530 grams of pseudo-boehmite (same as above) and 2 liters of water at 60 ° C and add 180 milliliters of 15 wt % hydrochloric acid (same as above), add to the above mixture af...

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Abstract

The invention relates to preparation and application of a dual functional solid cocatalyst which can resist pollution of vanadium and nickel in the process of cracking and converting heavy oils. The solid cocatalyst is characterized by being prepared from the following components in percentage by weight: 10 to 50 percent of high-activity lanthanum oxide, 0.1 to 20 percent of fine-grained antimonyoxide, 1 to 30 percent of high-activity Y molecular sieves of which the outer surfaces are modified with rare earth, and the balance of aluminum oxide-based binder which consists of acidified pseudoboehmite and/or alumina sol, wherein the high-activity lanthanum oxide is formed through gradual decomposition of the lanthanum carbonate which is directly added under the action of high temperature inpreparation and using processes; and the fine-grained antimony oxide is prepared from antimony trioxide and/or pentavalent colloidal antimony oxide which are/is directly added and have/has the average diameter of less than 1 micron. After the solid composition slurry is homogeneously ground, the slurry is subjected to spray drying to form a microspheric solid cocatalyst which comprises uniformly distributed heavy metal pollution-resisting active components with multiple apertures, and a cracking activity center to which macromolecules can get close. When the dual functional solid cocatalyst is used in the cracking and conversion process of catalytic cracking/pyrolysis of the heavy oil, toxication of the vanadium and the nickel in heavy fed stock on a catalyst in a system can be reduced, the distribution of a reaction product can be improved simultaneously, and the conversion efficiency of a heavy fed material and the yield of light hydrocarbon in the product are effectively improved.

Description

technical field [0001] The invention relates to the preparation and application of a heavy metal pollution-resistant co-catalyst, in particular to the preparation and application of a dual-functional solid co-catalyst for resisting vanadium and nickel pollution in the cracking and conversion process of heavy oil. Background technique [0002] In recent years, due to the heavy and inferior quality of crude oil worldwide, heavy and inferior crude oil has inevitably become part or even all of the raw materials in the refining process of refineries. The heavy and inferior quality of crude oil makes the content of heavy metals in the heavy oil (>350°C fraction) increase significantly. In the past, China's heavy oil has high nickel content, such as crude oil produced in Daqing, Shengli, Liaohe and other oilfields, etc., have encountered raw oil with high nickel content. In recent years, the amount of high-vanadium crude oil imported from the Middle East by China has increased ...

Claims

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Application Information

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IPC IPC(8): B01J29/16B01J33/00B01J35/08C10G11/05
Inventor 卓润生
Owner REZEL CATALYSTS CORP
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