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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. proceed smoothly
[0015] At present, the hydrorefining capacity of my country's refineries is limited and the cost is high, which is far from meeting the needs of actual production. The national conditions make most of my country's refineries limited in the selection of raw material oil, resulting in a period of time. heavy metal content will remain high

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] Get 330 grams of REY molecular sieves (produced by Nankai University Catalyst Factory, rare earth oxide 14.0% by weight, solid content 85% by weight), impregnate and mix with 400 ml of lanthanum chloride (prepared by chemically pure reagents, Beijing Chemical Reagent Company) solution by 4% by weight Uniform, 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., average particle size 0.3 to 0.9 micron, 98% by weight) in 500 milliliters of water Co., Ltd.) ground and dispersed into a slurry.

[0039]Add 3 liters of water in 10 liters of glue tanks, add the above-mentioned REY molecular sieve after impregnating and roasting and the antimony trioxide slurry after grinding and dispersing, add 660 grams of lanthanum carbonate powder (industrial product, Zibo Rongruida powder material factory, 95% by weight) after beating for 30 minutes, add 500 grams of ...

Embodiment 2

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

[0042] Add 3 liters of water in 10 liters of glue tanks, add USY molecular sieve and 640 grams of lanthanum carbonate (same as above) powder after adding the above-mentioned rare earth impregnation and roasting after beating for 15 minutes, add 160 grams of colloidal antimony pentoxide (industrial products, Guangdong Guanghua Science and Technology Co., Ltd. Co., Ltd. production, solid content 30% by weight, average particle diameter 30 nanometers) colloid continued beating for 15 minutes.

[0043] With 250 grams of pseudo-boehmite (industrial product, Al 2 o 3 60% by weight, produced by Chinalco Shandong Aluminum Works) and 600 milliliters of water were stirred...

Embodiment 3

[0045] Get 120 grams of REHY molecular sieves (produced by Catalyst Factory of Nankai University, rare earth oxide 6.0 weight percent, solid content 85 weight percent), and use 8 weight percent of cerium-rich mixed rare earths (industrial products, produced by Inner Mongolia Baotou Rare Earth Factory, wherein CeO 2 50% by weight, La 2 o 3 21% by weight, Pr 2 o 3 14% by weight, Nd 2 o 3 13% by weight) solution 200 ml impregnated and mixed evenly, dried at 110° C. for 2 hours and then calcined at 550° C. for 2 hours.

[0046] Add 2 liters of water in 10 liters of glue tank, add the above-mentioned REHY molecular sieve and 650 grams of lanthanum carbonate powder (same as above) after beating 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 ml of 15% by weight hydrochloric acid (same as above), add to the a...

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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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