Dispersion method of suspension bed hydrogenation catalyst

A hydrogenation catalyst and catalyst technology, applied in the direction of hydrocarbon oil treatment control/regulation, treatment with moving solid particles, etc., can solve the large burden of steam stripping and demulsification, poor performance, easy aggregation and dispersing effect of larger droplets, etc. problem, to achieve the effect of good dispersion and simple foaming process

Inactive Publication Date: 2018-01-23
SINOPEC YANGZI PETROCHEM +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The above-mentioned suspended bed hydrogenation catalyst and its dispersion method in heavy oil have the following problems: the specific surface area of ​​the aqueous solution is small, and it is easy to aggregate and form larger droplets in the immiscible residual oil system, which is the fundamental factor for the poor dispersion effect ; The water content of the catalyst raw material aqueous solution is relatively high, which will cause a large burden on the subsequent stripping and demulsification

Method used

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  • Dispersion method of suspension bed hydrogenation catalyst
  • Dispersion method of suspension bed hydrogenation catalyst
  • Dispersion method of suspension bed hydrogenation catalyst

Examples

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Embodiment 1

[0028] The suspended bed hydrogenation catalyst is composed of a water-soluble catalyst nickel sulfate solution and an oil-soluble catalyst iron naphthenate, the weight ratio of the water-soluble catalyst and the oil-soluble catalyst is 9:1, and the water-soluble catalyst is added into the water-soluble catalyst solution. Solution 2wt% foaming agent SDS, to obtain mixed solution A; Mixed solution A is placed under a high-speed mixer and stirred to make the foam rich, the speed of the high-speed mixer is 5000r / min, and the stirring time is 600 seconds to obtain a foam system; The soluble catalyst iron naphthenate is dissolved in 1wt% CTAB solution to obtain a mixed solution B. In the mixed solution B, the concentration of iron naphthenate is 5 wt%; the mixed solution B is added dropwise to the foam system to make it account for both 10% of the total volume, continue stirring after the dropwise addition to obtain a colloidal liquid foam. The colloidal liquid foam is added to the...

Embodiment 2

[0030] The suspended bed hydrogenation catalyst is composed of a water-soluble catalyst nickel sulfate solution and an oil-soluble catalyst molybdenum naphthenate. The weight ratio of the water-soluble catalyst to the oil-soluble catalyst is 4:1. The foaming agent SDBS of solution 1wt% is obtained mixed solution A; Mixed solution A is placed under the stirring of high-speed mixer, makes foam abundant, and rotating speed is 6000r / min, and stirring time is 700 seconds, obtains foam system; Oil-soluble catalyst ring Molybdenum alkanoate is dissolved in the Tween 80 solution of 1.5wt%, obtains mixed solution B, and in mixed solution B, the concentration of molybdenum naphthenate is 7.5wt%; In foam system, drop mixed solution B, make it account for two 20% of the total volume, continue to stir after the dropwise addition, to obtain a colloidal liquid foam. The colloidal liquid foam is added to the heavy oil raw material Venezuelan slag and stirred, and the resulting mixture enters ...

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Abstract

The invention relates to a dispersion method of a suspension bed hydrogenation catalyst, wherein the suspension bed hydrogenation catalyst is formed by a water-soluble catalyst and an oil-soluble catalyst. The dispersion method includes: adding a foaming agent to the water-soluble catalyst, and placing an obtained solution in a high-speed stirrer for stirring to enrich foam to obtain a foaming system; dissolving the oil-soluble catalyst in a surfactant solution prior to dropwise dropping into the foaming system to obtain CLA (colloidal liquid aphron); adding the obtained CLA into heavy-oil material for stirring to allow a mixture to enter a reaction system via stream stripping. The method is simple in foaming process, subsequent stripping dehydration process load can be reduced by reducingdispersion system moisture content through enrichment of catalytic active components by the foam, catalyst granules can be evenly and finely dispersed in raw oil, and the dispersion effect is betterthan that of a traditional mode.

Description

technical field [0001] The invention relates to a dispersion method, in particular to a dispersion method of a suspension bed hydrogenation catalyst, and the method is especially suitable for the suspension bed hydrogenation catalyst dispersion process. Background technique [0002] Suspension-bed hydrogenation catalysts currently used are divided into two categories: oil-soluble catalysts and water-soluble catalysts. Oil-soluble catalysts are easy to disperse and have high hydrogenation activity, but are expensive and have poor coke loading performance. The water-soluble catalyst is cheap and requires a large amount of input, so the coke loading performance is also better than that of the oil-soluble catalyst, but it is difficult to disperse because it is not easily miscible with residual oil. Studies have shown that the combination of the two catalysts has a synergistic effect. The dispersion of catalyst in raw oil is one of the key steps in the suspension bed hydrogenat...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G49/12C10G49/26
Inventor 廉勇沐宝泉
Owner SINOPEC YANGZI PETROCHEM
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