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Active hydrocracking proppant and preparation method thereof

A technology for hydrocracking and hydrogenation activity, applied in chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, etc. It has problems such as catalytic activity and low mechanical strength, and achieves the effect of improving the overall effect, improving the space utilization rate and low price.

Active Publication Date: 2015-04-29
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the above-mentioned new ceramic balls play a certain role in improving the logistics distribution and alleviating the pressure drop of the reactor, because the ceramic balls themselves have no catalytic activity and occupy a limited bed volume, they cannot fundamentally solve the problem of device expansion and product failure. Demand for quality upgrades, especially to improve the overall hydrogenation performance of the reaction system
The hydrocracking catalysts used in the prior art are not suitable for direct use as proppants due to their low mechanical strength, and the high-temperature-treated ceramic balls are difficult to load active components

Method used

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  • Active hydrocracking proppant and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] Amorphous silica-alumina dry rubber powder, macroporous pseudo-boehmite dry rubber powder and nanoscale small-pore pseudo-boehmite dry rubber powder with a mass ratio of 2:1:2 are placed in a roller compactor, and auxiliary Extrusion agent, sage powder, etc., the concentration of adding is 6.0gHNO 3 / 100mL and 10.0g acetic acid / 100mL mixed acid solution for peptization, extruded into a cylindrical shape with a diameter of 3mm, dried at 80°C for 30min, and then cut into balls with a spherical mold, and dried at 120°C for 6 hours to prepare the proppant carrier. Then impregnate the W-Ni solution in a supersaturated manner, separate the solid from the liquid, dry at 120°C for 4 hours, and bake at 500°C for 3 hours to prepare the finished proppant. The number is SP-1.

Embodiment 2

[0036] The preparation method is the same as in Example 1, except that the mass ratio of amorphous silica-alumina dry rubber powder, macroporous pseudo-boehmite dry rubber powder and nanoscale small-pore pseudo-boehmite dry rubber powder is 1:2: 2. Extrude the rod with a diameter of 6 mm to obtain a finished proppant product numbered SP-2.

Embodiment 3

[0038] The preparation method is the same as that in Example 1, except that the dried spherical proppant carrier is subjected to hydrothermal treatment at 600°C and steam pressure of 0.2 MPa for 60 minutes to load hydrogenation active components to obtain the finished proppant product numbered SP-3.

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Abstract

The invention discloses a preparation method of an active hydrocracking proppant. The method comprises the following steps: (1) adopting amorphous silica-alumina, dry glue powder of macroporous pseudoboehmite, and dry glue powder of nanoscale micropore pseudoboehmite as raw materials, molding the raw materials, and drying the molded raw materials so as to obtain a spherical proppant carrier; (2) preparing a metallic salt solution containing active hydrogenation components; (3) enabling the spherical proppant carrier in the step (1) to load the metallic salt solution containing the active hydrogenation components in the step (2), and drying and calcinating the spherical proppant carrier loading the metallic salt solution so as to obtain the active hydrorefining proppant. The proppant has appropriate specific surface area and pore volume, and has high mechanical strength and high hydrocracking performance.

Description

technical field [0001] The invention relates to a hydrocracking active propping agent and a preparation method thereof, in particular to an active propping agent with high mechanical strength and high ring-opening performance for polycyclic hydrocarbons. technical background [0002] In the 21st century, the consumption growth of my country's petrochemical products has exceeded the growth of petroleum products, and large-scale ethylene and large-scale aromatics plants will become the focus of petrochemical development. The refinery produces naphtha in accordance with the principle of "preferable ethylene for ene, suitable fragrance for fragrance, and suitable oil for oil". It is necessary to provide raw materials for ethylene cracking and catalytic reforming to produce high-octane gasoline Blending components and aromatic raw materials. Hydrocracking technology has become the core of the combination of oil-chemical-fiber in refineries due to its strong adaptability to feeds...

Claims

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Application Information

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IPC IPC(8): B01J23/888B01J35/10
Inventor 杜艳泽关明华王凤来
Owner CHINA PETROLEUM & CHEM CORP
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