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Preparation method of carrier silica gel for olefin catalyst

A technology of olefin catalyst and carrier, which is applied in the field of preparation of carrier silica gel, and can solve the problems of expensive solvent, large solvent consumption, difficult recovery, etc.

Active Publication Date: 2022-01-25
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The azeotropic distillation method has the problems of long time for distilling and removing water, expensive solvents, and high energy consumption; the organic solvent replacement method has the disadvantages of cumbersome operation steps, large solvent consumption, and difficult recovery.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0038]Add 20ml of aqueous ammonia solution with a concentration of 1.5mol / L into the closed reactor, turn on the stirring, and slowly raise the temperature to 50°C. Add 1.1mol / L sodium silicate aqueous solution and 1.15mol / L sulfuric acid aqueous solution concurrently with 4ml / min flow velocity, simultaneously add massfraction with 3ml / min flow velocity and be the ethanol aqueous solution 12ml (ethanol and water) of 6% slurry hydrotalcite The volume ratio is 1:8), when the pH value of the solution in the reactor reaches 11, stop adding the mixed aqueous solution, and react at a constant temperature for 2.0h. Add the n-butanol aqueous solution with a concentration of 1.0mol / L at a flow rate of 6ml / min (the volume ratio of n-butanol to water is 1:15), stop adding the n-butanol aqueous solution when the pH value of the solution is 9, and react at a constant temperature for 2.0h . The temperature of the reaction system was raised to 85° C., and the reaction was carried out at con...

Embodiment 2

[0040] The preparation process was the same as in Example 1, except that 15 ml of ammonium bicarbonate aqueous solution with a concentration of 1.8 mol / L was added into the closed reactor, stirring was turned on, and the temperature was slowly raised to 50° C. Add 1.1 mol / L potassium silicate aqueous solution and 1.15 mol / L sulfuric acid aqueous solution in parallel at a flow rate of 4 ml / min. Other conditions are identical with embodiment 1. The test results are shown in Table 1.

Embodiment 3

[0042] The preparation process is the same as in Example 1, except that 1.1mol / L sodium silicate aqueous solution and 2.2mol / L nitric acid aqueous solution are added in parallel at a flow rate of 4ml / min, and a slurry-like solution with a mass fraction of 6% is added at a flow rate of 3ml / min simultaneously. 12ml of ethanol aqueous solution of hydrotalcite (the volume ratio of ethanol to water is 1:8), when the pH value of the solution in the reaction kettle reaches 11, stop adding the mixed aqueous solution, and react at constant temperature for 2.0h. Add n-butanol nitric acid aqueous solution with a concentration of 2.0mol / L at a flow rate of 6ml / min (the volume ratio of n-butanol and water is 1:15), stop adding n-butanol nitric acid aqueous solution when the pH value of the solution is 9, and react at a constant temperature for 2.0h . The temperature of the reaction system was raised to 85° C., and the reaction was carried out at constant temperature for 5.0 h. Add concent...

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PUM

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Abstract

The invention relates to a method for preparing carrier silica gel for olefin catalysts. The carrier silica gel is made of silicate and inorganic acid as raw materials, and an alkaline medium is used as the base liquid, and silicate and inorganic acid aqueous solution are used to complete silica In the synthesis of sol, the pH value of the reaction solution is adjusted by adding organic alcohol aqueous solution of inorganic acid during gel reaction, and the preparation of silica gel is completed through high temperature hydrothermal reaction. Without affecting the pore volume of silica gel, this process can greatly increase the specific surface area of ​​silica gel, thereby improving the basic physical properties of carrier silica gel; the process is simple to operate, has good repeatability, and low energy consumption, providing technical support for industrial device production. support.

Description

technical field [0001] The invention relates to a preparation method of carrier silica gel, in particular to a preparation method of carrier silica gel for olefin catalysts. Background technique [0002] As a catalyst carrier, silica gel has a suitable pore volume, pore size and distribution, and a high specific surface area can greatly improve the catalyst activity. When the traditional method is used to prepare carrier silica gel, in order to obtain a high specific surface area, the pore volume and pore size are more sacrificed. Therefore, a new method must be adopted to meet the preparation process requirements of catalyst carrier silica gel. [0003] Hydrotalcite is a layered double metal hydroxide, and the laminates are composed of magnesium octahedron and aluminum oxygen octahedron. The specific surface area of ​​uncalcined hydrotalcite is 5-20m 2 / g, the calcined hydrotalcite has a higher specific surface area, and the specific surface area is 200-300m 2 / g, the sp...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J21/08B01J35/10C01B33/143
Inventor 王海王玲玲任峰刘小燕刘文霞张鹏徐人威杨世元陈雪蓉郝萍李忠
Owner PETROCHINA CO LTD