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A kind of propylene epoxidation reaction method

A technology of propylene and propylene oxide, applied in the field of preparation of known compounds, can solve the problems of interphase backmixing and particle loss in a fluidized bed, high pressure drop in a fixed bed, affecting reaction performance, etc. Effects of reduced lamination and high mass transfer efficiency

Active Publication Date: 2020-02-11
CHINA CATALYST HLDG CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The purpose of the present invention is to solve the problem that the pressure drop of the fixed bed is too high in the current propylene epoxidation reaction, channeling and local overheating affect the reaction performance, and also solve the problem that the fluidized bed interphase back-mixing and particle loss cause the catalytic performance to decline. , developed a new process combining a magnetically stabilized bed and a composite magnetic Ti-MWW molecular sieve catalyst, which improved the activity of propylene conversion and the selectivity of products

Method used

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  • A kind of propylene epoxidation reaction method
  • A kind of propylene epoxidation reaction method
  • A kind of propylene epoxidation reaction method

Examples

Experimental program
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Effect test

Embodiment 1

[0046] This example illustrates the preparation method of composite magnetic Ti-MWW molecular sieve catalyst microspheres

[0047] (1) Superparamagnetic NiFe 2 o 4 The material powder is mixed with silica sol (30wt%), kale powder and deionized water in a mass ratio of 1:20:0.02 to form a 35wt% slurry, and then prepared into 50-70 micron SiO 2 Coated NiFe 2 o 4 Magnetic microspheres NiFe 2 o 4 @SiO 2 , and then baked at 500°C for 6h for later use.

[0048] (2) Tetrabutyl titanate (TBOT) was added dropwise to 35% concentration of H at a mass ratio of 1:2 at room temperature 2 o 2 solution, while stirring for 1 hour, a yellow clear Ti solution was obtained. Boric acid is mixed with the above-mentioned Ti solution under stirring, and the NiFe obtained in (1) is added 2 o 4 @SiO 2 Add magnetic microspheres as silicon source and piperidine (PI) to the above mixed solution, stir and mix evenly to obtain the following raw material molar ratio of the mixture slurry: SiO 2 ...

Embodiment 2~4

[0051] This example illustrates the preparation method of composite magnetic Ti-MWW molecular sieve catalyst microspheres

[0052] Examples The catalyst preparation process is the same as in Example 1, except that there are differences in the selection of superparamagnetic materials, and the molar composition of the template agent and crystallization precursor solution used in the synthesis is also different, as shown in Table 1. Show.

[0053] Table 1

[0054]

Embodiment 5~9

[0056] These examples illustrate that using different magnetic composite Ti-MWW molecular sieve catalysts, the processes provided by the present invention all have good propylene epoxidation reaction effects. For comparison, the VS-1 catalyst prepared in Comparative Example 1 was tested in the absence of a magnetic field, and the results are shown in Table 2.

[0057] In the test, 100 mg of different catalysts with a particle size of 50-70 microns were loaded into a reactor with an inner diameter of 16 mm and a height of 300 mm; four inner diameters were 60 mm, outer diameters were 165 mm, heights were 50 mm, and the number of turns 390 coils are arranged axially along the reactor to provide a uniform magnetic field, and the distance between the coils is 25 millimeters; the concentration is 30.0wt% H 2 o 2 The solution and the acetonitrile solvent are mixed and input into the preheater, wherein the concentration in the acetonitrile mixed solution is 65wt%, and mixed with the ...

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Abstract

The invention discloses a propylene epoxidation reaction method. The method is characterized in that a mixture of propylene, a solvent and H2O2 and a magnetic Ti-MWW molecular sieve based catalyst aresubject to contact reaction through a magnetically-stabilized-bed reactor; the reaction is performed under the conditions that the temperature is 25-100 DEG C, the pressure is 0.1-10.0MPa, the weightspace velocity of propylene is 0.1-15h<-1>, the magnetic field intensity is 100-1000 Oe, and propylene is converted into epoxypropane in the reaction. The yield and the selectivity of epoxypropane inthe reaction are respectively beyond 92% and 98%; the conversion rate and the utilization rate of H2O2 are respectively beyond 98% and 93%; the product quality is improved; the reaction efficiency isimproved; moreover, the separation and purification cost is decreased. Compared with a fluidized bed technical method, the propylene epoxidation reaction method has the advantages that bubbles are crushed through a magnetic field, so that the transfer efficiency is high, little catalyst is taken away, and thus the energy consumption is reduced, the environmental pollution is reduced, and the device processing capacity is improved.

Description

technical field [0001] The invention belongs to the preparation method of known compounds, and in particular relates to a method for preparing propylene oxide by catalyzing the epoxidation reaction of propylene with a composite magnetic Ti-MWW molecular sieve in a magnetically stabilized bed. Background technique [0002] Propylene oxide (PO) is an important bulk chemical raw material. Because it has a highly tensioned oxygen-containing three-membered ring, its chemical properties are very active and it has a wide range of uses. It is mainly used for the production of polyether, further production of polyurethane plastics, foam stabilization Agent, paper industry defoamer, crude oil demulsifier, oil well acid treatment wetting agent and high-efficiency low-foam detergent, etc. Propylene oxide is also used to produce propylene glycol, and then to produce unsaturated polyester resin, etc. With the expansion of the use of propylene oxide and the continuous growth of the use of...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07D301/12C07D303/04
CPCC07D301/12C07D303/04
Inventor 王志光李进王炳春王建青
Owner CHINA CATALYST HLDG CO LTD