Unlock instant, AI-driven research and patent intelligence for your innovation.

Epoxidation catalyzing method of linear alpha olefins and hydrogen peroxide in parallel-flow-type dripping fixed bed

A hydrogen peroxide and fixed bed technology, applied in chemical instruments and methods, physical/chemical process catalysts, molecular sieve catalysts, etc., can solve environmental pollution, can not meet the problems of environmental protection, easy operation and high selectivity at the same time, and achieve catalyst The effect of long life, easy industrial production, and long online time

Active Publication Date: 2019-04-26
HUBEI UNIV
View PDF9 Cites 2 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] In summary, the above-mentioned published patents have their own deficiencies in terms of process system energy consumption, environmental pollution, catalyst life, material recovery, production efficiency, etc., and cannot At the same time meet the needs of environmental protection, easy operation and high selectivity

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Epoxidation catalyzing method of linear alpha olefins and hydrogen peroxide in parallel-flow-type dripping fixed bed
  • Epoxidation catalyzing method of linear alpha olefins and hydrogen peroxide in parallel-flow-type dripping fixed bed
  • Epoxidation catalyzing method of linear alpha olefins and hydrogen peroxide in parallel-flow-type dripping fixed bed

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0049] The first part: the preparation method of HBMZ molecular sieve catalyst comprises the steps:

[0050] 1) Hydrothermal crystallization

[0051] Mix the metal source, silicon source, organic template agent, complexing agent, mineralizer, and water according to the molar ratio of 0.0067:1.0:1.5:0.02:1.35:25, and use microwave or ultrasonic heating and stirring for 4 hours. The reaction process The medium microwave or ultrasonic power is 500W, and the heating temperature is 80°C; then the reaction mixture is hydrothermally crystallized at 170°C for 84 hours, and finally purified to obtain the crystallized product; the metal source is tin tetrachloride, and the The silicon source is fumed silica, the organic template is piperidine, the complexing agent is triethanolamine, and the mineralizer is boric acid.

[0052] 2) acid treatment

[0053] The HBMZ zeolite molecular sieve raw powder obtained in step 1) and the acidic solution with a molar concentration of 3mol / L are prep...

Embodiment 2

[0063] The first part: the preparation method of HBMZ molecular sieve catalyst comprises the steps:

[0064] 1) Hydrothermal crystallization:

[0065] Mix the metal source, silicon source, organic template agent, complexing agent, mineralizer, and water according to the molar ratio of 0.0375:1.0:1.5:0.1:1.34:40, and use microwave or ultrasonic heating and stirring for 2 hours. During the reaction The microwave or ultrasonic power is 600W, and the heating temperature is 90°C; then the reaction mixture is hydrothermally crystallized at 170°C for 144 hours, and finally purified to obtain the crystallized product; the metal source is dimethyl tin dichloride, The silicon source is silica sol, the organic template is 4-hydroxypiperidine, the complexing agent is diethanolamine, and the mineralizer is potassium chloride.

[0066] 2) acid treatment

[0067] The crystallized product obtained in step 1) and the acidic solution were fully mixed and reacted for 10 hours at a temperature ...

Embodiment 3

[0077] The first part: the preparation method of HBMZ molecular sieve catalyst comprises the steps:

[0078] 1) Hydrothermal crystallization:

[0079] Mix the metal source, silicon source, organic template agent, complexing agent, mineralizer, and water according to the molar ratio of 0.0133:2.0:2.0:0.01:1.0:100, and use microwave or ultrasonic heating and stirring for 1 hour. During the reaction The microwave or ultrasonic power is 1000W, and the heating temperature is 100°C; then the reaction mixture is hydrothermally crystallized at 150°C for 96 hours, and finally purified to obtain the crystallized product; the metal source is sodium metaaluminate, and the The silicon source is silica gel, the organic template is hexamethyleneimine, the complexing agent is triethanolamine, and the mineralizer is sodium borate.

[0080] 2) acid treatment

[0081] The crystallized product obtained in step 1) was fully mixed with the acidic solution at a weight ratio of 1:30 at a temperatur...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

PropertyMeasurementUnit
lengthaaaaaaaaaa
diameteraaaaaaaaaa
lengthaaaaaaaaaa
Login to View More

Abstract

The invention discloses an epoxidation catalyzing method of linear alpha olefins and hydrogen peroxide in a parallel-flow-type dripping fixed bed. The epoxidation catalyzing method comprises the following steps: at the temperature of 20-70 DEG C, mixed liquid of the linear alpha olefins, the hydrogen peroxide and a solvent is introduced from the upper end of the parallel-flow-type dripping fixed bed in a parallel-flow mode; the parallel-flow-type dripping fixed bed is filled with an HBMZ molecular sieve catalyst; the flow-parallelled reaction mixed liquid makes contact with the HBMZ molecularsieve catalyst from top to bottom; a reaction product flows out from the lower end of the parallel-flow-type dripping fixed bed; and then after the reaction product is subjected to low-temperature condensation through a condensation pipe and separated through a gas-liquid separator in sequence, a product, namely epoxide is obtained. According to the epoxidation catalyzing method, the alpha olefins, the hydrogen peroxide and the catalyst can make full contact, the catalytic activity is good, the utilization rate of the hydrogen peroxide is high, selectivity of the epoxy product is good, a process is simple, poisons and harm are avoided, the life of the catalyst is long, the online time is long, selectivity of the product is high, and industrial production is easy.

Description

technical field [0001] The invention relates to the technical field of inorganic chemical synthesis, in particular to a catalytic method for epoxidation of linear olefins and hydrogen peroxide in a co-current trickle-flow fixed bed. Background technique [0002] The epoxidation of olefins not only plays an important role in the production of bulk organic chemical raw materials (such as ethylene oxide, propylene oxide, and epichlorohydrin), but is also widely used in the preparation of various fine chemicals. , organic synthesis, pharmaceuticals, spices and electronics industries, etc., play an important role in the national economy. Olefin epoxidation is one of the most important reactions in the chemical industry. The epoxidation process has been industrialized very early. The chemical reaction is to add atomic oxygen between the carbon atoms at both ends of the double bond of the olefin compound to form a three-membered ring. to obtain epoxy compounds. At present, except...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Applications(China)
IPC IPC(8): C07D301/12C07D303/08C07D303/04C07D303/28C07D303/14B01J29/70B01J35/10
CPCC07D301/12C07D303/04C07D303/08C07D303/14C07D303/28B01J29/70B01J35/60
Inventor 夏清华鲁新环周丹
Owner HUBEI UNIV