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Production method of butylene oxide

A technology for the production of butylene oxide, which is applied in the direction of organic chemistry, can solve the problems of strong corrosion of equipment, pollution, large amount of waste water and waste residue, etc., and achieve the effects of high catalyst activity, good technical effect and high product selectivity

Active Publication Date: 2018-06-08
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The technical problem to be solved by the present invention is that the existing technology has the problems of large amount of waste water and waste residue, serious pollution, and strong corrosion of equipment, and provides a production method of butylene oxide

Method used

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  • Production method of butylene oxide
  • Production method of butylene oxide

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] At room temperature and under stirring, 150g of hexadecylamine was added to the solution containing 800ml of H 2 O and 600ml of ethanol in a mixed solution, stirred until the solution was one phase. Add 650 g of ethyl orthosilicate dissolved in 300 ml of ethanol to the above mixed solution, stir for 30 min and then crystallize for 24 h. The resulting solid was then filtered and washed with water. The washed material was dried at 110°C for 12 hours, and then calcined at 550°C for 4 hours to obtain a powder carrier with HMS structure characteristics. Using silica sol as a binder, a HMS molding carrier with a HMS weight percentage of 90% was prepared by using traditional extrusion molding technology.

[0038] Configuration contains 40gTiCl 4 500ml of cumene solution, the above-mentioned prepared catalyst shaped carrier is added to TiCl 4 In the cumene solution, under slow stirring and reflux, the temperature was raised to 150°C, and the reaction was carried out at this...

Embodiment 2

[0042] According to the method of [Example 1], an HMS shaped carrier with a HMS weight percentage of 90% was prepared. Take 100 grams of the shaped carrier prepared above and fill it into a quartz tube reactor, and heat it at 120° C. for 2 hours under dry air conditions. Raise the bed temperature to 200°C, under normal pressure, continuously feed TiCl 4 Dry air at 5.0% by volume for 6 hours. At this temperature and pressure, switch to air purge until the reactor outlet is TiCl-free 4 Check out. Then pass air with a water vapor volume content of 1.0% for 5 hours, and then switch to air to purge the residual water vapor in the system. Dry air with a hexamethyldisilazane volume content of 10.0% was continued for 6 hours. At this temperature and pressure, switch to nitrogen purge until no hexamethyldisilazane is detected at the outlet of the reactor, that is, a titanium-containing porous silica catalyst Ti- HMS.

[0043] The elemental analysis results showed that the weight ...

Embodiment 3

[0045] Add 150 g of fumed silica into 240 g of 25 wt % tetramethylammonium hydroxide aqueous solution, and continue stirring for 30 min to form a solution. Then, the above solution was added to 600 ml of aqueous solution containing 230 g of cetyltrimethylammonium bromide under stirring to form a transparent solution. The above mixed solution was transferred into a stainless steel autoclave lined with polytetrafluoroethylene at 100°C for static crystallization for 3 days. The crystallized product is washed and filtered, dried at 100°C for 24 hours, and calcined at 550°C for 6 hours to obtain a powder carrier with the structural characteristics of MCM-41. The MCM-41 molding carrier with the MCM-41 weight percentage of 90% is prepared by using silica sol as a binder and adopting traditional extrusion molding technology.

[0046] According to the method of [Example 2], the assembly of the active species titanium and the surface hydrocarbyl graft silanization treatment are carried...

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Abstract

The invention relates to a production method of butylene oxide, which mainly solves the problems of large amount of waste water and waste residue, serious pollution and strong corrosion of equipment in the prior art. The present invention uses butene and organic peroxide as raw materials, the reaction temperature is 25-200°C, the absolute reaction pressure is 0.1-8.0MPa, the molar ratio of butene to organic peroxide is 1-15, the organic peroxide The oxide concentration is 0.5 to 90% by weight, and the organic peroxide weight space velocity is 0.01 to 20 hours-1, and the technical scheme of obtaining butylene oxide through the contact reaction of the raw material and the titanium-containing porous silica catalyst is better solved Solved this problem and can be used in the industrial production of butylene oxide.

Description

technical field [0001] The present invention relates to a kind of production method of butylene oxide Background technique [0002] Polyether polyol, referred to as polyether, is a new type of synthetic lubricant base oil researched and developed in the late 1970s and early 1980s. There are many types of them, mainly distinguished by monomers. The monomers for the synthesis of polyethers have been developed to include ethylene oxide, propylene oxide, butylene oxide and tetrahydrofuran. In addition to being used as the base oil of new synthetic lubricants, polyether is also an important raw material for the production of polyurethane, and has multiple functions such as defoaming, demulsification, dispersion, penetration, and emulsification. Due to the limitation of butylene oxide production technology, our common polyethers are mainly polyether polyols synthesized from ethylene oxide or propylene oxide as monomer raw materials, and polyether polyols synthesized from butylene...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07D301/12C07D303/04
Inventor 金国杰康陈军高焕新杨洪云黄政丁琳
Owner CHINA PETROLEUM & CHEM CORP