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Sulfoether oxidation method

A sulfide oxidation and sulfide technology, which is applied in chemical instruments and methods, chemical recycling, organic chemistry, etc., can solve the problems of reducing the catalytic activity of titanium silicon molecular sieve, increasing the operating cost of the device, and fluctuating greatly in the activity of the catalyst. The effect of industrial production application, prolonging the service life of one-way, and prolonging the stable operation time

Active Publication Date: 2016-03-02
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, with the prolongation of the reaction time, the catalytic activity of titanium-silicon molecular sieves will show a downward trend, resulting in a significant decrease in the conversion rate of the oxidant and the selectivity of the target oxidation product.
When the reaction is carried out in a fixed-bed reactor, due to the reduction of the catalytic activity of the titanium-silicon molecular sieve, the titanium-silicon molecular sieve needs to be regenerated inside or outside the reactor, resulting in shutdown of the reactor, thereby affecting production efficiency and increasing the operating cost of the device
[0005] When the regenerated catalyst is put into operation again, especially after being regenerated in the reactor, the activity of the catalyst fluctuates greatly and takes a long time to stabilize, resulting in a decrease in the selectivity of the target oxidation product, which will not only reduce the operation efficiency, and the subsequent separation and purification process is required to adjust the operating conditions, which increases the complexity of the operation; at the same time, it is also necessary to combine operations such as increasing the reaction temperature to achieve a smooth operation of the reaction, but these measures often accelerate catalyst deactivation

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 4、12-15 and 17

[0085]Following examples 4, 12-15 and 17 adopt the following method to measure the activity of catalyst:

[0086] Catalyst, 36% by weight of ammonia water (as NH 3 meter), 30% by weight of hydrogen peroxide (as H 2 o 2 ), tert-butanol and cyclohexanone by mass ratio = 1:7.5:10:7.5:10 and then stirred and reacted at 80°C under atmospheric pressure for 2h, filtered the reactant, and analyzed the obtained liquid phase by gas chromatography The composition of the catalyst is analyzed, and the conversion rate of cyclohexanone is calculated by the following formula and used as the activity of the catalyst,

[0087] The conversion rate (%) of cyclohexanone=[(the molar amount of cyclohexanone added−the molar amount of unreacted cyclohexanone) / the molar amount of cyclohexanone added]×100%.

Embodiment 1

[0090] The catalyst (being a spherical catalyst with a volume particle diameter of 500 μm, the content of titanium-silicon molecular sieve TS-1 in the catalyst is 85% by weight, the content of silicon oxide is 15% by weight, and the density is 0.79g / cm 3 ) is packed in a fixed-bed reactor to form a catalyst bed, wherein the number of the catalyst bed is 1 layer, and the aspect ratio of the catalyst bed is 10.

[0091] Dimethyl sulfide, hydrogen peroxide as an oxidizing agent (provided in the form of hydrogen peroxide, the initial concentration of hydrogen peroxide in hydrogen peroxide is 30% by weight) and acetone as a solvent are mixed to form a liquid mixture, and the liquid mixture is removed from the bottom into a fixed bed reactor and flow through the catalyst bed. Among them, the initial molar ratio of dimethyl sulfide to hydrogen peroxide is 4:1, the molar ratio of dimethyl sulfide to acetone is 1:15, and the weight hourly space velocity of dimethyl sulfide is 2h -1 . ...

Embodiment 2

[0097] Dimethyl sulfide was oxidized by the same method as in Example 1, except that aqueous ammonia (concentration: 25% by weight) was also fed into the fixed-bed reactor to adjust the pH of the liquid mixture to 7.5.

[0098] The reaction was carried out for 620 hours, and the concentration of hydrogen peroxide in the hydrogen peroxide was 55% by weight at the end of the reaction. The results obtained for 0.5 hours and 620 hours of reaction are listed in Table 1.

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Abstract

The invention discloses a sulfoether oxidation method. The method comprises the steps that a liquid mixture is continuously fed into a fixed-bed reactor, and the liquid mixture flows through catalyst bed layers under the oxidation reaction condition to be reacted with titanium silicalite molecular sieves filled in the catalyst bed layers in a contacted mode, wherein the liquid mixture contains sulfoether, at least one oxidizing agent and at least one selectable solvent. The method further comprises the step that when the selectivity of a target oxidation product decreases to a certain degree, the content of the oxidizing agent in the liquid mixture is increased till the selectivity of the target oxidation product is raised to meet the requirement. By means of the sulfoether oxidation method, the selectivity of the target oxidation product can be maintained within a higher range even under the long-periodic continuous operation condition, therefore, the one-way service life of the titanium silicalite molecular sieves serving as a catalyst is effectively prolonged, the regeneration period of the catalyst is shortened, and the stable operation time of a device is prolonged. In addition, the sulfoether oxidation method is simple, easy to carry out and beneficial for industrial production and application.

Description

technical field [0001] The present invention relates to a kind of sulfide oxidation method. Background technique [0002] Sulfoxides are important sulfur-containing compounds. For example, dimethyl sulfoxide (DMSO) is a sulfur-containing organic compound. It is a colorless and transparent liquid at room temperature. properties such as protons. Dimethyl sulfoxide is soluble in water, ethanol, acetone, ether and chloroform, is a highly polar inert solvent, and is widely used as a solvent and reaction reagent. Moreover, dimethyl sulfoxide has a high selective extraction ability and can be used as an extraction solvent for the separation of alkanes and aromatics. For example: dimethyl sulfoxide can be used for the extraction of aromatics or butadiene. In the polymerization reaction, it is used as a processing solvent and spinning solvent, as a synthetic solvent and spinning solvent of polyurethane, and as a synthetic solvent of polyamide, fluorochloroaniline, polyimide and pol...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C315/02C07C317/04C07C317/14
CPCY02P20/582Y02P20/584
Inventor 史春风林民朱斌
Owner CHINA PETROLEUM & CHEM CORP
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