Catalyst system for desulfurizing sulfurous hydrocarbons and method for desulfurizing sulfurous hydrocarbons

A catalyst and technology for sulfur-containing hydrocarbons, which are applied to the catalyst system of sulfur-containing hydrocarbon desulfurization and the field of sulfur-containing hydrocarbon desulfurization, can solve the problems of desulfurization activity and desulfurization stability, affect the implementation effect of sulfur-containing hydrocarbon desulfurization, and incomplete reduction of active metals. and other problems, to achieve the effect of improving activity and stability, reducing heap ratio, and promoting isomerization and cracking

Active Publication Date: 2016-11-23
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, in the frequent oxidation regeneration-reduction process, metals as active components will aggregate, and the reduction temperature is limited by the sublimation temperature of zinc oxide, which will also lead to incomplete reduction of active metals, making the adsorption capacity of the adsorbent during recycling The desulfurization activity decreas

Method used

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  • Catalyst system for desulfurizing sulfurous hydrocarbons and method for desulfurizing sulfurous hydrocarbons
  • Catalyst system for desulfurizing sulfurous hydrocarbons and method for desulfurizing sulfurous hydrocarbons
  • Catalyst system for desulfurizing sulfurous hydrocarbons and method for desulfurizing sulfurous hydrocarbons

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Experimental program
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Embodiment approach

[0064] According to a preferred embodiment of the present invention, preferably, as figure 1 As shown, the method of the present invention is carried out in a device for sulfur-containing hydrocarbon desulfurization, which device includes a sulfur-containing hydrocarbon desulfurization reactor 1, an atmosphere replacement and pressure conversion unit, and a regenerator 25; the bottom of the sulfur-containing hydrocarbon desulfurization reactor 1 Sulfur-containing hydrocarbons and hydrogen donor feed pipes 5 and desulfurization aid feed pipes 6 are provided, and the top of the sulfur-containing hydrocarbon desulfurization reactor 1 is provided with an exhaust pipe 12 and a discharge pipe 14; the atmosphere replacement and change The pressure unit is provided with a reactor receiver 15, a reactor feed tank 31, a regenerator receiver 28, a regenerator feed tank 22, a replacement gas inlet pipe (not marked in the figure) and a replacement gas discharge pipe 19, wherein, The atmosp...

Embodiment 1

[0080] This example is used to illustrate the catalyst system and the method for desulfurizing sulfur-containing hydrocarbons of the present invention.

[0081] (1) Catalyst system (the weight ratio of the desulfurization aid to the active component coating of the structured catalyst is 1:1).

[0082] Preparation of structured catalyst: 1.01 kg of Y-type molecular sieve powder (produced by Beijing Chemical Plant, containing 1.0 kg on a dry basis) and 1 kg of deionized water were evenly mixed, wet ball milled into a slurry, and the particle diameter of the mixture was d90=8 microns;

[0083] Add 210 grams of water glass (containing 15% by weight of silicon oxide to the molecular sieve slurry, produced by Sinopec Catalyst Qilu Branch, with a modulus of 3.2, a particle diameter of 1 to 5nm, and an average particle diameter of 3nm), calculated as silicon oxide. Add-on is 25% by weight of Y type molecular sieve weight, stirs 10 minutes, adds polyethylene glycol solution 3.24 grams ...

Embodiment 2

[0095] This example is used to illustrate the catalyst system and the method for desulfurizing sulfur-containing hydrocarbons of the present invention.

[0096] According to the method of Example 1, the difference is that the reduction in (2): use "400°C" and "containing 70% hydrogen by volume" instead of "450°C" and "containing 96% hydrogen by volume"; desulfurization: use " The temperature is 430°C, the pressure is 3.0MPa, and the gasoline weight hourly space velocity is 7h -1 , the volume ratio of hydrogen to gasoline is 100", replacing "the temperature is 400°C, the pressure is 1.4MPa, and the space velocity of gasoline is 5h -1 , the volume ratio of hydrogen to gasoline is 45". The reaction conditions and reaction results are shown in Table 2.

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Abstract

The invention relates to the field of desulfurization, and specifically discloses a catalyst system for desulfurization of sulfur-containing hydrocarbons. The catalyst system is used for a method for desulfurization of sulfur-containing hydrocarbons. The catalyst system includes a desulfurization assistant and a regular structure catalyst; the active component coating of the regular structure catalyst contains 30-90 wt % of a transition metal promoter and 10-70 wt % of a matrix; the matrix contains 70-90 wt % At least one of molecular sieves of BEA structure and FAU structure in % by weight and 10-30% by weight of silica binder; the desulfurization aid contains 5-40% by weight of alumina, 5-40% by weight of silica source and 30-90% by weight of oxides of at least one metal in groups IIB, VB and VIB, the desulfurization aid is microspheres with an average particle size of 20-200 microns; the desulfurization aid and the regular The weight ratio of the active component coating of the structural catalyst is 1-9:1. The catalyst system provided by the invention can have better desulfurization activity and desulfurization stability.

Description

technical field [0001] The invention relates to a catalyst system for desulfurization of sulfur-containing hydrocarbons and a method for desulfurization of sulfur-containing hydrocarbons, in particular to a catalyst system for desulfurization of sulfur-containing hydrocarbons, which is used in the method for desulfurization of sulfur-containing hydrocarbons. Background technique [0002] Sulfur in vehicle fuel produces sulfur oxides after combustion. This substance will inhibit the activity of the precious metal catalyst in the automobile exhaust converter and cause it to be irreversibly poisoned, and cannot realize the catalytic conversion of toxic gases in the automobile exhaust, resulting in the unburned non-methane hydrocarbons and nitrogen in the automobile exhaust. oxides and carbon monoxide. These toxic gases are easily catalyzed by sunlight to form photochemical smog and cause acid rain. And sulfur oxide itself is also one of the main causes of acid rain. [0003]...

Claims

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Application Information

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IPC IPC(8): B01J29/14B01J29/76B01J35/10C10G45/12
Inventor 孙言田辉平王鹏林伟许明德徐志成
Owner CHINA PETROLEUM & CHEM CORP
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