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
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[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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