Catalyst system for desulfurization of sulfur-containing hydrocarbons and method for desulfurization of sulfur-containing hydrocarbons
A technology for catalysts and sulfur-containing hydrocarbons, applied in chemical instruments and methods, catalyst protection, molecular sieve catalysts, etc., can solve the problems of desulfurization activity and desulfurization stability, affect the effect of desulfurization of sulfur-containing hydrocarbons, and incomplete reduction of active metals, etc. problem, achieve the effect of improving activity and stability, reducing heap ratio, 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 SAPO-11 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 SAPO-11 weight, stirred for 10 minutes, added polyethylene glycol solution 3.24 grams (the weight percent of ...
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℃, 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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