Hydrofining catalyst, preparation method and application thereof, and hydrofining method of distillate oil
A technology for hydrorefining and catalyst, applied in catalyst activation/preparation, refined hydrocarbon oil, catalyst carrier, etc., can solve the problems of small pore size, low activity, high catalytic activity, and achieve the goal of reducing emissions, short process and realizing green manufacturing. Effect
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment approach
[0034] The inventors of the present invention found in research that introducing a carboxylic acid compound into a hydrorefining catalyst can improve the activity of the catalyst. Therefore, as long as the carboxylic acid is introduced into the catalyst, the effect of protecting the active components of the catalyst and improving the activity of the catalyst can be achieved, and there is no particular limitation on the added amount. According to a preferred embodiment of the present invention, based on the dry weight of the inorganic refractory component, the content of the carboxylic acid is 3-40 wt%, preferably 10-30 wt%.
[0035] Preferably, the carboxylic acid is selected from C1-18 monobasic saturated carboxylic acids (for example, C1, C2, C3, C4, C5, C6, C7, C8, C9, C10, C11, C12, C13, C14, C15 , C16, C17, C18 monobasic saturated carboxylic acids) (such as but not limited to formic acid, acetic acid, propionic acid, caprylic acid, pentanoic acid, caproic acid, capric aci...
Embodiment 1
[0079] This embodiment is used to illustrate the hydrorefining catalyst provided by the present invention and its preparation method
[0080] (1) Pseudo-boehmite (Pseudo-boehmite powder produced by Changling Catalyst Factory, with a specific surface area of 320m 2 / g, the average pore diameter is 13nm, the pore volume with a pore diameter of 2-4nm accounts for 10% of the total pore volume, and the pore volume with a pore diameter of 4-40nm accounts for 78% of the total pore volume), amorphous silica-alumina powder (SiO 2 content of 10% by weight), magnesium hydroxide powder mixed evenly, and then roasted at 500 ° C for 8 hours to obtain an inorganic refractory component.
[0081] Wherein, based on the dry basis weight of the inorganic refractory component, the content of magnesium oxide is 2.5% by weight, the content of amorphous silicon aluminum is 15% by weight, and the content of aluminum oxide is 82.5% by weight.
[0082] (2) A certain amount of MoO 3 Add basic cobalt...
Embodiment 2
[0089] This embodiment is used to illustrate the hydrorefining catalyst provided by the present invention and its preparation method
[0090] (1) Pseudo-boehmite (Pseudo-boehmite powder produced by Changling Catalyst Factory, with a specific surface area of 320m 2 / g, the average pore diameter is 13nm, the pore volume with a pore diameter of 2-4nm accounts for 10% of the total pore volume, and the pore volume with a pore diameter of 4-40nm accounts for 78% of the total pore volume), amorphous silica-alumina powder (SiO 2 content of 15% by weight), calcium hydroxide powder mixed evenly, and then roasted at 600 ° C for 5 hours to obtain an inorganic refractory component.
[0091] Wherein, based on the dry weight of the inorganic refractory component, the content of calcium oxide is 3.0% by weight, the content of amorphous silicon aluminum is 20.0% by weight, and the content of aluminum oxide is 77.0% by weight.
[0092] (2) A certain amount of MoO 3 , basic nickel carbonate...
PUM
| Property | Measurement | Unit |
|---|---|---|
| pore size | aaaaa | aaaaa |
| pore size | aaaaa | aaaaa |
| specific surface area | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More