Diesel oil hydrofining catalyst containing phosphorous or molecular sieve and preparation method thereof
A hydrorefining and catalyst technology, which is applied in the fields of refined hydrocarbon oil and petroleum industry, can solve the problems of increased diesel consumption and the inability to meet the requirements of deep refining of diesel oil, and achieve the effect of deep removal and improved catalytic efficiency
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Embodiment 1
[0039] Preparation of TiO by Sol-Gel Method 2 -SiO 2 Composite oxide carrier CTS
[0040] Dissolve 34.0g of tetrabutyl titanate and 20.8g of tetrabutyl titanate and 20.8g of tetraethyl orthosilicate in ethanol and mix uniformly to obtain solution A; mix 19ml of water, 41.2ml of acetic acid and 40ml of absolute ethanol to obtain solution B. Under strong magnetic stirring, drop solution B into A for reaction; after a certain period of reaction, a sol is obtained, and the sol is aged under natural conditions for a certain period of time to obtain a gel; the gel is dried by supercritical carbon dioxide fluid , the drying conditions are temperature 40-60°C, pressure 8.0-12.0MPa, time 2 hours, and then roasting at 500-600°C for 3-4 hours to obtain a white powder; put the obtained white powder in a muffle furnace at Calcined at 500-600°C for 3 hours, pressed into tablets, and ground to take particles with a particle size of 3-3.6 mm as the carrier for preparing the catalys...
Embodiment 2
[0043] Modification of CTS Carrier by Impregnating Phosphorous Solution
[0044] Under constant temperature conditions in a water bath of 60°C, the CTS carrier of Example 1 was mixed with an equal volume (NH 4 ) 2 HPO 4 Mix and impregnate in the solution for 2h, then dry at 120°C for 4h, and bake at 550°C for 2h, prepare different concentrations of (NH 4 ) 2 HPO 4 (or ammonium phosphate) impregnating solution, the modified CTS carrier (expressed as P-CTS) with a P loading amount of 1-4% (mass content, the same below) can be prepared. The specific surface area and pore volume data of the obtained carrier determined by the BET method are listed in Table 1.
[0045] carrier
Embodiment 3
[0047] Preparation of Phosphorus-Containing CTS Carrier Using Phosphoric Acid as Hydrolysis pH Regulator
[0048] Prepare TiO with sol-gel method in embodiment 1 2 -SiO 2 In the CTS process of the composite oxide carrier, phosphoric acid is used instead of part or all of acetic acid as the hydrolysis pH regulator. The amount of phosphoric acid added depends on the phosphorus content in the CTS carrier. Other preparation conditions are the same as in Example 1 to obtain a phosphorus-containing CTS carrier. (Denoted by CTS+P). The specific surface area and pore volume data of the obtained carrier determined by the BET method are shown in Table 2.
[0049] carrier
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