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

Inactive Publication Date: 2007-10-24
CHINA UNIV OF PETROLEUM (BEIJING)
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the catalyst is still insufficient in terms of deep desulfurization and denitrification. Facing the current situation of increasing diesel consumption and stricter restrictions on vehicle emissions, it is necessary to further improve and improve
[0008] To sum up, when the existing catalysts supported by alumina or titania, silica, or modified alumina are used for hydrogenation of diesel fuel, it is difficult to have good hydrodesulfurization, denitrification and denitrification at the same time. The properties of aromatics, whether it is a single-component carrier or a composite-component carrier catalyst, cannot meet the requirements for the deep refining of diesel oil. Therefore, the continuous development of new diesel hydrotreating catalysts is the direction of the industry's efforts

Method used

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Examples

Experimental program
Comparison scheme
Effect test

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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PUM

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Abstract

The invention relates to a diesel hydrofining accelerant, wherein a carrier is a modifying product that the titania and the silicon dioxde composite oxides is modified by P, HY molecular sieve or the molecular sieve modifying material; a active component is two metals of cobalt, molybdenum, nickel, tungsten; the hole volume of the accelerant is 0. 4-0. 7ml/g, and the specific surface area of the accelerant is 150-350m2/g. The invention also relates to a method preparing for the accelerant, which specially relates to the method modifying the property with phosphorus or the molecular sieve, in order to achieve the deep desulfuration, the denitrification and denying aromatic hydrocarbons of the diesel.

Description

technical field [0001] The invention relates to a catalyst for diesel hydrofinishing, in particular to a diesel hydrofinishing catalyst obtained by modifying a titanium dioxide and silicon dioxide composite oxide carrier and a preparation method thereof. Background technique [0002] With the increasing requirements for environmental protection, the restrictions on vehicle emissions have become more stringent, and the content control indicators of sulfur, nitrogen, aromatics and other harmful substances in clean diesel specifications have also been continuously improved. Hydrogenation is the most effective means to achieve diesel desulfurization, denitrogenation and dearomatization. The performance of the catalyst used in the hydrogenation process plays a key role in the technical level of the hydrogenation process. An ideal diesel hydrogenation catalyst should have high catalytic desulfurization, denitrogenation and aromatics saturation activities, so that the hydrogenation...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G45/12
Inventor 周亚松魏强马海峰张宗辉
Owner CHINA UNIV OF PETROLEUM (BEIJING)
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