Hydrogenation catalysts carrier with nickel and cobalt, hydro-catalyst and its preparing method

A hydrogenation catalyst and catalyst technology, which are applied to catalyst carriers, molecular sieve catalysts, chemical instruments and methods, etc., can solve the problem of reducing the specific surface area and pore volume of the catalyst, failing to give full play to the effect of titanium oxide, and having a low-activity nickel-aluminum spinel structure. and other problems, to avoid the decrease of specific surface area, avoid blockage and decrease of specific surface area, and improve the dispersion and vulcanization performance.

Active Publication Date: 2011-07-13
BC P INC CHINA NAT PETROLEUM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, due to the inevitable interaction of alumina and nickel atoms in the preparation process of the catalyst, a low-activity nickel-aluminum spinel structure is formed, which is not conducive to the full play of the hydrogenation activity of the metal active component on the catalyst; and because The introduction method of titanium element causes the content of titanium oxide in the catalyst to not be very high, and cannot give full play to the role of titanium oxide in the hydrogenation catalyst
[0008] The common feature of the above-mentioned catalyst preparation methods is the introduction of inactive metal components in the carrier or catalyst. The corresponding problem brought by this type of preparation method is to increase the amount of metal components or reduce the specific surface area and pore volume of the catalyst.

Method used

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  • Hydrogenation catalysts carrier with nickel and cobalt, hydro-catalyst and its preparing method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 3

[0042] Dissolve 2g of nickel nitrate in 72ml of ethanol to obtain solution A; add 109.2g of tetrabutyl titanate and 16.8g of tetraethyl orthosilicate to solution A, and stir and disperse 3g of HY molecular sieves in solution A, evenly Mix to obtain solution B; mix 19ml of water, 41.2ml of acetic acid and 40ml of absolute ethanol to obtain solution C. Add solution C dropwise to B and stir for 10 to 30 minutes to obtain a sol, and the sol is aged for a certain period of time under natural conditions to obtain a gel; the gel drying and roasting conditions are the same as in Example 1, and a carrier material B containing 1% NiO is obtained. 1. The specific surface area, pore volume and pore diameter of the sample measured by BET method are SBET=321m2·g-1, V=0.72ml·g-1, D=9.0nm respectively.

Embodiment 4

[0044] 109.2g of tetrabutyl titanate and 16.8g of tetrabutyl titanate and 16.8g of ethyl orthosilicate were respectively dissolved in 72ml of ethanol to obtain solution A; 3g of HY molecular sieves were stirred and dispersed in solution A to obtain solution B; 2g of nickel nitrate was dissolved in Green solution C was obtained in 40ml of ethanol; solution D was obtained by mixing 19ml of water and 41.2ml of acetic acid with solution C. Put solution D dropwise into A and stir for 10-30 minutes to obtain a sol, and the sol is aged under natural conditions for a certain period of time to obtain a gel; the drying and roasting conditions of the gel are the same as in Example 1, and a carrier material C containing 1% NiO is obtained -1, the specific surface area, pore volume, and pore diameter of the sample measured by the BET method are: SBET=328m2·g-1, V=0.73ml·g-1, D=8.9nm.

Embodiment 5

[0046] Change the quality of the nickel nitrate in embodiment 2 into 4g, all the other steps and preparation conditions are constant, make the carrier B-2 that contains NiO 2%, adopt the method for BET to record the specific surface area and pore volume of this carrier material, The pore sizes are: SBET=321m2·g-1, V=0.71ml·g-1, D=8.5nm.

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Abstract

The invention provides a carrier of pre-impregnating metal components, and hydrotreating catalyst containing the carrier, wherein carrier materials are Al 2 O3, SiO 2, TiO2, and a composite oxide of two of the Al2 O3, the SiO2, and the TiO2 which are prepared by a sol-gel method, a certain amount of molecular sieve is added into the carrier, saline solution containing nickel and cobalt is inducted in the process of the carrier materials prepared by a sol method, in order that the content of NiO and CoO in the carrier is 0.1 to 5 wt percent, the specific surface area of the obtained carrier containing the nickel or the cobalt is in 250 to 400 m <2> * g <-1>, and the pore volume is in 0.5 to 1.0 ml * g <-1>. The invention also provides a preparation method for the catalyst, group 6B metals and group 8 metals are taken as active components, the adoption of an equivalent-volumetric impregnation method produces the petroleum fraction hydrotreating catalyst, and the catalyst of the invention has excellent activity of hydrogen desulfurization and hydrodenitrification.

Description

technical field [0001] The invention provides a hydrogenation catalyst carrier in which nickel or cobalt is pre-impregnated, a catalyst containing the pre-impregnated nickel or cobalt carrier and a preparation method thereof. Specifically, in the process of sol-gel preparation of the support, a part of the metal active component nickel or cobalt of the catalyst is introduced into the support preparation system to form a new type of pre-impregnated nickel or cobalt support, which changes the The existence state of the metal component nickel or cobalt in the carrier improves the interaction between the carrier and other metal components, improves the dispersibility and vulcanization performance of the metal component, and thus produces the pre-impregnated nickel or cobalt. The hydrogenation catalyst of the carrier, the hydrogenation catalyst of the present invention has very good hydrodesulfurization and hydrodenitrogenation properties for petroleum fractions. Background techn...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/88B01J32/00B01J29/10C10G45/04
Inventor 周亚松魏强温世昌郭栋
Owner BC P INC CHINA NAT PETROLEUM CORP
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