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 clogging and decrease of specific surface area, and improve the dispersion and vulcanization performance.

Active Publication Date: 2008-04-09
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,

Method used

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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 ethyl orthosilicate into solution A, and stir and disperse 3g of HY molecular sieve in solution A, uniformly Mix to obtain solution B; mix 19 ml of water, 41.2 ml of acetic acid and 40 ml 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 under natural conditions for a certain period of time to obtain a gel; the gel drying and calcination conditions are the same as those in Example 1, and a carrier material B-containing NiO 1% is obtained- 1. The specific surface area, pore volume and pore diameter of the sample were measured by BET method, respectively SBET=321m2·g-1, V=0.72ml·g-1, D=9.0nm.

Embodiment 4

[0044] Dissolve 109.2g of tetrabutyl titanate and 16.8g of ethyl orthosilicate in 72ml of ethanol respectively to obtain solution A; stir and disperse 3g of HY molecular sieve in solution A to obtain solution B; dissolve 2g of nickel nitrate into Green solution C was obtained in 40 ml of ethanol; solution D was obtained by mixing 19 ml of water and 41.2 ml of acetic acid with solution C. The solution D is dropped into A and stirred for 10 to 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 gel drying and roasting conditions are the same as those 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 were measured by BET method: SBET=328m2·g-1, V=0.73ml·g-1, D=8.9nm.

Embodiment 5

[0046] The quality of the nickel nitrate in Example 2 was changed to 4g, and the remaining steps and preparation conditions were unchanged to obtain a carrier B-2 containing NiO 2%, and the specific surface area and pore volume of the carrier material were measured by the method of BET, The pore diameters 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 O 3, SiO 2, TiO 2, and a composite oxide of two of the Al 2 O 3, the SiO 2, and the TiO 2 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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IPC IPC(8): B01J32/00B01J23/88B01J29/10C10G45/04
Inventor 周亚松魏强温世昌郭栋
Owner BC P INC CHINA NAT PETROLEUM CORP
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