A kind of coal tar hydrodenitrogenation catalyst and its application

A hydrodenitrogenation and catalyst technology, which is applied in the field of medium and low temperature coal tar hydrodenitrogenation treatment and medium and low temperature coal tar hydrodenitrogenation catalyst, can solve the problem of short reaction time, no obvious stability, unsuitable continuous treatment, etc. problem, to achieve the effect of enhanced adsorption capacity, enhanced carrier strength, increased loading of auxiliary agents

Inactive Publication Date: 2014-10-22
NORTHWEST UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At 360°C, hydrogen pressure 6.0MPa, hydrogen oil volume ratio 500:1, space velocity 1.5h -1 When dealing with catalytic cracking (FCC) gasoline under operating conditions, the desulfurization and denitrification are ideal, but the reaction time is short and the stability is not obvious, so it is not suitable for long-term continuous treatment of medium and low temperature coal tar with extremely high nitrogen content

Method used

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  • A kind of coal tar hydrodenitrogenation catalyst and its application
  • A kind of coal tar hydrodenitrogenation catalyst and its application
  • A kind of coal tar hydrodenitrogenation catalyst and its application

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0022] Example 1 Weigh a certain amount of γ-Al 2 o 3 Dry rubber powder (85%, Wt) and α-Al 2 o 3 ·(1~3)H 2 Two carbon blacks (9%, Wt) of NEROX 505 and FW 200 are mixed into the dry rubber powder (6%, Wt) as a pore-expanding agent, and the mass ratio M (NEROX 505):M (FW 200) =7:3, Mix with dilute nitric acid (1.5%, Wt), knead into a clover shape, and roast at 660°C for 4.5h to obtain the catalyst γ-Al 2 o 3 carrier. The catalyst carrier was soaked in deionized water for 3.6h, dried at 80°C, and then washed with Ni(NO 3 ) 2 ·6H 2 O (6%, Wt), (NH 4 ) 6 h 2 W 24 ·6H 2 The catalyst support was impregnated with O (16%, Wt) co-impregnation method for 6 hours, dried at 100°C for 6 hours, and calcined at 700°C for 4 hours to obtain the hydrodenitrogenation catalyst. The catalyst obtained in the above steps was impregnated with phosphoric acid (4.25%, Wt) solution in the same impregnation method, dried at 110 °C for 4 h, and calcined at 550 °C for 3 h to obtain a hydroden...

Embodiment 2

[0023] Example 2 Weigh a certain amount of γ-Al 2 o 3 Dry rubber powder (83%, Wt) and α-Al 2 o 3 ·(1~3)H 2 Two carbon blacks (9%, Wt) of NEROX 505 and FW 200 are mixed into the dry rubber powder (8%, Wt) as a pore-expanding agent, and the mass ratio M (NEROX 505): M (FW 200) = 3: 2, Mix with dilute nitric acid (1.5%, Wt), knead into a clover shape, and roast at 660°C for 4.5h to obtain the catalyst γ-Al 2 o 3 carrier. Soak the catalyst carrier in deionized water for 3 h, dry it at 80 °C, and use Ni(NO 3 ) 2 ·6H 2 O (10%, Wt), (NH 4 ) 6 h 2 W 24 ·6H 2 The catalyst support was impregnated with O (20%, Wt) co-impregnation method for 6 h, dried at 100 °C for 6 h, and calcined at 700 °C for 4 h to obtain the hydrodenitrogenation catalyst. The catalyst obtained in the above steps was impregnated with phosphoric acid (4%, Wt) solution in the same impregnation method, dried at 110 °C for 4 h, and calcined at 550 °C for 3 h to obtain a hydrodenitrogenation catalyst. Th...

Embodiment 3

[0024] Example 3 Weigh a certain amount of γ-Al 2 o 3 Dry rubber powder (81%, Wt) and α-Al 2 o 3 ·(1~3)H 2 Two carbon blacks (10%, Wt) of NEROX 505 and FW 200 were mixed into dry rubber powder (9%, Wt) as pore-expanding agents, M (NEROX 505): M (FW 200) = 1: 1, use dilute Nitric acid (1.5%, Wt) was mixed, kneaded into a clover shape, and calcined at 660°C for 4.5h to obtain the catalyst γ-Al 2 o 3 carrier. The catalyst carrier was soaked in deionized water for 4 h, dried at 80 °C, and then filled with Ni(NO 3 ) 2 ·6H 2 O (7%, Wt), (NH 4 ) 6 h 2 W 24 ·6H 2 The catalyst carrier was impregnated with O (12%, Wt) co-impregnation method for 6 hours, dried at 100°C for 6 hours, and calcined at 700°C for 4 hours to obtain the hydrodenitrogenation catalyst. Using phosphoric acid (3.75%, Wt) solution in the same impregnation method, the catalyst obtained in the above step was impregnated, dried at 110 °C for 4 h, and calcined at 550 °C for 3 h to obtain a hydrodenitrogenat...

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Abstract

The invention discloses coal tar hydro-denitrification catalyst and a preparing method thereof. Carrier for the catalyst is gamma-Al2O3 which carries Ni and W metal active components and P auxiliary. For the catalyst, pores with the diameter ranging from 5nm to 10nm occupy 27-37%, pores with the diameter ranging from 10nm to 20nm occupy 22-30%, the pore volume ranges from 0.32 mL / g to 0.45mL / g, and the specific surface area ranges from 198.2m<2> / g to 268.1 m<2> / g. The catalyst includes, by weight, no more than 0.1% of Na2O, 2.3-4.3% of P2O5, 3-5% of NiO, and 15-25% of WO3. Two carbon blacks including NEROX505 and FW200 are utilized as pore-enlarging additive for the catalyst, so that distribution proportion of the pores with diameters in 5-10nm and 10-20nm in the catalyst is reasonably controlled, pores of the obtained catalyst are small in diameters and are concentrative in distribution, and accordingly reactive metal and auxiliary loading of the catalyst can be greatly improved. Evaluated by a pilot plant, the coal tar hydro-denitrification catalyst is stable in activity, long in service life and applicable to hydro-denitrification for middle and low-temperature coal tar with large amount of nitrogen content.

Description

technical field [0001] The invention relates to a medium-low temperature coal tar hydrogenation denitrification catalyst and an application thereof, which is suitable for the medium-low temperature coal tar hydrogenation denitrification treatment with extremely high nitrogen content, and belongs to the technical field of catalyst preparation. Background technique [0002] In recent years, with the rapid development of my country's economy, domestic oil and gas primary energy is insufficient, and my country's dependence on foreign oil consumption has exceeded 55%, and the oil security situation is not optimistic. my country's annual coking by-products of coal tar is about 17 million tons. The use of coal tar hydrogenation to produce gasoline, diesel and other fuel oils has important practical and strategic significance for replacing some of my country's petroleum resources. [0003] Medium and low temperature coal tar resources are rich in polycyclic aromatic hydrocarbons, co...

Claims

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Application Information

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Patent Type & AuthorityPatents(China)
IPC IPC(8): B01J27/188B01J37/02C10G45/08
Inventor李稳宏李冬李振龙雷宝刚汪谨陈秀娜
OwnerNORTHWEST UNIV