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Preparation method for hydrogenation pretreatment catalyst containing silicon aluminum-phosphorus aluminum composite molecule sieve

A composite molecular sieve and hydrogenation pretreatment technology, which is applied in the direction of molecular sieve catalysts, catalyst activation/preparation, physical/chemical process catalysts, etc., can solve the problem of increasing carbon deposition in catalysts, molecular sieves cannot effectively match acid centers, and affect hydrogenation treatment Catalyst long-term stable operation and other issues, to achieve the effect of weakening the force and improving hydrogenation saturation performance

Active Publication Date: 2014-12-17
CHINA NAT OFFSHORE OIL CORP +2
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Hydrogenation pretreatment catalysts usually use alumina as a carrier. However, due to the limitations of the pore size and surface acidity of alumina itself, the catalyst prepared solely as a carrier cannot achieve deep polycyclic aromatic hydrocarbon saturation and removal of heterocyclic nitrides. Modification of alumina
[0004] CN1769384A discloses a method for preparing a heavy oil hydrotreating catalyst, which is characterized in that a certain amount of Beta molecular sieve and alumina are used as a carrier together, and after impregnating the active component, the catalyst is prepared, but a strong acidic molecular sieve is added to modify the carrier, Although it increases the cracking activity of the catalyst, it also increases the amount of carbon deposition on the catalyst, which affects the long-term stable operation of the hydrotreating catalyst
However, a single introduction of molecular sieves cannot effectively match acid centers and hydrogenation centers. It is necessary to comprehensively modify the surface of the support and impregnate the active metals at the locked position to develop a high-activity hydrogenation pretreatment catalyst.

Method used

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  • Preparation method for hydrogenation pretreatment catalyst containing silicon aluminum-phosphorus aluminum composite molecule sieve
  • Preparation method for hydrogenation pretreatment catalyst containing silicon aluminum-phosphorus aluminum composite molecule sieve
  • Preparation method for hydrogenation pretreatment catalyst containing silicon aluminum-phosphorus aluminum composite molecule sieve

Examples

Experimental program
Comparison scheme
Effect test

Embodiment -1

[0024]Preparation of Ni-Mo impregnation solution: Take 360.0 g molybdenum trioxide (Jiangsu Jiangyan Bond Metal Products Factory, purity 99.8%), 120.0 g basic nickel carbonate (Fushun Xinguang Fine Chemical Co., Ltd., purity 99.8%) and Put 18.0 g of citric acid into a three-necked flask, add 240 mL of deionized water, heat and stir, slowly drop in 45.0 g of phosphoric acid (mass concentration 85%), stir at 100 °C for 2 h, add deionized water after completely dissolving The volume is fixed to 600 mL, so that the concentration of each substance in the final impregnation solution is (calculated as oxide): MoO 3 60.0g / 100mL, NiO 12.0g / 100mL, P 2 o 5 4.0g / 100 mL, the pH value of the soaking solution is 1.6, and it is marked as soaking solution A.

[0025] Weigh 30.0 g of ethylenediaminetetraacetic acid (EDTA) and dissolve 55.0 g of ammonia water, then add 20.0 g of deionized water to prepare an EDTA-ammonia solution with a mass concentration of 30%.

[0026] Take 50 mL of soak...

Embodiment -2

[0031] USY / AlPO 4 Synthesis of -5 composite molecular sieve: Mix 436.0 g of phosphoric acid (AR, mass concentration 85%) and 1224.0 g of deionized water in a 35 °C water bath, add 240.0 g of pseudoboehmite Shandong Aluminum Co., Ltd., Al 2 o 3 The mass content is 72.0wt%), and magnetically stirred in a water bath at 35 °C for 0.5 h to obtain an aluminum phosphate sol; add 16.0 g of poly N,N-ditetraethylammonium hydrochloride (referred to as PCD, Henan Daochun Co., Ltd., purity 95%), after stirring slowly for 0.5 h, add 256.0 g of triethylamine (abbreviated as TEA, purity 99%), and continue stirring for 0.5 h to form a uniform sol. The molar ratio of the materials in this reaction system is Al 2 o 3 :P 2 o 5 :TEA:H 2 O=1:1.05:1.2:50. The sol was put into a polytetrafluoroethylene autoclave and aged at 100 °C (heating rate 1 °C / min) for 4 h to obtain AlPO 4 -5 seed crystals, and then add 160.0 g USY molecular sieves (Shanghai Xinnian Auxiliary Co., Ltd., with a silicon-al...

Embodiment -3

[0035] Take 65.0 g of HTZ-1 carrier and place it in an impregnation tank, pour a certain volume of impregnating solution C into it, and after impregnating it for 2 hours, dry the impregnated carrier naturally, dry it in an oven at 120 °C for 8 hours, and finally place it in a muffle furnace The temperature was programmed to rise to 480 ℃ and calcined for 4 h to obtain the catalyst HTC-1D.

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Abstract

The present invention discloses a preparation method for a hydrogenation pretreatment catalyst containing a silicon aluminum-phosphorus aluminum composite molecule sieve. According to the catalyst prepared by the method, a silicon aluminum-phosphorus aluminum composite molecule sieve, macroporous alumina and modified alumina form a carrier, one or a plurality of materials selected from group VIB metals and group VIII metals are adopted as active components, P2O5 is adopted as an auxiliary agent, a specific surface area of the catalyst is ??150-300 m<2> / g, and a pore volume is 0.30-0.60 cm<3> / g. According to the method, the silicon aluminum-phosphorus aluminum composite molecule sieve is introduced to regulate acid distribution of the catalyst, and the pH value of the impregnating solution is modulated to weaken acting force between the carrier and the metal, increase active center density, and reasonably match a hydrogenation activity center and an acid center of the catalyst. The catalyst prepared by the method provides an excellent aromatic ring hydrogenation saturation performance and C-N bond clearage capacity during a poor quality wax oil hydrotreating process so as to increase hydrogenation dearomatization and hydrogenation denitrogenation of the catalyst.

Description

technical field [0001] The invention relates to the field of hydrogenation treatment catalysts, in particular to a method for preparing a hydrogenation pretreatment catalyst containing silicon-aluminum-phosphorus-aluminum composite molecular sieves. Background technique [0002] As the world's petroleum resources become increasingly heavy and inferior, and petroleum fuel products become increasingly high-quality and clean, the development of high-efficiency conversion of heavy crude oil and clean oil production technology has become the top priority of today's petroleum processing industry. Hydrocracking technology is a comprehensive processing technology that integrates the lightening of heavy oil and the production of clean oil products. It has become the core technology of future oil processing and the main trend of vigorous development of refining and chemical enterprises. The core of the hydrocracking technology lies in the hydrocracking catalyst, and the catalyst conta...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/84B01J37/00B01J32/00
Inventor 肖寒杨建国于海斌李孝国朱金剑石芳张国辉李佳
Owner CHINA NAT OFFSHORE OIL CORP