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Modified supported catalyst as well as preparation method and application thereof

A supported catalyst and modification technology, applied in the field of polyethylene polymerization catalysts, can solve the problems of titanium source polluting the environment, cumbersome steps, etc., and achieve the effects of improving the content and distribution, high activity, and sensitive hydrogen responsiveness.

Inactive Publication Date: 2021-12-17
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0010] The main purpose of the present invention is to provide a modified supported catalyst and its preparation method and application, so as to overcome the problems such as environmental pollution and cumbersome steps caused by titanium sources in the prior art. Further, the preparation method of the present invention can Further improve the dispersion degree of the active metal on the surface of the catalyst and improve the catalytic activity of the catalyst

Method used

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  • Modified supported catalyst as well as preparation method and application thereof

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preparation example Construction

[0031] The invention provides a preparation method of a modified supported catalyst, the preparation method comprising: impregnating an inorganic carrier with a solution containing a chromium precursor, a vanadium precursor and a titanium precursor, drying and roasting to obtain a modified supported catalyst ;

[0032] Wherein, the titanium precursor is potassium titanium oxalate and / or ammonium titanium oxalate.

[0033]In the preparation process of the catalyst of the present invention, chromium and vanadium are added as active components, and titanium is added as a modified component. The catalyst of the present invention uses titanium potassium oxalate and / or titanium ammonium oxalate as the titanium source, which can overcome the various defects of other titanium sources in the prior art. Corrosive gas, pollutes the environment, and requires high equipment; tetra-n-butyl titanate is used as the titanium source, which needs to be impregnated in an organic solvent, and can...

Embodiment 1

[0073] A certain amount of potassium titanium oxalate, ammonium metavanadate and basic chromium acetate (the ratio of the amount of substances of titanium potassium oxalate, ammonium metavanadate and basic chromium acetate is 3:1:1, and the loading capacity of titanium is 1.5 wt%, the loading capacity of chromium is 0.5wt%) dissolved in water, stirred at 60°C for 6h, added 10g of silica gel (the pore volume is 1.5-1.7cm 3 / g, the surface area is 250-300m 2 / g), the solution temperature was maintained at 60°C and stirred for 4h, then heated to 120°C and dried for 5h, then transferred to a 120°C oven for 6h; the impregnated silica gel carrier was transferred to a quartz fluidized bed for roasting and activation, and firstly heated at 150°C under nitrogen Calcined under ambient conditions for 1 hour, then raised the temperature to 500°C, switched the gas phase to high-purity air for 4 hours, and then cooled and transferred naturally under the protection of nitrogen to obtain the ...

Embodiment 2

[0075] A certain amount of titanium ammonium oxalate, ammonium metavanadate and basic chromium acetate (the ratio of the amount of titanium ammonium oxalate, ammonium metavanadate and basic chromium acetate is 3:2:1, and the loading capacity of titanium is 1.5 wt%, the loading capacity of chromium is 0.5wt%) dissolved in water, stirred at 60°C for 6h, added 10g of silica gel (the pore volume is 1.5-1.7cm 3 / g, the surface area is 250-300m 2 / g), the solution temperature was maintained at 60°C and stirred for 4h, then heated to 120°C and dried for 5h, then transferred to a 120°C oven for 6h; the impregnated silica gel carrier was transferred to a quartz fluidized bed for roasting and activation, and firstly heated at 150°C under nitrogen Calcined under ambient conditions for 1 hour, then raised the temperature to 500°C, switched the gas phase to high-purity air for 4 hours, and then cooled and transferred naturally under the protection of nitrogen to obtain the catalyst for sto...

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Abstract

The invention discloses a modified supported catalyst as well as a preparation method and application thereof. The preparation method comprises the following steps of: impregnating an inorganic carrier in a solution containing a chromium precursor, a vanadium precursor and a titanium precursor, drying and roasting to obtain the modified supported catalyst, wherein the titanium precursor is titanium potassium oxalate and / or titanium ammonium oxalate. The preparation method disclosed by the invention is simple, low in cost and environment-friendly. The catalyst is controllable in form and performance. The preparation of the catalyst can be completed in a water-phase environment by adopting titanium potassium oxalate and / or titanium ammonium oxalate as a titanium source under the condition of not needing titanium alkoxide and an organic solvent.

Description

technical field [0001] The invention belongs to a polyethylene polymerization catalyst, in particular to a modified supported catalyst and its preparation method and application. Background technique [0002] Currently known polyethylene catalysts mainly include Ziegler-Natta catalysts, chromium-based catalysts, metallocene catalysts and other non-metallocene catalysts. Among them, chromium-based catalysts are favored by the market for their outstanding contribution to the production of high-density polyethylene and the irreplaceability of their products, and up to now, about 50% of the world's high-density polyethylene is still produced by them. [0003] J.PHogan and R.L.Bank both reported silica gel-loaded chromium oxide catalysts in the patent US2825721, that is, the first-generation Phillips catalysts known later. Some patents such as US4294724, US4295997, US4528338, US5401820, US6388017, etc. have carried out modification research on such supported chromium oxide catal...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08F10/02C08F4/69C08F4/68C08F210/16C08F210/14
CPCC08F10/02C08F110/02C08F210/16C08F2410/04C08F4/69C08F4/68C08F2500/04C08F210/14
Inventor 任鹤张瑞高宇新杨琦王华孙彬彬王立娟王文燕牛娜杨国兴张明强赵兴龙郭峰
Owner PETROCHINA CO LTD