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Difunctional coupling catalyst for hydrocracking of waste plastics and preparation method of difunctional coupling catalyst

A hydrocracking and catalyst technology, applied in chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, preparation of liquid hydrocarbon mixtures, etc., can solve the problem of high metal loading, high catalyst cost, and liquid product Problems such as low yield

Pending Publication Date: 2022-05-13
CHINA UNIV OF PETROLEUM (EAST CHINA) +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The catalysts currently reported for the hydrocracking of waste plastics are all noble metal catalysts, with high metal loading and high catalyst cost. In addition, the yield of liquid products obtained from waste plastics hydrocracking is low.

Method used

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  • Difunctional coupling catalyst for hydrocracking of waste plastics and preparation method of difunctional coupling catalyst
  • Difunctional coupling catalyst for hydrocracking of waste plastics and preparation method of difunctional coupling catalyst
  • Difunctional coupling catalyst for hydrocracking of waste plastics and preparation method of difunctional coupling catalyst

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preparation example Construction

[0039] On the other hand, a method for preparing a catalyst for hydrocracking of waste plastics comprises the following steps:

[0040] (1) Add the zirconium source to the ammonium metatungstate solution to obtain mixture I;

[0041] (2) The mixture I is dried and calcined to obtain the carrier WO 3 -ZrO 2 ;

[0042] (3) The carrier WO of step (2) 3 -ZrO 2 Immersed in a metal salt solution to obtain mixture II;

[0043] (4) The mixture II is dried and roasted to obtain MO x / WO 3 -ZrO 2 precursor;

[0044] (5) The above MO x / WO 3 -ZrO 2 Precursor reduction to give M / WO 3 -ZrO 2 catalyst.

[0045] M represents the supported metal, including one or a mixture of two or more of Pd, Rh, Ir, Ni, Fe, Co, and Cu. MO x Indicates the most stable metal oxide supported metal elements.

[0046] In some embodiments, the mixture I is dried at a temperature of 90-100°C.

[0047] In some embodiments, in step (2), the calcination temperature is 550-800°C.

[0048] In some em...

Embodiment 1

[0072] Prepare a 0.245g / ml ammonium metatungstate solution with ammonium metatungstate and deionized water, weigh 1g of uniformly ground zirconium hydroxide powder and impregnate it in 0.65ml ammonium metatungstate solution for 30min, the impregnated catalyst is passed through Drying overnight at 90°C and calcining at 923K for 3 hours to obtain the superacid carrier WO 3 -ZrO 2 ; Prepare the nickel nitrate solution of 0.479g / ml with nickel nitrate hydrate and deionized water, weigh 1g of evenly ground superacid carrier WO 3 -ZrO 2 The powder was impregnated in 0.65ml of nickel nitrate solution and left to stand for 30min, and the impregnated catalyst was dried overnight at 90°C and calcined at 773K for 3h to obtain nickel oxide-supported WO 3 -ZrO 2 Precursor; the calcined catalyst was passed through 10% H at 500°C 2 / 90%Ar reduction for 3h to obtain (10wt%)Ni / (15wt%)WO 3 -ZrO 2 -650.

Embodiment 2

[0074] Prepare a 0.245g / ml ammonium metatungstate solution with ammonium metatungstate and deionized water, weigh 1g of uniformly ground zirconium hydroxide powder and impregnate it in 0.65ml ammonium metatungstate solution for 30min, the impregnated catalyst is passed through Drying overnight at 90°C and calcining at 1073K for 3 hours to obtain the superacid carrier WO 3 -ZrO 2 ; Prepare the nickel nitrate solution of 0.479g / ml with nickel nitrate hydrate and deionized water, weigh 1g of evenly ground superacid carrier WO 3 -ZrO 2 The powder was impregnated in 0.65ml of nickel nitrate solution and left to stand for 30min, and the impregnated catalyst was dried overnight at 90°C and calcined at 773K for 3h to obtain nickel oxide-supported WO 3 -ZrO 2 Precursor; the calcined catalyst was passed through 10% H at 500°C 2 / 90%Ar reduction for 3h to obtain (10wt%)Ni / (15wt%)WO 3 -ZrO 2 -800.

[0075] Carry out NH to the catalyst before and after the catalyst supporting metal ...

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Abstract

The invention relates to a difunctional coupling catalyst for waste plastic hydrocracking and a preparation method thereof, the difunctional coupling catalyst is obtained by preparation of an acidic carrier WO3-ZrO2 and loading of metal components, the content of WO3 in the catalyst is 5-30%, the metal components are one or more than two of Pd, Rh, Ir, Ni, Fe, Co and Cu, and the loading capacity is 0.01-30%. The difunctional coupling catalyst disclosed by the invention is simple in preparation method and relatively high in catalytic activity, and full conversion of the waste plastics can be realized under mild conditions. The catalyst disclosed by the invention realizes effective coupling of a cracking function and a hydrogenation / dehydrogenation function by utilizing a synergistic effect of an acidic carrier and metal, and promotes efficient hydrocracking conversion of waste plastics into naphtha and fuel oil.

Description

technical field [0001] The invention relates to catalytic technology in the field of petrochemical industry, in particular to a catalyst for hydrocracking of waste plastics and a preparation method thereof. Background technique [0002] Plastic products are widely used in many important areas of the national economy due to their advantages such as abundant sources, good processability, and low price. Human life and health are also threatened. Plastic pollution has become a challenge to global sustainable development, and the control of plastic pollution has become a common consensus in society. [0003] It is of great significance to rationally and effectively utilize waste plastics as new resources. As people's awareness of environmental protection increases, more and more waste plastics are recycled. The recycling methods of waste plastics mainly include physical and chemical methods. The physical recycling method mainly recycles waste plastics mechanically, and uses p...

Claims

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Application Information

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IPC IPC(8): B01J23/888C10G1/08
CPCB01J23/888C10G1/08
Inventor 冯翔商敬媛赵辉张新功杨朝合陈德
Owner CHINA UNIV OF PETROLEUM (EAST CHINA)