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Continuous reforming catalyst and preparation method and application thereof

A technology for reforming catalysts and catalysts, applied in chemical instruments and methods, physical/chemical process catalysts, naphtha catalytic reforming, etc., can solve problems such as low carbon deposition rate and increased catalyst carbon deposition rate, and achieve coke production Low efficiency, good reproducibility, good activity and stability

Active Publication Date: 2020-09-15
REZEL CATALYSTS CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0022] CN1234455C discloses a multi-metal reforming catalyst and its preparation method. The mass percentages of the components included are 0.01-2.0 for group VIII metals, 0.01-5.0 for group IV metals, 0.01-10.0 for europium, 0.01-10 for cerium, and 0.1-10 for halogens. 10.0, high temperature resistant inorganic oxide 63-99.9, the catalyst is used for naphtha reforming reaction, has high activity and selectivity, low carbon deposition rate, long service life; The lanthanide components Eu and Cerium are also introduced into the metal reforming catalyst. In the reforming reaction of naphtha, it also has high activity and selectivity, low carbon deposition rate and long life.
[0030] CN105561991B discloses a platinum-tin bimetallic reforming catalyst and its preparation method. The average tin concentration in the shell area of ​​the catalyst is 1.0 to 2.0 times the average tin concentration in the central area, that is, the tin element is non-uniformly distributed in the catalyst, which has relatively Good activity and stability, and low carbon deposition rate
However, the increase in operating severity makes the catalyst carbon deposition rate increase rapidly

Method used

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  • Continuous reforming catalyst and preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0057] Add 2 liters of water in the gel-forming tank, add dropwise sodium aluminate solution (industrial product, Sichuan Leshan Runhe Catalytic New Material Company, Na 2 O 150g / L, Al 2 o 3 100g / L) and aluminum sulfate solution (industrial product, Sichuan Leshan Runhe Catalytic New Material Company, Al 2 o 3 90g / L), and respectively control the dropping rate of sodium aluminate solution and aluminum sulfate solution, so that the pH of the material is kept in the range of 8.5 to 9.5, add about 0.9 liter of sodium aluminate and 0.82 liter of aluminum sulfate. After filtering and washing with water, add 13 milliliters of dilute nitric acid (chemically pure reagent, Beijing Chemical Plant, 1:1 volume) to acidify with 0.3 liters of water after acidifying for 1 hour, and add a predetermined amount of stannous chloride (chemically pure reagent, Beijing Chemical plant) and the hydrochloric acid solution (chemically pure reagent, Beijing chemical plant) of lanthanum chloride (ch...

Embodiment 2

[0069] This example is combined with Example 1 to illustrate the effect of coating the protective layer on the performance of the catalyst.

[0070] The catalyst was prepared according to the method of Example 1, except that the catalyst pellet coating step was omitted, and drying and water chlorine activation were carried out under the same conditions to obtain the catalyst of Example 2. The quality of each component relative to dry alumina is: platinum 0.25%, tin 0.25%, lanthanum 0.10, chlorine 1.15%; its pore volume is 0.80 ml / g, and its specific surface area is 252 m 2 / g, bulk density 0.65 g / ml, catalyst average particle size 1.2mm.

Embodiment 3

[0072] This example is combined with Example 1 to illustrate the effect of changes in rare earth components on the performance of the catalyst of the present invention in actual use.

[0073] The catalyst was prepared according to the method of Example 1, except that the rare earth lanthanum chloride solution was not added during the preparation process, and drying and water chlorine activation were carried out under the same conditions to obtain the catalyst of Example 3. The quality of each component relative to dry alumina is: platinum 0.25%, tin 0.25%, chlorine 1.22%; its pore volume is 0.72 ml / g, and its specific surface area is 244 m 2 / g, bulk density 0.67 g / ml, catalyst average particle size 1.21 mm.

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Abstract

The invention relates to a continuous reforming catalyst and a preparation method thereof. The catalyst is characterized in that the catalyst has a high pore volume and is provided with a compact outer protection layer, and the catalyst comprises an alumina carrier and the following content components based on alumina: 0.1-0.4 m% of platinum, 0.1-0.6 m% of tin, 0.7-1.5 m% of chlorine, and 0.1-0.4m% of lanthanum; the preparation method comprises the following steps: firstly, preparing high-pore-volume aluminum oxide pellets containing tin and lanthanum, and impregnating with platinum; coatingwith tin-containing aluminum oxychloride sol to form a compact outer protective layer, wherein the content of tin / total tin in the protective layer is 0.1-10.0 m%, and the content of aluminum oxide / total aluminum oxide in the protective layer is 0.1-10.0 m%; the particle size of the prepared spherical catalyst ranges from 1.0 mm to 2.0 mm, the pore volume ranges from 0.4 ml / g to 1.0 ml / g, the specific surface area ranges from 150 m < 2 > / g to 400 m < 2 > / g, and the bulk density ranges from 0.5 g / ml to 0.9 g / ml. The catalyst has the advantages of good renewability, good wear resistance, good activity and stability, high aromatic hydrocarbon yield and low coke yield.

Description

technical field [0001] The invention relates to a reforming catalyst and its preparation method and application, in particular to a high pore volume continuous reforming catalyst containing platinum tin and lanthanum, its preparation method and application, and belongs to the technical field of petrochemical industry. Background technique [0002] The catalytic reforming process is one of the important petroleum processing technologies for the production of gasoline, aromatics and cheap hydrogen. The naphtha components can be converted into products rich in aromatics through the catalytic reforming process, which can be used to deploy high-octane gasoline or Separation and purification to obtain benzene, toluene, xylene and other chemical raw materials. [0003] With the upgrading of environmental protection indicators of refined oil products, the inferior quality of some processing raw materials brought about by the diversification of processing raw materials, and the rapid...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J27/135B01J35/02B01J35/10C10G35/09B01J35/00
CPCB01J27/135C10G35/09B01J35/40B01J35/615B01J35/635Y02P20/52
Inventor 卓润生刘新生祝世珍刘兵王洪飞
Owner REZEL CATALYSTS CO LTD