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A catalyst for propane dehydrogenation to propylene, its preparation method and application

A technology for propane dehydrogenation and catalyst, applied in the direction of catalyst, catalyst carrier, carbon compound catalyst, etc., can solve the problem of fast decay of activity, and achieve the effect of prolonging life, good mechanical performance and good stability

Active Publication Date: 2021-12-21
CHINA PETROLEUM & CHEM CORP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the present invention, adding a small amount of S or S compounds to the alkane raw material is beneficial to increase the activity and anti-coking performance of the catalyst, but its activity decays quickly

Method used

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  • A catalyst for propane dehydrogenation to propylene, its preparation method and application

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0039] Preparation of Al-Si-C-O composite carrier material: Take 1 weight part of phenolic resin and dissolve it in 4 weight parts of absolute ethanol. After 0.06 parts by weight of oxalic acid and 0.05 parts by weight of hydrochloric acid, hydrolyze for 30 hours at room temperature to obtain a carbon-silicon binary sol; Gel, the gel was dried at 90°C for 18 hours to obtain a dry gel, and the dry gel and 16 parts by weight of pseudo-boehmite were ball-milled with a ball mill for 18 hours; 2 Under the atmosphere, the temperature was raised to 1300°C at a heating rate of 5°C / min, and after 13 hours of reaction, it was cooled to room temperature; then the reacted product was oxidized in air at 700°C for 4 hours, washed with nitric acid and hydrofluoric acid in turn, and then washed with Al-Si-C-O composite carrier material can be obtained by washing, filtering and drying;

[0040] Preparation of spherical carrier: Add the Al-Si-C-O composite carrier material to the aqueous solut...

Embodiment 2

[0045] Preparation of Al-Si-C-O composite carrier material: Take 1 weight part of phenolic resin and dissolve it in 4 weight parts of absolute ethanol. After 0.08 parts by weight of oxalic acid and 0.04 parts by weight of hydrochloric acid, hydrolyze at room temperature for 25 hours to obtain a carbon-silicon binary sol; Gel, the gel was dried at 80°C for 23 hours to obtain a dry gel, and the dry gel and 14 parts by weight of pseudo-boehmite were ball-milled for 15 hours with a ball mill; 2 Under the atmosphere, the temperature was raised to 1350°C at a heating rate of 8°C / min, and after 23 hours of reaction, it was cooled to room temperature; then the reacted product was oxidized in air at 650°C for 3 hours, washed with nitric acid and hydrofluoric acid in turn, and then washed with Al-Si-C-O composite carrier material can be obtained by washing, filtering and drying;

[0046] Preparation of spherical carrier: Add the Al-Si-C-O composite carrier material into the sodium algi...

Embodiment 3

[0050] Preparation of Al-Si-C-O composite carrier material: Preparation of Al-Si-C-O composite carrier material: get 1 weight part of phenolic resin, dissolve it in 4 weight parts of absolute ethanol, and under stirring condition, mix 7 weight parts After adding 0.03 parts by weight of oxalic acid and 0.07 parts by weight of hydrochloric acid, hydrolyze for 35 hours at room temperature to obtain a carbon-silicon binary sol; then add 0.35 parts by weight of The gelling agent hexamethylenetetramine was used to obtain a gel, and the gel was dried at 100°C for 10 hours to obtain a xerogel, and the xerogel and 18 parts by weight of pseudo-boehmite were ball-milled for 120 hours with a ball mill; The material after ball milling is in N 2 Under the atmosphere, the temperature was raised to 1250°C at a heating rate of 3°C / min, and after 8 hours of reaction, it was cooled to room temperature; then the reacted product was oxidized in air at 750°C for 6 hours, washed with nitric acid and...

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Abstract

A catalyst for propane dehydrogenation to propylene, a preparation method and application thereof, belonging to the field of propane dehydrogenation to propylene catalysts. It is characterized in that: it includes an active component and a carrier, the mass percentage of the active component in the catalyst is Pt: 0.25-0.45%, Sn: 0.05-0.2%, K: 0.5-1.1%; the carrier is Al ‑Si‑C‑O composite carrier, the Al‑Si‑C‑O composite carrier is a spherical carrier with a diameter of 1.6-2.0 mm. The preparation method can effectively combine several carriers of aluminum, silicon and carbon to form a unified whole. The carrier has been modified by a special method, which has high strength on the one hand and large pore volume on the other hand. In addition, the catalyst has good thermal conductivity and mechanical properties, which can avoid hot spots during the reaction process, and has good anti-wear ability, which greatly prolongs the life of the catalyst.

Description

technical field [0001] A catalyst for propane dehydrogenation to propylene, a preparation method and application thereof, belonging to the field of propane dehydrogenation to propylene catalysts. Background technique [0002] As an important basic chemical raw material, propylene is mainly used to produce chemical products such as polypropylene, cumene, carbonyl alcohol, propylene oxide, acrylic acid, and acrylonitrile. Currently, propylene supply comes mainly from the by-products of naphtha cracking to ethylene and catalytic cracking processes. However, due to the rapid growth of demand for propylene, the supply of propylene has become increasingly tight in recent years, and the original source of propylene cannot meet the demand. The production processes to expand the source of propylene include propane dehydrogenation to propylene, olefin interconversion process, olefin metathesis process and methanol to olefin, among which the propane dehydrogenation to propylene proces...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/62B01J35/08C07C5/333C07C11/06B01J32/00
CPCC07C5/3332B01J23/002B01J23/626C07C2523/62B01J2523/00B01J35/51B01J2523/13B01J2523/41B01J2523/43B01J2523/828C07C11/06Y02P20/52
Inventor 贾庆龙菅秀君王申军马瑞杰朱相春
Owner CHINA PETROLEUM & CHEM CORP