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High-strength alumina-based hydrogenation catalyst as well as preparation method and application thereof

A hydrogenation catalyst and alumina-based technology, which is applied in the field of oil hydrogenation, can solve the problems of poor hydrothermal stability and low mechanical strength, and achieve the goal of increasing crystallinity and grain size, improving mechanical strength, and improving activity Effect

Active Publication Date: 2022-05-06
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] In order to solve the problems of low mechanical strength and poor hydrothermal stability of alumina-based hydrogenation catalysts in the prior art, the present invention provides a high-strength alumina-based hydrogenation catalyst with high mechanical strength and hydrothermal stability. Stability, which broadens the scope of application of the catalyst, especially, it is especially suitable for the hydrogenation process of coal tar, biodiesel and other water-containing raw materials

Method used

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  • High-strength alumina-based hydrogenation catalyst as well as preparation method and application thereof
  • High-strength alumina-based hydrogenation catalyst as well as preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0041] (1) Add zirconium nitrate to the reaction tank and place 1L of deionized water as the bottom liquid. Put 1L of aluminum sulfate solution and 1L of sodium hydroxide solution into the raw material tank respectively. The temperature of the reaction tank is controlled at 65°C. The aluminum sulfate solution was injected into the reaction tank at a rate of 12 mL / min, while the sodium hydroxide solution was injected and the rate was adjusted to keep the pH value of the reaction tank solution constant at 8.0, and the neutralization was completed after 120 min. Ammonium heptamolybdate and magnesium nitrate were added to the reaction tank after the precipitation was completed, kept at a constant temperature of 95°C and a constant pH value of 7.5 in the reaction tank, aged for 3 hours, then washed with deionized water for 3 times, filtered, and the filter cake was placed in the Dry at 120°C for 3 hours, then use 1.5%H 2 The hydrogen of S is vulcanized, the vulcanization temperatur...

Embodiment 2

[0046] (1) Add titanium nitrate to the reaction tank and place 1L of deionized water as the bottom liquid. Put 1L of aluminum sulfate solution and 1L of sodium hydroxide solution into the raw material tank respectively. The temperature of the reaction tank is controlled at 65°C. The aluminum sulfate solution was injected into the reaction tank at a rate of 15 mL / min, while the sodium hydroxide solution was injected and the rate was adjusted to keep the pH value of the reaction tank solution constant at 8.5, and the neutralization was completed after 120 min. Add ammonium tungstate and calcium nitrate to the reaction tank after the precipitation is completed, keep the temperature in the reaction tank at 90°C and the pH value at 8.0, aging for 3 hours, then wash with deionized water for 3 times, filter the filter cake at 120 ℃ for 3 hours, and then use 1.5%H 2 The hydrogen of S is vulcanized, the vulcanization temperature is 300°C, the vulcanization pressure is 3.4MPa, the vulca...

Embodiment 3

[0051] (1) Add zirconium nitrate to the reaction tank and place 1L of deionized water as the bottom liquid. Put 1L of aluminum sulfate solution and 1L of sodium hydroxide solution into the raw material tank respectively. The temperature of the reaction tank is controlled at 70°C. The aluminum sulfate solution was injected into the reaction tank at a rate of 10 mL / min, while the sodium hydroxide solution was injected and the rate was adjusted to keep the pH value of the reaction tank solution constant at 8.5, and the neutralization was completed after 120 min. Ammonium heptamolybdate and calcium nitrate were added to the reaction tank after the precipitation was completed, kept at a constant temperature of 80°C and a constant pH value of 7.5 in the reaction tank, aged for 3 hours, then washed with deionized water for 3 times, filtered, and the filter cake was placed in the Dry at 120°C for 3 hours, then use 1.5%H 2 The hydrogen of S is vulcanized, the vulcanization temperature ...

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Abstract

The invention provides a high-strength alumina-based hydrogenation catalyst, which comprises a carrier and an active component, the carrier comprises alumina, a modifier A selected from at least one of zirconia, titanium oxide and silicon oxide, and a modifier B selected from at least one of magnesium oxide, potassium oxide and calcium oxide; the active component is a VIB group metal sulfide and a VIII group metal oxide. The catalyst is prepared by adopting a coprecipitation method and comprises the following steps: firstly, preparing a mixture of aluminum oxide and a modifier A, adding group VIB metal salt and precursor salt of a modifier B in an aging process after precipitation is completed, vulcanizing, forming, dipping group VIII metal salt, and drying to obtain the catalyst. The catalyst has high mechanical strength and hydrogenation activity, the application range of the catalyst is widened, and the catalyst is especially suitable for the hydrogenation process of water-containing raw materials such as coal tar and biodiesel.

Description

technical field [0001] The invention relates to the technical field of hydrogenation of oil products, in particular to a high-strength alumina-based hydrogenation catalyst. Background technique [0002] As the maintenance period of the main hydrogenation unit in the refinery increases from 2-3 years to 4-5 years, the high mechanical strength of the hydrogenation catalyst is also an important factor to ensure the long-term operation of the unit. Since the alumina carrier is in a water vapor environment, the surface of the alumina will react with water, resulting in a reduction in the mechanical strength of the conventional alumina-based hydrogenation catalyst, resulting in an increase in the pressure drop of the device, resulting in a reduction in the operating cycle of the device. [0003] Hydrotreating of coal tar is an important process for refining coal tar, mainly to remove impurities such as sulfur and nitrogen in coal tar. CN 108906118A discloses a coal tar hydrogenat...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J27/051B01J27/049B01J37/02B01J37/03B01J37/10B01J37/20C10G45/08
CPCB01J27/0515B01J27/049B01J37/0201B01J37/031B01J37/10B01J37/20C10G45/08C10G2300/202C10G2300/70Y02P20/52
Inventor 刘丽杨成敏郭蓉段为宇周勇李扬姚运海孙进郑步梅
Owner CHINA PETROLEUM & CHEM CORP
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