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Catalyzer for regenerating the waste lubricant oil by hydrogenation and the preparing method

A technology of hydrogenation regeneration and waste lubricating oil, which is applied in the direction of chemical instruments and methods, physical/chemical process catalysts, lubricating compositions, etc., can solve the problems such as difficult to achieve hydrogenation refining effect, achieve strong saturation ability of aromatic hydrocarbons, and repeat preparation Good performance and short preparation process

Inactive Publication Date: 2008-11-19
京福马(北京)石油化工高新技术有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the current waste lubricating oil regeneration process, the hydrogenation catalyst used is an ordinary oil hydrogenation catalyst. Due to the particularity of the waste lubricating oil components, it is difficult to achieve the ideal hydrogenation catalyst when the existing ordinary hydrogenation catalyst is used to recycle waste lubricating oil. Hydrogen refining effect

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0026] Embodiment 1, the preparation of catalyst (one)

[0027] (1) Preparation of catalyst carrier

[0028] Weigh 1202.7 grams of commercially available aluminum hydroxide dry rubber powder (containing 25% water of crystallization), add 50 ml of glacial acetic acid, 30 grams of citric acid, 15 grams of ammonium bicarbonate, 36 g of turnip powder and about 1044.2 ml of deionized water, and mix thoroughly , kneaded and extruded into a clover shape of Φ1.6×(3~8)mm, air-dried at room temperature, and then dried at 120°C for 3 hours.

[0029] Put the above-mentioned dried samples in a high-temperature furnace, raise the temperature to 550°C at a rate of 5°C / min, and roast at a constant temperature for 4 hours to obtain the alumina carrier of the present invention. It can be measured that the bulk density of the alumina carrier is 47.3g / 100ml, the pore volume is 0.75ml / g, and the specific surface area is 300m 2 / g, see Table 1 for the main physicochemical properties.

[0030] (2) ...

Embodiment 2

[0035] Embodiment 2, the preparation of catalyst (two)

[0036] (1) Preparation of catalyst carrier

[0037] Weigh 1202.7 grams of commercially available aluminum hydroxide dry rubber powder (containing 25% water of crystallization), add 50 ml of glacial acetic acid, 30 grams of citric acid, 15 grams of ammonium bicarbonate, 36 g of turnip powder and about 1044.2 ml of deionized water, and mix thoroughly , kneaded and extruded into a clover shape of Φ1.6×(3~8)mm, air-dried at room temperature, and then dried at 120°C for 3 hours.

[0038] Put the above-mentioned dried samples in a high-temperature furnace, raise the temperature to 550°C at a rate of 5°C / min, and roast at a constant temperature for 4 hours to obtain the alumina carrier of the present invention. It can be measured that the bulk density of the alumina carrier is 48.1g / 100ml, the pore volume is 0.74ml / g, and the specific surface area is 298m 2 / g, see Table 1 for the main physicochemical properties.

[0039] (2...

Embodiment 3

[0044] Embodiment 3, the preparation of catalyst (three)

[0045] (1) Preparation of catalyst carrier

[0046] Weigh 1202.7 grams of commercially available aluminum hydroxide dry rubber powder (containing 25% water of crystallization), add 50 ml of glacial acetic acid, 30 grams of citric acid, 15 grams of ammonium bicarbonate, 36 g of turnip powder and about 1044.2 ml of deionized water, and mix thoroughly , kneaded and extruded into a clover shape of Φ1.6×(3~8)mm, air-dried at room temperature, and then dried at 120°C for 3 hours.

[0047] Put the above-mentioned dried samples in a high-temperature furnace, raise the temperature to 550°C at a rate of 5°C / min, and roast at a constant temperature for 4 hours to obtain the alumina carrier of the present invention. It can be measured that the bulk density of the alumina carrier is 47.9g / 100ml, the pore volume is 0.77ml / g, and the specific surface area is 295m 2 / g, see Table 1 for the main physicochemical properties.

[0048] ...

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Abstract

The invention relates to a used lube oil hydrogenation catalyst and the preparing method. The catalyst is formed as the alumina is used as the carrier to carry active components W, Ni and assistant agent component P. The catalyst comprises 25%-35% of WO3 by wt, 2.0-7.0% of NiO by wt, 2.0%-5.5% of P by wt and other is alumina carrier. The catalyst is provided with high pore capacity and high surface area. Under the softer medium-pressure condition, impurities such as S, N, O and heavy metal so on in used lube oil is eliminated in large space velocity.

Description

technical field [0001] The invention relates to a hydrogenation catalyst and a preparation method thereof, in particular to a catalyst which can be used for hydrogenation reaction in the regeneration treatment process of waste lubricating oil and a preparation method thereof. Background technique [0002] With the continuous rapid growth of China's economy, the consumption of lubricating oil products is also increasing year by year. In 2006, the apparent consumption of lubricating oil in my country was about 6.8 million tons, and correspondingly, about 4 million tons of waste lubricating oil will be produced. And the recovery rate of waste lubricating oil can reach more than 90%, and most of them are used as fire oil, which not only pollutes the environment, but also wastes energy. [0003] With the continuous rise of crude oil prices and the dwindling of petroleum resources, the regeneration of waste oil has attracted increasing attention, especially the recycling and reuse...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J27/188C10M175/00
Inventor 叶红兵姚光明罗继刚何清玉杨开财张笑剑
Owner 京福马(北京)石油化工高新技术有限公司
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