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Gasoline hydrodesulfurization catalyst, and preparation method and application thereof

A technology for desulfurization catalysts and gasoline hydrogenation, applied in metal/metal oxide/metal hydroxide catalysts, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems of catalyst deactivation and deactivation

Active Publication Date: 2020-03-17
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, under too high temperature and pressure, the existing Al 2 o 3 Supported hydrodesulfurization catalysts will be permanently deactivated
Because under high temperature and high pressure, Al 2 o 3 The Al atoms in the catalyst will undergo atom transfer reactions with the metal atoms (such as Ni, Mo, etc.) of the metal active center supported by them, thereby changing the molecular structure of the catalyst and causing the catalyst to lose its activity.

Method used

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  • Gasoline hydrodesulfurization catalyst, and preparation method and application thereof
  • Gasoline hydrodesulfurization catalyst, and preparation method and application thereof
  • Gasoline hydrodesulfurization catalyst, and preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0052] Mix Co powder (140-160 μm in particle size), Mo powder (140-160 μm in particle size), and catalytic oil slurry in proportions of 3% by weight, 10% by weight, and 87% by weight, and fill the graphite with a cavity. rod (the length is 70mm, the diameter is 8mm, the cavity length is 50mm, and the cavity inner diameter is 5mm), and then the graphite rod is sealed to obtain the anode graphite rod. Place the above-mentioned anode graphite rod and cathode graphite rod (a solid graphite rod with a diameter of 20 mm and a length of 30 mm) in an arc discharge plasma device. After closing the device hatch, turn on the vacuum pump to evacuate the device, and then purge the device with nitrogen for 3 times , and then purged the device once with a mixture of hydrogen and helium. Then pass into the arc discharge device a mixed atmosphere containing hydrogen and helium (the content of hydrogen is 50% by volume) to an absolute pressure of 0.01 to 0.03 MPa, then turn on the circulating c...

Embodiment 2

[0054] Mix Co powder (140-160 μm in particle size), Mo powder (140-160 μm in particle size), and catalytic oil slurry in proportions of 5% by weight, 10% by weight, and 85% by weight, and fill the graphite with a cavity. rod (the length is 70mm, the diameter is 8mm, the cavity length is 50mm, and the cavity inner diameter is 5mm), and then the graphite rod is sealed to obtain the anode graphite rod. Place the above-mentioned anode graphite rod and cathode graphite rod (a solid graphite rod with a diameter of 20 mm and a length of 30 mm) in an arc discharge plasma device. After closing the device hatch, turn on the vacuum pump to evacuate the device, and then purge the device with nitrogen for 3 times , and then purged the device once with a mixture of hydrogen and helium. Then pass into the arc discharge device a mixed atmosphere containing hydrogen and helium (the content of hydrogen is 50% by volume) to an absolute pressure of 0.01 to 0.03 MPa, then turn on the circulating c...

Embodiment 3

[0056] Mix Co powder (140-160 μm in particle size), Mo powder (140-160 μm in particle size, and catalytic oil slurry in proportions of 7% by weight, 10% by weight, and 83% by weight, and fill them into graphite rods with cavities. (length is 70mm, and diameter is 8mm, cavity length 50mm, cavity internal diameter 5mm), then seals graphite rod, obtains anode graphite rod.The above-mentioned anode graphite rod and cathode graphite rod (solid graphite rod, diameter is 20mm, length 30mm) placed in the arc discharge plasma device, after closing the device hatch, turn on the vacuum pump to evacuate, then use the nitrogen to purge the device for 3 times, and then use the mixed gas containing hydrogen and helium to purge the device for 1 time. Then to Into the arc discharge device, a mixed atmosphere containing hydrogen and helium (hydrogen content is 50% by volume) is introduced to an absolute pressure of 0.01-0.03MPa, then the circulating cooling water is turned on, the DC power suppl...

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Abstract

The invention relates to a gasoline hydrodesulfurization catalyst, and a preparation method and an application thereof. The method comprises the following steps: a, a graphite rod with a cavity is filled with a mixed material containing a first metal component, a second metal component and a catalytic oil slurry, and then the graphite rod is sealed to obtain an anode graphite rod; and b, the anodegraphite rod obtained in step a and a cathode graphite rod are put into an arc discharge device, the anode graphite rod and the cathode graphite rod are subjected to arc discharge under a mixed atmosphere containing hydrogen and helium, and after the anode graphite rod is consumed completely, the gasoline hydrodesulfurization catalyst with graphene as a carrier, obtained in the arc discharge device, is collected, wherein the first metal component is selected from group VIB metals, and the second metal component is a selected from group VIII metals. The catalyst has a high desulfurization activity, and can be used for deep desulfurization of industrial catalytically cracked gasoline under mild conditions.

Description

technical field [0001] The disclosure relates to a preparation method of a gasoline hydrodesulfurization catalyst, a gasoline hydrodesulfurization catalyst and applications thereof. Background technique [0002] There are many hazards in the sulfur compounds in gasoline: the sulfur oxides generated by combustion at high temperature will turn into acid, corrode and damage engine parts, cause irreversible poisoning of the three-way catalyst in the engine exhaust purification system, and cause NO X and CO X content increased significantly, and the SO emitted into the atmosphere X It also causes acid rain. Therefore, many countries in the world have made strict regulations on the sulfur content of motor gasoline through regulations. From January 1, 2017, China's motor vehicles have fully implemented the National V emission standard (the sulfur content index limit is 10 μg / g), and the more stringent National VI standard is also being formulated. It can be seen that it is immi...

Claims

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Application Information

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IPC IPC(8): B01J23/882B01J23/883C10G45/08
CPCB01J23/882B01J23/883C10G45/08C10G2300/1037C10G2300/1044C10G2300/104C10G2300/70C10G2300/202
Inventor 任亮邵志才刘涛施瑢邓中活聂鑫鹏
Owner CHINA PETROLEUM & CHEM CORP
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