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Asphalt ball oxidation non-melting pretreatment method

A pitch ball, hourly technique

Active Publication Date: 2020-08-07
SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The amount of liquid organic solvent used in the prior art is dozens of times the weight of asphalt pellets. More importantly, the organic solvent is flammable and explosive, which is extremely dangerous and leads to dangerous production processes.

Method used

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  • Asphalt ball oxidation non-melting pretreatment method
  • Asphalt ball oxidation non-melting pretreatment method
  • Asphalt ball oxidation non-melting pretreatment method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] Put 1 kg of 0.05mm naphthalene pitch balls into the oxidation non-melting reactor, feed 50 liters / h of air, raise the temperature from room temperature to 80°C at a heating rate of 60°C / h, and stay for 2h; then switch to volume Mixed gas of n-heptane vapor and N2 with a ratio of 0.1:100, the gas flow rate is 100 liters / h, the temperature is raised from 80°C to 90°C at a heating rate of 60°C / h, and the temperature is raised for 5 hours to obtain asphalt balls with all naphthalene removed ;Finally switch to 300 liters / h of air from 90°C to 280°C at a heating rate of 240°C / h, and stay for 0.5h to obtain oxidized asphalt balls.

[0030] In the embodiment, the oxidation and non-melting degree of asphalt balls can be calculated according to the cohesive rate: the oxidized and non-melting pitch balls in N 2 Heat up to 800°C in the atmosphere and stay for 1 hour to obtain carbonized asphalt balls; randomly select 30-50 carbonized asphalt balls, and the percentage of the total n...

Embodiment 2

[0034] Put 1 kg of 2mm naphthalene pitch-containing balls into the oxidation non-melting reactor, feed 150 liters / h of air, raise the temperature from room temperature to 80°C at a heating rate of 10°C / h, and stay for 10h; then switch to volume ratio It is a mixed gas of 30:100 methanol vapor and Ar, the gas flow rate is 500 liters / h, the temperature is raised from 80°C to 120°C at a heating rate of 5°C / h, and the temperature is raised for 50 hours to obtain asphalt balls with all naphthalene removed; finally switch 1000 liters / h of air is heated from 120°C to 350°C at a rate of 100°C / h, and stays for 5 hours to obtain oxidized asphalt balls.

[0035] After testing, the bonding rate is 0.1%, the oxygen content is 6.3wt%, CO 2 The specific surface area is 94.4m 2 / g, the pore structure is shown in the attached figure 2 .

Embodiment 3

[0037] Put 1 kg of 1mm naphthalene pitch-containing balls into the oxidation non-melting reactor, feed 100 liters / h of air, raise the temperature from room temperature to 50°C at a heating rate of 20°C / h, and stay for 20h; then switch to volume ratio It is a mixed gas of 20:100 petroleum ether vapor and N2, the gas flow rate is 300 liters / h, the temperature is raised from 50°C to 100°C at a heating rate of 10°C / h, and the temperature is raised for 30h to obtain asphalt balls from which all naphthalene has been removed; finally Switch to 500 liters / h of air from 100°C to 300°C at a heating rate of 120°C / h, and stay for 3 hours to obtain oxidized pitch balls.

[0038] After testing, the bonding rate is 0.08%, the oxygen content is 8.8wt%, and the CO 2 The specific surface area is 100.9m 2 / g, the pore structure is shown in the attached image 3 .

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Abstract

The invention discloses an asphalt ball oxidation non-melting pretreatment method, which is provided for the pretreatment of asphalt balls containing naphthalene or anthracene before oxidation non-melting, and directly adopts gas-phase organic solvent steam to replace the conventional liquid-phase extraction method. The method specifically comprises the following steps: introducing air into asphalt balls containing naphthalene or anthracene, heating from room temperature to 50-80 DEG C at a certain heating rate, and keeping for 2-20 hours to obtain asphalt balls with a small amount of naphthalene or anthracene removed; then switching to inert gas containing organic solvent steam, and heating to the temperature for removing naphthalene or anthracene at a certain heating rate to obtain asphalt balls with naphthalene or anthracene completely removed; and finally, switching to air, and obtaining corresponding oxidized asphalt balls according to a conventional oxidation non-melting process.A liquid-phase organic solvent is not used, the reaction time is greatly shortened, the treatment range is wide, the cost is greatly reduced, and the operation is simple and convenient.

Description

technical field [0001] The invention relates to a pretreatment method for oxidation and non-melting of asphalt pellets, in particular to a method for removing naphthalene or anthracene in asphalt by gas or steam. Background technique [0002] Pitch-based spherical activated carbon is a high-performance activated carbon that is used in many fields. But it is essential that oxidation does not melt during its preparation. According to the research literature, it is known that the aromatic hydrocarbon mixture such as naphthalene or anthracene in the asphalt pellets must be extracted with an organic solvent before the oxidative non-melting process can be carried out. [0003] US Patent US 4,228,037 "Spherical activated carbon having low dusting property and high physical strength and process for producing the same", US Patent US 4,273,675 "Process for the preparation of spherical carbon preparticles and spherical activated carbon particles" and US Patent 1US 4,44 "Processing ca...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10C3/04C10C3/00
CPCC10C3/002C10C3/04
Inventor 李开喜
Owner SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI