Method for preparing fuel oil and carbon black by low-temperature catalytic pyrolysis of automobile waste tires
A technology for low-temperature catalysis and waste tires, which is applied in the petroleum industry, treating hydrocarbon oil, and fibrous fillers. It can solve the problems of slow reaction rate, land occupation, and high cracking temperature, and achieves less catalyst consumption, greater economic value, and The effect of high carbon black quality
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment 1
[0020] Separate the waste tires from the steel wires and crush them into waste rubber particles of 5-30 meshes, add 0.3% nickel chloride to mix with them, then add them to the cracking furnace, and heat them at a temperature of 400°C and a pressure of 0MPa-0.01MPa. Cracking for 30 minutes, the high-temperature oil gas and fine carbon black produced during the cracking process are discharged from the oil and gas outlet of the cracking furnace, enter the high-temperature gas-solid separator, and separate high-temperature oil gas and fine carbon black, and the high-temperature oil gas enters the fractionating tower to condense to obtain fuel oil. The coarse carbon black in the cracking slag produced in the cracking furnace is discharged from the slag outlet of the cracking furnace, crushed into fine carbon black, and mixed with the aforementioned fine carbon black to obtain a carbon black product. The yield of pyrolysis products is: fuel oil 42%, carbon black 36%.
Embodiment 2
[0022] Separate the waste tires from the steel wires and crush them into 5-30 mesh waste rubber particles, add 0.5% nickel chloride to mix with them, and then add them to the cracking furnace at a temperature of 450°C and a pressure of -0.01MPa to 0MPa. Thermal cracking for 35 minutes. The high-temperature oil gas and fine carbon black produced during the cracking process are discharged from the oil and gas outlet of the cracking furnace and enter the high-temperature gas-solid separator to separate high-temperature oil gas and fine carbon black. The coarse carbon black in the pyrolysis slag produced in the process is discharged from the slag outlet of the pyrolysis furnace, crushed into fine carbon black, and mixed with the aforementioned fine carbon black to obtain a carbon black product. The yield of pyrolysis products is: fuel oil 49%, carbon black 33%.
Embodiment 3
[0024] Separate the waste tires from the steel wires and break them into 5-30 mesh waste rubber particles, add 0.8% nickel chloride to mix with them, and then add them to the cracking furnace for thermal cracking at a temperature of 520°C and a pressure of -0.01MPa For 40 minutes, the high-temperature oil gas and fine carbon black produced during the cracking process are discharged from the oil and gas outlet of the cracking furnace and enter the high-temperature gas-solid separator to separate high-temperature oil gas and fine carbon black. The high-temperature oil gas enters the fractionation tower to condense to obtain fuel oil. The coarse carbon black in the generated pyrolysis slag is discharged from the slag outlet of the cracking furnace, crushed into fine carbon black, and mixed with the aforementioned fine carbon black to obtain a carbon black product. The yield of pyrolysis products is: fuel oil 52%, carbon black 35%.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More