4.6 Article

Steam Pyrolysis of Oil Sludge for Energy-Valuable Products

期刊

APPLIED SCIENCES-BASEL
卷 12, 期 3, 页码 -

出版社

MDPI
DOI: 10.3390/app12031012

关键词

oil sludge; steam pyrolysis; semi-coke; non-condensable gas; liquid hydrocarbons; spray; combustion

资金

  1. Ministry of Science and Higher Education of the Russian Federation [075-00268-20-02, 0718-2020-0040]
  2. Russian Federal budget [075-GZ/X4141/687/3, 075-03-2021-138/3]

向作者/读者索取更多资源

Experimental studies were conducted on the steam pyrolysis of oil sludge using a flowtype pilot plant. Valuable energy products including liquid hydrocarbons, semi-coke, non-condensable gas-phase compounds, and bitumen were obtained. The physicochemical characteristics, atomization process, droplet ignition, and combustion of the liquid hydrocarbons were comprehensively studied. This study is of great importance for the design of new installations and technological systems for hydrocarbon pyrolysis.
Experimental studies of the steam pyrolysis of oil sludge were performed using a flowtype pilot plant with 300 kg/h capacity (raw material) to obtain energy-valuable products, such as liquid hydrocarbons (30.4 wt%), semi-coke (39.6 wt%), non-condensable gas-phase compounds (26.5 wt%), and bitumen (3.5 wt%). The pyrolysis process was conducted at a temperature of 650 ffi C and with a steam flow rate of 150 kg/h. Liquid hydrocarbons were considered a target product. Comprehensive studies of their physicochemical characteristics, atomization process, droplet ignition, and combustion were carried out. The studied sample had physicochemical characteristics similar to traditional fuel oil (calorific value-42.6 MJ/kg, sulfur content-0.8 wt%). The jet spraying angle was 25 degrees in view of the improved rheological properties of the test sample, with a homogeneous jet structure and a predominant droplet diameter of no more than 0.4 mm. The flame combustion process was accompanied by the formation of microexplosions, the frequency and intensity of which depended on the temperature of the air (Tg = 450-700 degrees C). This study, in view of its applied nature, is of interest in the design of new installations and technological systems for hydrocarbon pyrolysis.

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