Petroleum-containing residue processing via co-catalyzed pyrolysis

Chalov, K.V.; Lugovoy, Yury V.; Kosivtsov, Yu. Yu.; Stepacheva, Аntonina A.; Sulman, Mikhail G.; Молчанов, В. П.; Smirnov, I. S.; Panfilov, Victor; Sulman, Esther M.

doi:10.1016/j.fuel.2016.08.055

Cited by 13 publications

(5 citation statements)

References 18 publications

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“…The solid residue obtained from the pyrolysis of HFO and VRO conformed to the amount of fixed carbon present in the HFO and VRO, and the amount of char obtained followed the trend HFO (10.77 wt.%) < VRO (14.08 wt.%). Chalov et al[34] investigated the pyrolysis of oil residue in the temperature range of 500-750 °C and observed similar trends for liquids and gases. It can be noted that the consistency in the liquid and char yield after 800 °C suggested that increment in conversions of HFO and VRO cannot be achieved by increasing the temperature further.…”

mentioning

confidence: 83%

On the Products from the Pyrolysis of Heavy Fuel and Vacuum Residue Oil

Gautam¹,

Alabbad²,

Guevara³

et al. 2023

Preprint

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mentioning

confidence: 83%

On the Products from the Pyrolysis of Heavy Fuel and Vacuum Residue Oil

Gautam¹,

Alabbad²,

Guevara³

et al. 2023

Preprint

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“…The analysis of the liquid phase of the pyrolysis products obtained at 600°C was performed using GCMS-QP2010S (SHIMADZU, Japan) according to the procedure described elsewhere [34]. The summarized results are presented in Fig.…”

Section: Pyrolysis Product Analysismentioning

confidence: 99%

Product Comparison for Slow and Fast Pyrolysis of Flax Shive

Lugovoy¹,

Chalov²,

Stepacheva³

et al. 2022

Preprint

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In the current work, a comparison of the composition and properties of products obtained by the slow and fast pyrolysis of flax shive is presented to evaluate the influence of the process mode on the thermal decomposition of agricultural waste. The thermogravimetric studies were carried out to estimate the temperature range of the decomposition of the feedstock main component (cellulose, hemicelluloses, and lignin) and to choose the pyrolysis temperature. It was found that the slow pyrolysis was found to provide the higher conversion depth of the feedstock resulting in the formation of gaseous and liquid products with higher calorific values (9.65 MJ/m3, and 16.51 MJ/kg respectively). Moreover, the solid residue of the slow pyrolysis was characterized by the higher surface area and narrow pore size distribution in comparison with that obtained by the fast process.

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“…Analysis of the liquid pyrolysis products was performed using GCMS-QP2010S (Shimadzu, Japan) according to the procedure described in [32]. The concentration of the components in the liquid phase was determined with diphenylamine as the external standard.…”

Section: Fast Pyrolysis Proceduresmentioning

confidence: 99%

Fast Pyrolysis of Flax Shive in a Screw‐Type Reactor

et al. 2021

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A novel screw-type reactor for the fast pyrolysis of agricultural waste (flax shive) is described. A preliminary study on the influence of process parameters on the yield, composition, and properties of pyrolysis products was carried out. Based on the results obtained, the optimal conditions of fast pyrolysis of flax shive particles in terms of feedstock particle size, solid residence time, and process temperature were identified. Considering the construction, the developed reactor seems to be close to the screw fluidized bed and auger reactor and is characterized by a simple design and operation control. Moreover, the proposed reactor can be used for continuous pyrolysis without any significant modification.

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Petroleum-containing residue processing via co-catalyzed pyrolysis

Cited by 13 publications

References 18 publications

On the Products from the Pyrolysis of Heavy Fuel and Vacuum Residue Oil

On the Products from the Pyrolysis of Heavy Fuel and Vacuum Residue Oil

Product Comparison for Slow and Fast Pyrolysis of Flax Shive

Fast Pyrolysis of Flax Shive in a Screw‐Type Reactor

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