Abstract

In this paper, we have shown that the possibility of increasing the productivity of viscous hydrocarbon liquids gasification in the filtration combustion mode with superadiabatic heating can be achieved by increasing the gaseous oxidant consumption. The addition of steam to the gaseous oxidizer has allowed the combustion heat of gaseous products to be increased, while the maximum combustion temperature has remained fairly high for the complete and efficient processing of fuel. The increase in the coal content in the charge has ensured an increase in the maximum combustion temperature, which has in turn contributed to the more stable course of the process and has also lead to an increase in the calorific capacity of the product gas.

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