Modelling exo- and endotermic reactions with heat transfer wall in modernized reactor of conversion of methane

Are considered modeling process of secondary steam conversion of methane in a mine reactor with use of the special amalgamator located in the top zone of a reactor. In the amalgamator there is exothermal reaction for reception of thermal energy necessary for carrying out endothermal reaction for conversion of methane, that essentially raises economy of a source of raw materials and reduces powerarrying out of process as the part of technological gas is not used ass a source of thermal energy. For an intensification of process plans of transfer of thermal energy through a metal partition with a parallel stream of reacting gas streams and a countercurrent when in one stream reaction proceeds exothermic, and in other endothermic are considered.