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DEVELOPMENT OF CONSTRUCTION OF A CATALYTIC REACTOR FOR METHANE OXIDISING IN VENTILATION AIR IN COAL MINES AND THE RESEARCH ON INTEGRATED “HEAT PIPE” RECUPERATOR

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Figure

Fig. 1. The schemes of construction and typical temperature courses of monolith reactors (CMR): a) classical and b) reverse flow; To – input temperature, Ti – initiation temperature, Tmax – maximum temperature, T1 – output temperature, ΔTlad = T1 – To [2]
Fig. 3. Single section of the “heat pipe” exchanger
Fig. 4. The scheme of test bench for examining “heat pipe” exchangers
Fig. 5. The relation between initial temperature of heat absorbing agent Tpwy and the obtained usable power Quż to the volumetric expense of the agents

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