The invention relates to a low-temperature
distillation and liquefying separation
recovery system and method for
coal bed gas high in
nitrogen content,
oxygen content and
hydrogen content. The low-temperature
distillation and liquefying separation
recovery system is provided with a cold box, a heavy
hydrocarbon separation tank, a rectifying
tower, an LCPM
storage tank, a
refrigerant compressor, a cooler, a final-stage gas-liquid separator, a
flash gas compressor and a
flash gas cooler. The low-temperature
distillation and liquefying separation
recovery method of the
coal bed gas high in
nitrogen content,
oxygen content and
hydrogen content comprises the steps that heavy
hydrocarbon separation and
liquefaction are conducted on feedstock gas after the feedstock gas is pre-cooled through a pre-cooling section of the cold box; the liquefied feedstock gas enters the rectifying
tower for
nitrogen removal,
oxygen removal and
hydrogen removal, and then the liquefied feedstock gas returns into the cold box to be further cooled and then enters the LCPM
storage tank; after the gas mixed with refrigerants is compressed and cooled by two stages, the liquid-phase
refrigerant separated by the final-stage gas-liquid separator is used for providing cold energy for the pre-cooling section of the cold box; the gaseous-phase
refrigerant obtained after separation is used for providing cold energy for the liquefying section and the
supercooling section of the cold box; purge gas is heated and then completely exhausted; and
flash gas is pressurized and returns to the liquefying section of the cold box to be liquefied again after heat exchange is conducted between the flash gas and the liquid-phase refrigerant. By the adoption of the low-temperature distillation and liquefying separation recovery
system and method, the recovery rate of
methane can be increased, so that the
processing capacity of a device is improved, the
energy consumption of the system is reduced, and the production cost is reduced.