The utility model belongs to the technical field of
carbon dioxide hydro-conversion, particularly relates to a
membrane reactor for a reaction-separation
coupling process, and aims to solve the problem of performance failure of the
membrane reactor in a high-temperature environment in the background technology, the following scheme is provided: the
membrane reactor comprises a
reaction tube body, end covers are screwed on the outer walls of two ends of the
reaction tube body, and the end covers are screwed on the outer walls of two ends of the
reaction tube body; a
product gas outlet is welded to one end of the outer wall of the bottom of the reaction tube body, a feed gas inlet is welded to the other end of the outer wall of the top of the reaction tube body, and a purge gas outlet is welded to the outer wall of one side of one end cover. The NaA
molecular sieve membrane loaded by the
ceramic hollow
fiber carrier is adopted, a compact and defect-free
zeolite membrane layer is formed through a multi-time in-situ growth process, the membrane can still keep a stable hydrophilic nano channel (the aperture is 0.4 nm) at the temperature of 300-400 DEG C and the
high pressure of 4 MPa, water molecules are preferentially adsorbed and permeated, the
thermodynamic equilibrium limitation is effectively broken, and compared with a traditional
molecular sieve membrane, the membrane has the advantages that the membrane is simple in structure and convenient to use, and the cost is low. The
thermal stability is obviously improved.