The invention discloses a
continuous production technology for
tetra-
aryl-bi-
metal porphyrin. The
continuous production technology is that a resolvent is fed into a heterogeneous reaction and separation synchronous reactor, wherein the reactor comprises a stirring reaction
tower and at least two constant-temperature
settling towers, the stirring reaction
tower comprises a reflow device, the constant-temperature
settling towers are communicated with the bottom of the stirring reaction
tower, and the interior of the stirring reaction tower comprises a gas-phase area and a reaction area; during reaction, the reaction area and the constant-temperature
settling towers are full of the resolvent, and reaction raw materials such as
tetra-
aryl-
porphin and
divalent metal salt are fed into the stirring reaction tower and react with air led into the stirring reaction tower when the reaction area and the constant-temperature settling towers are heated to the
backflow temperature of the resolvent; the
tetra-
aryl-bi-
metal porphyrin generated during the reaction settles directly under the actino of gravity and enters into a constant-temperature settling tower from the reaction area; when the constant-temperature settling tower is fully filled with the tetra-aryl-bi-metal
porphyrin, the stirring reaction tower is switched to be communicated with the other constant-temperature settle tower fully filled with the resolvent; the steps are carried out alternately to ensure
continuous production. The technology can be used for producing high-purity tetra-aryl-bi-metal porphyrin continuously with high yield and low cost.