The present invention discloses a method for continuously co-producing HFO1234ze and HCFO1233zd (E, Z), which comprises the following steps: using a catalyst, HF and R240fa as the bottom materials, wherein the catalyst includes an amine catalyst and a co-catalyst, controlling the
reaction temperature and pressure in the reactor, and then continuously introducing HF and R240fa for fluorination reaction, and continuously extracting the products containing HFO1234ze and HCFO1233zd (E, Z). By introducing the amine catalyst and the co-catalyst, the
present method constructs a homogeneous near-
ionic liquid system, enabling the full fusion of the organic phase and the inorganic phase, improving the reaction efficiency, having a high total product yield, having a simple and
direct process route, having an
advantage in industrial production cost, having the reaction products and intermediates mainly existing in the form of olefin compounds, reducing the by-products of the fluorination reaction, reducing the purification difficulty and the equipment cost, and having a continuous, stable, safe and controllable reaction process.