采用绝热固定床积分反应器，在工业条件下（５００ｈ － １ ，２ ．６ ＭＰａ） ，对条形ＦｅＣｕＫ 工业催化剂进行了ＦＴ合成反应性及宏观动力学考察。在稳态下，用集总的方法，保持一定的轴向温度分布及均温下，求得的宏观动力学方程，与实验数据符合较好。 Adopting adiabatic fixed-bed integral reactor, FT synthesis reaction and macro-kinetic investigation of bartype FeCuK industrial catalyst under industrial conditions (500h - 1, 2. 6 MPa) were carried out. In the steady state, using the lumped method to maintain a certain axial temperature distribution and the average temperature, the obtained macroscopic kinetic equation, in good agreement with the experimental data.