ONE OF THE BEST METHODS FOR CONSTRUCTING A PILOT PLANT OF PLUG AND PACKED BED FLOW REACTOR IS TO SCALE DOWN THE DIMENSIONS OF AN INDUSTRIAL ONE. IN THIS REGARD, THE FIRST STEP IS TO SIMULATE THE REACTIONS OF THE INDUSTRIAL EQUIPMENT BY EMPLOYING PROPER KINETIC EQUATIONS AND THEN SCALE DOWN ALL THE DIMENSIONS WITH DIFFERENT SCALING FACTOR IN ORDER TO FIND OUT THE SMALLEST POSSIBLE DIMENSIONS FOR THE PHYSICAL MODEL. IN THIS PAPER ATTEMPTS WERE MADE TO FIND OUT THE PROPER DIMENSIONS OF PHYSICAL MODEL, OF A CATALYTIC NATURAL GAS REFORMER PILOT BASED ON THE INDUSTRIAL REFORMER WHICH IS CURRENTLY OPERATES AT GHADIR IRON AND STEEL COMPANY IN IRAN. IN THIS REGARD, THE SIMULATION OF REFORMING, WATER-GAS SHIFT AND METHANATION REACTIONS ON THE NI/ AL2O3 CATALYST, WITH THE OPERATIONAL CONDITION DATA WAS PERFORMED WITH ASPEN-HYSYS SOFTWARE. THE RESULTS SHOWED THAT SINCE THE REFORMING REACTIONS ARE SO FAST, THE KINETICS OF THE REACTIONS IS NOT MUCH DEPENDENT ON THE TUBE REACTOR DIMENSIONS AND THEREFORE THE DIMENSION OF THE PHYSICAL MODEL OF THE REFORMER IS NOT AN ISSUE IN DESIGNING A PHYSICAL MODEL.