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Tubular heating furnaces are used as process heating equipment in the petrochemical industry. Generally, the radiant furnace tube is supported on the furnace wall of the radiant section of the heating furnace through the furnace tube hanger.
In general, the design temperature of the pipe frame and the furnace tube guide frame in contact with the flue gas shall be determined according to the operating conditions of the heating furnace in accordance with the following provisions: a) The supporting parts located in the radiation section, the shielding section and exposed to refractory materials, equal to the flue gas temperature plus 100 ° C (180 ° F) and the minimum design temperature is not less than 870 ° C (1600 ° F); b) Support parts located in the convection section equal to the contact flue gas temperature plus 55 ° C (100 ° F); c) The flue gas temperature gradient across each convective intermediate tube plate shall not exceed 222 ° C (400 ° F); d) The cast radiant tube frame shielded by the tube row can adopt the fire wall temperature. The protective effect of covering the intermediate pipe frame or furnace pipe guide frame with refractory material should be ignored.
The furnace tube guide frame, the middle tube frame of the horizontal radiation tube, and the top tube frame of the vertical radiation tube shall be designed to allow the replacement of the tube frame without moving the furnace tube, and the minimum amount of fire layer repair.
The maximum suspended length of the furnace tube between the two supporting points of the horizontal tube is 35 times the outer diameter of the furnace tube or 6m(20ft), which is the smaller value.
The minimum surface corrosion margin for all pipe and guide frames in contact with flue gas is: 1.3mm(0.05in) for austenitic materials; Ferrite material 2.5mm(0.1in).
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