A method for controlling a hydrocarbon steam reforming process carried out in a combustion chamber comprising burners and tubes, the tubes being filled with catalyst and being capable of being passed through by a mixture of hydrocarbons and steam, the burners being positioned so as to transfer the heat from their combustion to the mixture of hydrocarbons and steam through the wall of the tubes, in which the wall temperature T of each tube is measured, preferably in the downstream part of the tube, wherein when, for at least one tube, the temperature measured T is greater than or equal to the maximum operating temperature of the tubes, then at least one operating parameter of the reforming process is modified so as to lower the temperature measured T of this tube to a value below the maximum operating temperature of the tubes equal to the design temperature of the tube −15° C.