| CPC B01J 19/0033 (2013.01) [B01J 19/0013 (2013.01); B01J 19/2415 (2013.01); C01B 3/34 (2013.01); B01J 2219/00157 (2013.01); B01J 2219/00162 (2013.01); B01J 2219/00164 (2013.01); C01B 2203/0233 (2013.01); C01B 2203/0283 (2013.01); C01B 2203/042 (2013.01); C01B 2203/061 (2013.01); C01B 2203/068 (2013.01); C01B 2203/0816 (2013.01); C01B 2203/1604 (2013.01); C01B 2203/1609 (2013.01); C01B 2203/1619 (2013.01); C01B 2203/1633 (2013.01)] | 19 Claims |

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1. A method for starting a steam reformer arrangement up to a normal operating state, the steam reformer arrangement comprising a reactor comprising reformer tubes and a plurality of burners, the plurality of burners comprising a first group of pilot burners, a second group of startup burners, and third group of non-startup burners, the steam reformer arrangement configured for production of hydrogen, methanol, ammonia, or synthesis gas, the method comprising:
controlling and regulating burners that are coupled to a reactor comprising reformer tubes, wherein startup is performed and regulated in an automated manner by the non-startup burners that ensure normal operation, wherein the non-startup burners are ignited indirectly as a function of temperature by the pilot burners and the startup burners provided specifically for startup, as a function of at least one of automatically evaluated flame monitoring or temperature monitoring at least with respect to the pilot burners.
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