A process for producing syngas, comprising: introducing a first hydrocarbon via a line and an oxidant via a line to one or more catalytic partial oxidation (CPOX) reactors, partially oxidizing the first hydrocarbon in the presence of an oxidant and one or more first catalysts in the CPOX reactor(s) at conditions sufficient to partially combust a portion of the first hydrocarbon to provide carbon dioxide, non-combusted first hydrocarbon, and heat; reforming at least a portion of the non-combusted first hydrocarbon in the presence of at least a portion of the heat generated in the partial oxidation step and the one or more first catalysts in the CPOX reactor(s), as the partially combusted first hydrocarbon flows through/across one or more first catalyst zones (155, 157) to provide a first syngas comprising hydrogen, carbon monoxide, and carbon dioxide; introducing the first syngas via a line to the shell-side or the tube-side of one or more reforming exchangers; introducing a second hydrocarbon, which is mixed with steam via a line to the one or more reforming exchangers via a line; indirectly exchanging heat from the first syngas to a second hydrocarbon to reform at least a portion of the second hydrocarbon in the presence of steam and one or more second catalysts to provide a second syngas comprising hydrogen, carbon monoxide, and carbon dioxide; reacting at least a portion of the carbon monoxide in the first syngas, the second syngas, or a mixture thereof to carbon dioxide to provide a converted syngas comprising 5% mol dry basis or less carbon monoxide, separating at least a portion of the hydrogen from the converted syngas gas to provide a hydrogen product. introducing a first hydrocarbon via a line and an oxidant via a line to one or more catalytic partial oxidation (CPOX) reactors, partially oxidizing the first hydrocarbon in the presence of an oxidant and one or more first catalysts in the CPOX reactor(s) at conditions sufficient to partially combust a portion of the first hydrocarbon to provide carbon dioxide, non-combusted first hydrocarbon, and heat; reforming at least a portion of the non-combusted first hydrocarbon in the presence of at least a portion of the heat generated in the partial oxidation step and the one or more first catalysts in the CPOX reactor(s), as the partially combusted first hydrocarbon flows through/across one or more first catalyst zones (155, 157) to provide a first syngas comprising hydrogen, carbon monoxide, and carbon dioxide; introducing the first syngas via a line to the shell-side or the tube-side of one or more reforming exchangers; introducing a second hydrocarbon, which is mixed with steam via a line to the one or more reforming exchangers via a line; indirectly exchanging heat from the first syngas to a second hydrocarbon to reform at least a portion of the second hydrocarbon in the presence of steam and one or more second catalysts to provide a second syngas comprising hydrogen, carbon monoxide, and carbon dioxide; reacting at least a portion of the carbon monoxide in the first syngas, the second syngas, or a mixture thereof to carbon dioxide to provide a converted syngas comprising 5% mol dry basis or less carbon monoxide, separating at least a portion of the hydrogen from the converted syngas gas to provide a hydrogen product.