A method for producing hydrocarbon products from a wide boiling range condensate, the method comprising the steps of: introducing the wide boiling range condensate and a combined hydrogen fraction into a hydroprocessing reactor of an aromatics production system, where a volume ratio of the combined hydrogen fraction to the wide boiling range condensate introduced is in a range of from 0.01 to 10, where the wide boiling range condensate comprises paraffins, naphthenes and aromatics, and where the combined hydrogen fraction comprises a make-up hydrogen and a recycled high-purity hydrogen; operating the aromatics production system under conditions such that the hydroprocessing reactor forms both a light product gas mixture and a naphtha boiling temperature range liquid product, whereby the hydroprocessing reactor operates at a hydrocracking severity such that paraffins, naphthenes and aromatics of the wide boiling range condensate that are introduced into the system and that exhibit a true boiling point temperature greater than 220°C are cracked and saturated into paraffins having a TBP temperature within a naphtha boiling temperature range, which is from 30°C to 220°C, where the light product gas mixture is predominantly a mixture of hydrogen and light alkanes in the methyl (C 1) to pentyl (C 5) hydrocarbon range; passing the naphtha boiling temperature range liquid product to an aromatization reactor system and the light product gas mixture passes to a hydrogen extraction unit; operating the aromatization reactor system under conditions appropriate for forming one or more hydrocarbon products and a hydrogen-rich gas product, where the hydrocarbon products comprise at least 30% by weight aromatics in the hexyl (C 6) to octyl (C 8) range, and where the hydrogen-rich gas product includes hydrogen and light alkanes; passing the hydrogen-rich gas product to the hydrogen extraction unit; producing the recycled high-purity hydrogen and a mixed hydrogen-poor gas in the hydrogen extraction unit by selectively separating hydrogen from the light product gas mixture and the hydrogen-rich gas product, wherein the mixed hydrogen-poor gas comprises no less than 70% by weight C 1 to C 5 alkanes; and passing the recycled high-purity hydrogen to the hydroprocessing reactor. introducing the wide boiling range condensate and a combined hydrogen fraction into a hydroprocessing reactor of an aromatics production system, where a volume ratio of the combined hydrogen fraction to the wide boiling range condensate introduced is in a range of from 0.01 to 10, where the wide boiling range condensate comprises paraffins, naphthenes and aromatics, and where the combined hydrogen fraction comprises a make-up hydrogen and a recycled high-purity hydrogen; operating the aromatics production system under conditions such that the hydroprocessing reactor forms both a light product gas mixture and a naphtha boiling temperature range liquid product, whereby the hydroprocessing reactor operates at a hydrocracking severity such that paraffins, naphthenes and aromatics of the wide boiling range condensate that are introduced into the system and that exhibit a true boiling point temperature greater than 220°C are cracked and saturated into paraffins having a TBP temperature within a naphtha boiling temperature range, which is from 30°C to 220°C, where the light product gas mixture is predominantly a mixture of hydrogen and light alkanes in the methyl (C 1) to pentyl (C 5) hydrocarbon range; passing the naphtha boiling temperature range liquid product to an aromatization reactor system and the light product gas mixture passes to a hydrogen extraction unit; operating the aromatization reactor system under conditions appropriate for forming one or more hydrocarbon products and a hydrogen-rich gas product, where the hydrocarbon products comprise at least 30% by weight aromatics in the hexyl (C 6) to octyl (C 8) range, and where the hydrogen-rich gas product includes hydrogen and light alkanes; passing the hydrogen-rich gas product to the hydrogen extraction unit; producing the recycled high-purity hydrogen and a mixed hydrogen-poor gas in the hydrogen extraction unit by selectively separating hydrogen from the light product gas mixture and the hydrogen-rich gas product, wherein the mixed hydrogen-poor gas comprises no less than 70% by weight C 1 to C 5 alkanes; and passing the recycled high-purity hydrogen to the hydroprocessing reactor.