Integrated process and apparatus for the primary and secondary c

Compositions – Gaseous compositions – Nitrogen and hydrogen containing

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252373, 423359, 423652, C01B 113

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048225215

ABSTRACT:
Integrated primary-secondary reforming operations are carried out with the partly reformed product effluent from the reformer tubes of the primary reforming zone passing to a catalyst-free reaction space at the feed end of a catalyst bed in the secondary reforming zone. The exothermic heat of reaction generated in said reaction space supplies the necessary heat for the endothermic reforming reaction that occurs in the catalyst bed of the secondary reforming zone, and the still hot secondary product effluent leaving the secondary reforming zone is passed in the shell side of the primary reformer zone to supply the endothermic heat of reaction required in said primary reforming zone. Essentially autothermal operating conditions are thereby achieved so as to essentially eliminate the necessity for employing an external fuel-fired primary reformer and/or for consuming a portion of the hyrocarbon feed material for fuel purposes.

REFERENCES:
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patent: 3397962 (1968-08-01), Squires
patent: 3442613 (1969-05-01), Grotz
patent: 4079017 (1978-03-01), Crawford et al.
patent: 4264066 (1966-08-01), Quartulli et al.
patent: 4296085 (1981-10-01), Banquy
patent: 4337170 (1982-06-01), Fuderer
patent: 4391794 (1983-07-01), Skberring
patent: 4479925 (1984-10-01), Shires et al.
Oil and Gas Journal, Dec. 12, 1977, pp. 81-84, Author-George Friedman .

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