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Lee, Jaewon; Cho, Hyungtae; Kim, Myungjun; Hall, Steve; Moon, Il
Industrial & engineering chemistry research, 10/2020, Letnik: 59, Številka: 40Journal Article
A novel design of a double-tube steam methane reforming (SMR) reactor was evaluated in terms of conversion and reactor temperature, compared with the conventional, single-tube, fixed bed reactor. The heat from the reformate could be recovered through the double-tube reactor, which increased the conversion from 71.7 to 89.3% and lowered the reactor outlet temperature from 732.7 to 674.5 °C. An actual plant was then designed, wherein the entire operating process was tested using the double-tube reactor, which produced 100 N m3/h of pure hydrogen. Last, to maximize the thermal efficiency and to achieve a hydrogen-production rate of >100 N m3/h, the operating conditions were optimized with the decision variables and constraints based on actual operating experiences. Consequently, our developed optimal SMR system gave a thermal efficiency of 81.3%, higher than that of the current commercial products (approximately 70%), and achieved a hydrogen-production rate of 124.8 N m3/h.
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Leto | Faktor vpliva | Izdaja | Kategorija | Razvrstitev | ||||
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JCR | SNIP | JCR | SNIP | JCR | SNIP | JCR | SNIP |
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in: SICRIS
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