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Corrugated cardboard (CCB) comprises a substantial portion of municipal solid waste, of which ~5% is wax coated CCB (WCCB) to enhance its performance. WCCB cannot be recycled, making it a suitable resource to recover wax and produce char. The WCCB was characterized for its extractable wax, lignin, and carbohydrate contents and by thermogravimetric analysis to study its thermal degradation behavior. WCCB was preliminarily examined by pyrolysis‐gas chromatography–mass spectrometry to determine product composition. WCCB samples were then pyrolyzed in auger and tube reactors at 450, 500, and 550°C, and their pyrolysis wax‐oil and char products characterized. WCCB and char were subjected to proximate, ultimate, surface area, analyses. The highest char yield was 36% at 450°C, and the highest wax‐oil yield was 53% at 550°C in the tube reactor. The wax‐oil fraction contained mainly alkanes, alkenes, and dienes (C9–C36), and chain length decreased with pyrolysis temperature. This wax fraction could be recovered and used as bunker fuel (C12–C40) or further converted to diesel (C10–C20). [ABSTRACT FROM AUTHOR]

A novel silica nanospring (NS) supported cobalt catalyst for Fischer-Tropsch synthesis (FTS) was synthesized and investigated, and the results were compared with those of a conventional cobalt catalyst. The NS catalyst was prepared using deposition of Co followed by thermal assisted reduction and characterized by scanning electron microscopy-energy dispersive spectroscopy, transmission electron microscopy, N2 physisorption, X-ray powder diffraction, X-ray photoelectron spectroscopy, and H2-temperature programmed reduction. FTS performance was evaluated in a quartz fixed-bed microreactor (230°C, H2:CO ratio 2:1), and the products were trapped and analyzed with gas chromatography-thermal conductivity detector (GC-TCD, gases) and gas chromatography-mass spectrometry (GC-MS, semivolatiles) to determine the percentage of CO conversion and selectivity. Semivolatile products from both catalysts were C6-C18 hydrocarbons. Even though the NS FTS catalyst was not fully reduced during the activation period it still showed higher FTS activity than the conventional catalyst, which is attributed to the higher accessibility of the gases to the Co on the NS surface. © 2013 American Institute of Chemical Engineers Environ Prog, 33: 693-698, 2014 [ABSTRACT FROM AUTHOR]