Properties Of Gaseous Products Research Articles

Elucidation of synergistic effects in straw/sludge co-pyrolysis through gaseous product monitoring and biochar analysis

The environmental problems posed by the increasing global production of sludge highlight the need for efficient sludge treatment methods ideally affording value-added products, as exemplified by the co-pyrolysis of sludge and biomass. In this study, we aimed to investigate the effects of temperature (500, 600, 700, and 800 °C) and straw content (0, 25, 50, 75, and 100 wt%) on the properties of gaseous products and biochar during pyrolysis of sludge–straw mixtures in a fixed-bed reactor. Gas (e.g., CO2, CO, CH4, and H2) release increased with increasing temperature (up to 700 °C) and straw content, which was ascribed to the high content of volatiles in straw and its ability to act as a hydrogen source for sludge. The specific surface area and pore volume of biochar first decreased and then increased with increasing temperature, whereas the reverse was true for pore size. The synergy between sludge and straw, quantified as the difference between experimental and predicted biochar yields and specific surface areas, was maximized at a straw content of 75 wt% and was analyzed to design a pyrolysis product framework based on the circular economy concept. Thus, this study paves way for the effective utilization of sludge co-pyrolysis products and the preparation of mixed biochar, providing a reference for solid-waste treatment and efficient energy utilization.

Gaseous Fuels from Degraded Scrape Rubber and Used Lube Oil

The present investigation deals with the composition and properties of gaseous products of the oxidative cracking process that are applied to fulfill the disposal and utilization of shredded automotive tire scrape and spent lubricating oils mixed at different proportions. Cracking of these mixtures has been performed in an autoclave in an air atmosphere under a pressure of 7 atm, using 0.8 wt% phenols as a catalyst under different conditions of temperatures and time of reaction. The main products of pyrolysis are pyrolytic gases, pyrolytic oils and pyrolytic char. The gases were identified as C 1 , CO 2 , C 2 , C 3 , olefins C 4 , i-C 4 , n-C 4 , olefins C 5 , I-C 5 , n-C 5 , C 6 , and C 7 . Gas chromatography analysis showed that an increase in temperature and time of reaction led to an increase in the light fraction and decreases of the proportion of heavy fraction. The optimum cracking conditions were fulfilled when using oil-rubber ratio 1/0.5, and was, respectively, 0.7 Mpa air pressure, 450°C, and a reaction time of 45 min. The produced gases could be used as a natural gas in heating and as a chemical source based on calorific value and olefins content nature.