Daytime radiative cooling technology can release heat
into outer
space without consuming any electricity during the day while reflecting
as much solar radiation as possible. This characteristic gives radiative
cooling materials considerable application potential in the fields
of energy-saving buildings, fabrics, and photovoltaic cells. The radiative
cooling coating (RC coating) applied to a building should cover a
large area of the building surface, so a RC coating was prepared by
spraying. The RC coating consisted of highly near-infrared reflective
yttrium oxide (Y2O3), titanium dioxide (TiO2), and polydimethylsiloxane (PDMS). The RC coating could reach
a high solar reflectance of 92.2% and a high atmospheric window emissivity
of 94.9%. The complementary reflectivity of TiO2 and Y2O3 was the key to obtaining high reflectivity for
RC coatings. The results of field tests showed that the cavity where
the RC coating is cooled was 7.7 °C lower than the ambient temperature
under direct sunlight. Moreover, the average radiative cooling power
of the RC coating was 72.5 W/m2 on a hot summer day. In
addition, the RC coating has good stability and thus can be used in
various conditions, such as on outdoor buildings.
An effective strategy for achieving cost-effective and environmentally friendly desulfurization wastewater in coal-fired power plants involves the incorporation of desulfurization wastewater into the slag water system. The objective of this study was to analyze the corrosion behavior of Q235-A slag-picker shell material upon the introduction of FGD wastewater into the slag water system. The dynamic weight loss method, electrochemical testing method and microscopic phase characterization were employed to investigate the impact of varying chloride ion concentrations (ranging from 1000 mg/L to 30,000 mg/L) of flue gas desulfurization wastewater (FGD wastewater) on the corrosion of Q235-A slag-picker shell material. The test results indicate that as the concentration of chloride ions increases, the corrosion rate increases from 1.1487 mm/a to 1.5590 mm/a when the concentration is less than 10,000 mg/L. However, when the concentration exceeds 10,000 mg/L, the corrosion rate decreases from 1.559 mm/a to 1.0393 mm/a. The corrosion rate is above 1 mm/a at all concentrations. As the Cl− concentration, the quality of the corrosion product film initially increases and then decreases. The primary components of the corrosion product are α- FeOOH, γ-FeOOH, β-FeOOH, Fe3O4 and γ-Fe2O3.
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