Journal
JOURNAL OF ENVIRONMENTAL CHEMICAL ENGINEERING
Volume 10, Issue 3, Pages -Publisher
ELSEVIER SCI LTD
DOI: 10.1016/j.jece.2022.107932
Keywords
Coal to ethyl glycol; Boron-doped; Activated carbon; Catalyze; Reduction of nitric acid
Categories
Funding
- Joint Research Fund of Fujian Institute of Research on the Structure of Matter & Institute of Urban Environment [RHZX-2019-007]
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Coal to ethylene glycol (CTEG) technology has gained increasing attention in the past decades. The production of nitric acid (NA) as a by-product during the oxidative esterification reaction can cause equipment corrosion and increase nitrogen replenishment and wastewater treatment costs. This study demonstrates the use of non-metallic B doped activated carbon (B-AC) as a catalyst to reduce NA in the CTEG process. The structure and physicochemical properties of B-AC were examined, and its catalytic performance and stability were evaluated. Results show that B-AC exhibits higher activity compared to pure activated carbon (AC) and has potential as a catalyst for reducing NA wastewater.
Coal to ethylene glycol (CTEG) technology has attracted more and more attention in the past decades. However, the by-production of nitric acid (NA) during oxidative esterification reaction not only causes equipment corrosion but also increases the cost of nitrogen replenishment and wastewater treatment, therefore it is meaningful to convert NA to useful feedstock. Herein, non-metallic B doped activated carbon (B-AC) was prepared and used to activate the reduction of NA. The structure and physicochemical properties of B-AC were firstly examined by SEM, ICP-OES, N-2 adsorption and desorption isotherms, FT-IR, Raman, and XPS spectrum. Furthermore, the catalytic performance and stability of B-AC were evaluated in the batch experiments. Results showed that BET surface area and pore volume of B-AC decreased with the increase of B doping amount, and the content of BC3 component enhanced with the increase of calcination temperature. B-AC-800(10) with the mass ratio of AC to BA of 10 and the calcinated temperature of800 degrees C performed the best activity with about 85% and 66% conversion under 2% and 5% of NA solution, and each catalytic performance of B-AC is about 10% higher than pure AC. The slight blockage of pore structure due to the residual NA and the fall of B atoms from B-AC together lead to a decline of about 20% in NA conversion after five cycles. These findings indicated the application of B-AC as a promising catalyst to reduce NA wastewater in the CTEG process.
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