Carbon dioxide sequestration through novel use of ion exchange fibers (IX-fibers)

Denitrification of nitrate in regeneration waste brine using hybrid cation exchanger supported nanoscale zero-valent iron with/without palladium nanoparticles

The Sustainable Development Goals require that reducing waste is a priority. This work described the application of an innovative zero-waste hybrid ion exchange nanotechnology that concurrently removed nitrate and induced denitrification to ammonia, with the ability to generate fertilizer for the agriculture sector from the recycled by-products. Herein, hybrid cation exchanger-supported zero-valent iron (Fe⁰), and bimetallic Fe⁰/Pd nanoparticles (HCIX-Fe⁰ and HCIX-Fe⁰/Pd) were synthesized and successfully validated for denitrification of nitrate in spent waste brine that contained nitrate. The kinetics of nitrate catalysis by both HCIX-Fe⁰ and HCIX-Fe⁰/Pd were compared and presented by six kinetic models, namely, zero-order, pseudo first- and second-order reaction, pseudo first- and second-order adsorption, and Elovich. HCIX-Fe⁰/Pd displayed a higher kinetic value than HCIX-Fe⁰, with k₁ of 0.0019 and 0.0026 min^-1, respectively. Nitrate was predominantly catalysed to NH₄⁺ at a ratio of ammonia to other nitrogen compounds of around 80:20. Although HCIX-Fe⁰/Pd showed slightly better (14%) kinetic results, it was determined as unfavourable for real-life application due to low selectivity toward N₂ gas and the need to use H₂ gas. Based on practicability, the HCIX-Fe⁰ was further validated. The effect of salt (using NaCl) and the role of initial pH conditions were optimized and discussed. The recovery of nitrate removal was also calculated, and a recovery range of 91.42-99.14% was obtained for three consecutive runs. The sustainable, novel, zero waste hybrid ion exchange nanotechnology using the combination of two fixed-bed columns containing nitrate-selective resin for nitrate removal and novel HCIX-Fe⁰ for nitrate reduction to NH₄⁺ may be a promising sustainable solution toward the goal of discharging zero nitrate waste to the environment.

Aluminum-Cycle Ion Exchange Process for Hardness Removal: A New Approach for Sustainable Softening

From a sustainability viewpoint, sodium exchange softening, although used widely, is under scrutiny due to its production of excess Na-laden spent regenerant and subsequent discharge to the environment. Many arid regions are introducing regulations disallowing dumping of concentrated sodium salts, the residuals from popular Na-exchange softening. The sodium content of the softened water is, also, always higher than in the feed, which poses a dietary health concern when used for drinking or cooking. An efficient, easy-to-operate hardness removal process with reduced sodium in both the treated water and in the spent regenerant is an unmet global need. Use of a cation exchange resin in Al³⁺-form for hardness removal, that is, exchange of divalent Ca²⁺ or Mg²⁺ with trivalent Al³⁺, is counterintuitive, and this is particularly so, because the aluminum ion to be exchanged has higher affinity than calcium. Nevertheless, ion exchange accompanied by precipitation of aluminum hydroxide allows progress of the cation exchange reaction leading to hardness removal. Experimental results demonstrated that calcium can be consistently removed for multiple cycles using a stoichiometric amount of AlCl₃ as the regenerant. The process essentially operates at the maximum possible thermodynamic efficiency: removal of one equivalent of Ca²⁺ corresponds to use of one equivalent of Al³⁺ as a regenerant. During the Al-cycle process there is no increase in Na⁺ concentration and partial reduction in the total dissolved solids (TDS) of the treated water. It is noteworthy that the ion-exchange resin used, components of the fixed-bed column and operational protocol are nearly the same as traditional softening processes on Na-cycle. Thus, existing Na-cycle systems can be retrofitted into Al-cycle operation without major difficulty.