Droplet-impingement, flow-assisted electro-fenton purification using heterogeneous silica/iron nanocomposite catalyst

Pending Publication Date: 2020-10-08
KING FAHD UNIVERSITY OF PETROLEUM AND MINERALS
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  • Abstract
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  • Claims
  • Application Information

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Benefits of technology

[0027]Anodes useful in the invention may be silicon/boron-doped diamond anodes and/or useful cathode may be polymer-based graphite felt electrodes.
[0028]Aspects of the invention provide methods, comprising: passing water comprising an organic compound through one or more electrochemical cells in any inventive permutation described herein, thereby subjecting the organic compound to a droplet-impingement, flow-assisted Fenton reaction to degrade the organic compound, wherein the passing reduces a content of the organic compound in the water by at least 90 wt. % from an inlet of the cell to an outlet of the cell within 20 minutes.
[0029]Aspects of the inventi

Problems solved by technology

The lack of efficient water treatment technologies to degrade β-blockers, alongside inadequate analytical techniques, has limited deeper understanding of β-blocker degradation and transformation pathways.
However, the utility of electro-Fenton is limited by high electrical energy demand and correspondingly higher operational costs.
Univariate optimization poor

Method used

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  • Droplet-impingement, flow-assisted electro-fenton purification using heterogeneous silica/iron nanocomposite catalyst
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  • Droplet-impingement, flow-assisted electro-fenton purification using heterogeneous silica/iron nanocomposite catalyst

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[0081]CHEMICAL AND MATERIALS: All chemicals described herein were of analytical grade quality and were used as received without further purification. Acebutolol hydrochloride (ACE, at least 98% pure) and propranolol hydrochloride (PROP, at least 99% pure) were purchased from Sigma-Aldrich (Deisenhofen, Germany). Ferric nitrate, Fe(NO3)3.9H2 (98.5%), cetyltrimethylammonium bromide (CTAB), nitric acid, sodium hydroxide, sulfuric acid, hydrochloric acid, acetone, sodium chloride, and glycerol were purchased from Sigma-Aldrich (St. Louis, USA). Acetonitrile, formic acid, and methanol (LC-MS grade) were purchased from Fisher Scientific (Schwerte, Germany). In all experiments, a 0.05 M Na2SO4 solution was used as a supporting electrolyte. An Si / BDD electrode with 2.75 μm BDD thin layer thickness (both sides) deposited on a conductive Si sheet, was purchased from NeoCoat (Switzerland). A graphite felt electrode (GFE) based on 5 mm thick PAN was purchased from Shanghai Qijie Limited Co. (Chi

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Abstract

A droplet-impingement, flow-assisted electro-Fenton (DFEF) catalyst, system, and method can degrade to trace level organic materials, such as β-blockers in water. A silica/carbon-x % iron composite (RHS/C-x % Fe) can be made, e.g., from rice husks and iron ions into heterogeneous catalysts of varied iron content. The DFEF approach can improve oxygen saturation, mass transfer of β-blockers at the cathode, and continuous electrogeneration of hydroxyl radicals (.OH) in solution and at boron-doped anode surfaces. A central composite design (CCD) can reduce costs and increase efficiency. Beta-blockers can be completely degraded within 15 minutes, following pseudo first-order kinetics with rate constants of 0.19 to 2.72×10−2 (acebutolol) and 0.16 to 2.54×10−2 (propranolol) at increasing catalyst concentration. Beta-blocker degradation can be mostly by .OHbulk rather than .OHadsorbed for anodic oxidation (AO) at BDD electrode. The degradation efficiency of β-blockers can be: DFEF>FEF>BEF>AO.

Description

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Claims

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Application Information

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Owner KING FAHD UNIVERSITY OF PETROLEUM AND MINERALS
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