Latest Adsorbent for the Adsorption, Removal or Recovery of Environmental Pollutants

A special issue of Separations (ISSN 2297-8739). This special issue belongs to the section "Environmental Separations".

Deadline for manuscript submissions: closed (31 March 2023) | Viewed by 1755

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Department of Environmental Ecology and Landscape Management, Faculty of Natural Sciences, Comenius University, Ilkovičova 6, Mlynská dolina B2, 842 15 Bratislava, Slovakia
Interests: water and wastewater decontamination especially onto natural clinoptilolite & surface treatments; synthesis of functionally upgraded zeolitic adsorbents & material characterization with a broad spectral and thermoanalytical methods; processes to identify factors that limit mass transfer, kinetics, equilibria and phase separation by means of natural clay minerals and zeolites; adsorption and isotherms calculation
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Special Issue Information

Dear Colleagues,

The topic of ion exchange and adsorption has passed through an interesting historical and scientific development, since the first synthetic ion exchanger, prepared probably in 1903 by the two German chemists Harms and Rupler, advanced into current technological maturity. Nevertheless, only scarce references had been found until 1850, when Thompson and Way, two English chemists, discovered “basic principles of cation exchange” through observations of soils. Materials responsible for those phenomena were chiefly described later on by Lemberg and Wiegner as clays, glauconites, zeolites, and humic acids. Also at the beginning of 20th century, specifically in 1935, two English chemists, Adams and Holmes, discovered the ion exchange properties in crushed phonograph records, which perhaps especially in Europe enabled scientists in the following decades to synthesize organic ion exchangers, called resins. For the first time in history, both inventors have been recognized for their scientific contribution. Although the process of ion exchange may be considered to have been discovered in 1850, it was not applied as an industrial separation process until 1905, when the German inventor Richard Gans demonstrated it as a unique process for water softening and for the removal of iron and manganese from waste streams. Approximately 50 years passed, especially after the Second World War (WWII), before an extensive development of the new organic ion exchangers, e.g., sulfonated and aminated copolymers of styrene and divinyl benzene with superior stability and easier recovery or regeneration, fabricated usually in oil refineries or petrochemical companies, enabled rapidly expanding all the ion exchange processes for plenty of industrial applications. Nevertheless, the higher thermal and radiation resistance of some natural zeolites in regard to synthetic ion exchange resins and their excellent selectivity to large, weakly hydrated cations and noxious radioisotopes allowed combining a development of entirely new technological applications of natural zeolites in the following decades. This phenomenon die not generally displace competitive synthetic ion exchangers in then-existing environmental applications, but quite the opposite: it initiated a development of entirely new processes for which synthetic resins were not suited.

Adsorption science has a very long history, with the first practical adoption of adsorption noted in ancient times. The current adsorption theory and relevant applications initiated by Langmuir's fundamental work have been developed extensively more or less during the last 80 years. Today, they comprise many advanced approaches, including a wide spectrum of modern surface chemistry sciences. The autonomous existence of adsorption is based on the enormous complexity that is inherent in adsorption phenomena at various interfaces and the widespread, general occurrence and importance of adsorption and related domains in nature, including everyday-life products and environmental applications.

Prof. Dr. Eva Chmielewska
Guest Editor

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Keywords

  • separation processes
  • adsorption
  • ion exchange
  • environmental pollutant removal
  • regeneration
  • synthetic and natural adsorbents

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Published Papers (1 paper)

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Research

16 pages, 5403 KiB  
Article
CO2 Adsorption on Natural Zeolites from Puebla, México, by Inverse Gas Chromatography
by Miguel Angel Hernandez, Gabriela Itzel Hernandez, Roberto Portillo, Efraín Rubio, Vitalii Petranovskii, Karin Montserrat Alvarez, Ma de los Angeles Velasco, Juana Deisy Santamaría, Mario Tornero and Laura Alicia Paniagua
Separations 2023, 10(4), 238; https://doi.org/10.3390/separations10040238 - 4 Apr 2023
Cited by 1 | Viewed by 1361
Abstract
The applicability of clinoptilolite zeolites in controlling the emission of greenhouse gases (GHGs) such as CO2, the most significant GHG, is investigated herein. In this research, Mexican natural zeolites (ATN) originating from an Atzinco deposit in the state of Puebla were [...] Read more.
The applicability of clinoptilolite zeolites in controlling the emission of greenhouse gases (GHGs) such as CO2, the most significant GHG, is investigated herein. In this research, Mexican natural zeolites (ATN) originating from an Atzinco deposit in the state of Puebla were used. Samples of modified clinoptilolite (ATH4, ATH3, ATH2 and ATH1) were obtained from the starting material by acid treatment of various intensities. Inverse gas chromatography was used to evaluate CO2 adsorption in clinoptilolite, natural and chemically modified. Adsorption of CO2 was investigated in the temperature range of 433–573 K, using a TCD detector, and He as a carrier gas. The experimental CO2 adsorption data were processed by Freundlich and Langmuir equations. The degree of interaction between CO2 and the dealuminated clinoptilolite samples was examined through the evaluation of the isosteric enthalpy of adsorption. This calculation was made by using the Clausius–Clapeyron equation, which established the following sequence: ATH1 > ATH2 > ATH4 > ATN > ATH3. The nanoporosity of these clinoptolite zeolites from new deposit in sedimentary rocks was studied through HRADS adsorption of N2. Simultaneously, these zeolites were, respectively, characterized by XRD, EDS, and SEM. Micropores are described by the Dubinin–Asthakov distribution. Various adsorption mechanisms that occur in these nanoporous materials at different relative pressures can be visualized. The quantitative determination of starting mineral is described as: Ca-Clinoptilolite (88.76%) >> Montmorillonite (11.11%) >> quartz (0.13%). The Si/Al molar ratio after acid treatment is: ATH4 > ATH2 > ATN > ATH3 > ATH1. The Langmuir specific surface area (ASL) varies as follows: ATN > ATH2 > ATH4 > ATH3 > ATH1. At the same time, the VΣ values are as follows: ATN > ATH4 > ATH3 > ATH1 > ATH2. Full article
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