Bedoukian   RussellIPM   RussellIPM   Piezoelectric Micro-Sprayer


Home
Animal Taxa
Plant Taxa
Semiochemicals
Floral Compounds
Semiochemical Detail
Semiochemicals & Taxa
Synthesis
Control
Invasive spp.
References

Abstract

Guide

Alphascents
Pherobio
InsectScience
E-Econex
Counterpart-Semiochemicals
Print
Email to a Friend
Kindly Donate for The Pherobase

« Previous AbstractPhytotoxicity of pheromonal chemicals to fruit tree foliage: chemical and physiological characterization    Next AbstractTargeted impact of cyproterone acetate on the sexual reproduction of female rotifers »

Waste Manag


Title:Siloxanes removal from biogas by high surface area adsorbents
Author(s):Gislon P; Galli S; Monteleone G;
Address:"ENEA C.R. Casaccia Via Anguillarese, 301 00123 Rome, Italy. Electronic address: paola.gislon@enea.it"
Journal Title:Waste Manag
Year:2013
Volume:20130926
Issue:12
Page Number:2687 - 2693
DOI: 10.1016/j.wasman.2013.08.023
ISSN/ISBN:1879-2456 (Electronic) 0956-053X (Linking)
Abstract:"Biogas utilized for energy production needs to be free from organic silicon compounds, as their burning has damaging effects on turbines and engines; organic silicon compounds in the form of siloxanes can be found in biogas produced from urban wastes, due to their massive industrial use in synthetic product, such as cosmetics, detergents and paints. Siloxanes removal from biogas can be carried out by various methods (Mona, 2009; Ajhar et al., 2010 May; Schweigkofler and Niessner, 2001); aim of the present work is to find a single practical and economic way to drastically and simultaneously reduce both the hydrogen sulphide and the siloxanes concentration to less than 1 ppm. Some commercial activated carbons previously selected (Monteleone et al., 2011) as being effective in hydrogen sulfide up taking have been tested in an adsorption measurement apparatus, by flowing the most volatile siloxane (hexamethyldisiloxane or L2) in a nitrogen stream, typically 100-200 ppm L2 over N2, through an activated carbon powder bed; the adsorption process was analyzed by varying some experimental parameters (concentration, grain size, bed height). The best activated carbon shows an adsorption capacity of 0.1g L2 per gram of carbon. The next thermogravimetric analysis (TGA) confirms the capacity data obtained experimentally by the breakthrough curve tests. The capacity results depend on L2 concentration. A regenerative carbon process is then carried out by heating the carbon bed up to 200 degrees C and flushing out the adsorbed L2 samples in a nitrogen stream in a three step heating procedure up to 200 degrees C. The adsorption capacity is observed to degrade after cycling the samples through several adsorption-desorption cycles"
Keywords:Adsorption *Biofuels Charcoal Siloxanes/*isolation & purification Biogas Renewable energies Siloxanes removal;
Notes:"MedlineGislon, P Galli, S Monteleone, G eng Comparative Study Evaluation Study 2013/10/01 Waste Manag. 2013 Dec; 33(12):2687-93. doi: 10.1016/j.wasman.2013.08.023. Epub 2013 Sep 26"

 
Back to top
 
Citation: El-Sayed AM 2024. The Pherobase: Database of Pheromones and Semiochemicals. <http://www.pherobase.com>.
© 2003-2024 The Pherobase - Extensive Database of Pheromones and Semiochemicals. Ashraf M. El-Sayed.
Page created on 22-11-2024