<?xml version="1.0" encoding="UTF-8"?><xml><records><record><source-app name="Biblio" version="6.x">Drupal-Biblio</source-app><ref-type>17</ref-type><contributors><authors><author><style face="normal" font="default" size="100%">D. Dias</style></author><author><style face="normal" font="default" size="100%">N. Lapa</style></author><author><style face="normal" font="default" size="100%">M. Bernardo</style></author><author><style face="normal" font="default" size="100%">W. Ribeiro</style></author><author><style face="normal" font="default" size="100%">Matos, I.</style></author><author><style face="normal" font="default" size="100%">I. Fonseca</style></author><author><style face="normal" font="default" size="100%">Pinto, F</style></author></authors></contributors><titles><title><style face="normal" font="default" size="100%">Cr(III) removal from synthetic and industrial wastewaters by using co-gasification chars of rice waste streams</style></title><secondary-title><style face="normal" font="default" size="100%">Bioresource Technology</style></secondary-title></titles><keywords><keyword><style  face="normal" font="default" size="100%">Char</style></keyword><keyword><style  face="normal" font="default" size="100%">Cr(III) removal</style></keyword><keyword><style  face="normal" font="default" size="100%">Gasification</style></keyword><keyword><style  face="normal" font="default" size="100%">Rice waste streams</style></keyword></keywords><dates><year><style  face="normal" font="default" size="100%">2018</style></year></dates><urls><web-urls><url><style face="normal" font="default" size="100%">http://www.sciencedirect.com/science/article/pii/S0960852418308332</style></url></web-urls></urls><volume><style face="normal" font="default" size="100%">266</style></volume><pages><style face="normal" font="default" size="100%">139 - 150</style></pages><language><style face="normal" font="default" size="100%">eng</style></language><abstract><style face="normal" font="default" size="100%">&lt;p&gt;Blends of rice waste streams were submitted to co-gasification assays. The resulting chars (G1C and G2C) were characterized and used in Cr(III) removal assays from a synthetic solution. A Commercial Activated Carbon (CAC) was used for comparison purposes. The chars were non-porous materials mainly composed by ashes (68.3–92.6% w/w). The influences of adsorbent loading (solid/liquid ratio – S/L) and initial pH in Cr(III) removal were tested. G2C at a S/L of 5 mg L−1 and an initial pH of 4.50 presented an uptake capacity significantly higher than CAC (7.29 and 2.59 mg g−1, respectively). G2C was used in Cr(III) removal assays from an industrial wastewater with Cr(III) concentrations of 50, 100 and 200 mg L−1. Cr(III) removal by precipitation (uptake capacity ranging from 11.1 to 14.9 mg g−1) was more effective in G2C, while adsorption (uptake capacity of 16.1 mg g−1) was the main removal mechanism in CAC.&lt;/p&gt;
</style></abstract><notes><style face="normal" font="default" size="100%">n/a</style></notes></record></records></xml>