Production of activated carbon from rice husk Vietnam

Détails bibliographiques
Parent link:IOP Conference Series: Earth and Environmental Science
Vol. 43 : Problems of Geology and Subsurface Development.— 2016.— [012066, 6 p.]
Auteur principal: Korobochkin V. V. Valery Vasilievich
Collectivité auteur: Национальный исследовательский Томский политехнический университет (ТПУ) Институт физики высоких технологий (ИФВТ) Кафедра общей химии и химической технологии (ОХХТ)
Autres auteurs: Tu N. V., Hieu N. M.
Résumé:Title screen
This work is dedicated to the production of activated carbon from rice husk from Delta of the Red River in Viet Nam. At the first stage, carbonization of a rice husk was carried out to obtain material containing 43.1% carbon and 25 % silica with a specific surface area of 51.5 m{2}/g. After separating of silica (the second stage), the specific surface area of the product increased to 204 m{2}/g and the silica content decreased to 1.23% by weight as well. The most important stage in the formation of the porous structure of the material is the activation. The products with the high specific surface area in the range of 800-1345 m{2}/g were obtained by activation of carbonized product with water vapour or carbon dioxide at temperatures of 700 °C and 850 °C, with varying the flow rate of the activating agent and activation time. The best results were achieved by activation of carbon material with water vapour at the flow rate of 0.08 dm{3}/min per 500 g of material and the temperature of 850 °C.
Langue:anglais
Publié: 2016
Collection:Integrated Use and Processing of Mineral Resources
Sujets:
Accès en ligne:http://dx.doi.org/10.1088/1755-1315/43/1/012066
http://earchive.tpu.ru/handle/11683/35175
Format: Électronique Chapitre de livre
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=650888

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330 |a This work is dedicated to the production of activated carbon from rice husk from Delta of the Red River in Viet Nam. At the first stage, carbonization of a rice husk was carried out to obtain material containing 43.1% carbon and 25 % silica with a specific surface area of 51.5 m{2}/g. After separating of silica (the second stage), the specific surface area of the product increased to 204 m{2}/g and the silica content decreased to 1.23% by weight as well. The most important stage in the formation of the porous structure of the material is the activation. The products with the high specific surface area in the range of 800-1345 m{2}/g were obtained by activation of carbonized product with water vapour or carbon dioxide at temperatures of 700 °C and 850 °C, with varying the flow rate of the activating agent and activation time. The best results were achieved by activation of carbon material with water vapour at the flow rate of 0.08 dm{3}/min per 500 g of material and the temperature of 850 °C. 
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