Tungsten production technology from low-grade tungsten-containing materials; Методология проектирования молодежного научно-инновационного пространства как основа подготовки современного инженера

Библиографические подробности
Источник:Методология проектирования молодежного научно-инновационного пространства как основа подготовки современного инженера.— 2014.— [С. 13-17]
Главный автор: Amanbayev D. D.
Автор-организация: Национальный исследовательский Томский политехнический университет (ТПУ) Физико-технический институт (ФТИ) Кафедра химической технологии редких, рассеянных и радиоактивных элементов (№ 43) (ХТРЭ)
Другие авторы: Chegrincev S. N. Sergey Nikolaevich (научный руководитель)
Примечания:Заглавие с экрана
Tungsten is a worldwide highly-consumed metal. As the tungsten price has increased substantially in the last decade there is an economic imperative to recycle it. It is suggested to involve tungsten-containing metallurgical slags and wastes in reprocessing. Extraction of 87 % of tungsten into solution was reached by autoclave pressure leaching with sodium carbonate (250 g/l) as a leaching agent. Temperature of the process is 220-230°C, solid-to-liquid ratio - 1:5, stirring rate - 60 rpm, duration - 6 hours. After liquor purification from sulfur and silicon by flocculating agent VPK-402, ion-exchange extraction of tungstate-ion was carried out. Sorption properties of two anion-exchange resins - Amberjet 4200 and AV-17-8 - were studied in static conditions. It was revealed that strongly basic anion-exchange resin AV-17-8 in chloride-form is more capable of tungsten in comparison with Amberjet 4200: 42,5 kilos of W/m{3} against 32 kilos of W/m{3}. Carbonate-ions showed a greater affinity to the resin than tungstate-ions, therefore ion-exchange stage was performed in two steps: 1 - to remove CO[3]{2}- from liquor, 2 - extract WO[4]{2}-. Desorption was implemented by NH[4]Cl (50 g/l) with solid-to-liquid ratio 2,5:1 yielding ammonium paratungstate (NH[4])[2]WO[4] (APT). Technology steps for production pure tungsten powder from APT through WO[3] are well-known and described briefly.
Язык:английский
Опубликовано: 2014
Серии:Nuclear technologies as integral part of engineering science in the modern world
Предметы:
Online-ссылка:http://earchive.tpu.ru/handle/11683/64994
http://www.lib.tpu.ru/fulltext/c/2014/C07/002.pdf
Формат: MixedMaterials Электронный ресурс Статья
Запись в KOHA:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=607890

MARC

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330 |a Tungsten is a worldwide highly-consumed metal. As the tungsten price has increased substantially in the last decade there is an economic imperative to recycle it. It is suggested to involve tungsten-containing metallurgical slags and wastes in reprocessing. Extraction of 87 % of tungsten into solution was reached by autoclave pressure leaching with sodium carbonate (250 g/l) as a leaching agent. Temperature of the process is 220-230°C, solid-to-liquid ratio - 1:5, stirring rate - 60 rpm, duration - 6 hours. After liquor purification from sulfur and silicon by flocculating agent VPK-402, ion-exchange extraction of tungstate-ion was carried out. Sorption properties of two anion-exchange resins - Amberjet 4200 and AV-17-8 - were studied in static conditions. It was revealed that strongly basic anion-exchange resin AV-17-8 in chloride-form is more capable of tungsten in comparison with Amberjet 4200: 42,5 kilos of W/m{3} against 32 kilos of W/m{3}. Carbonate-ions showed a greater affinity to the resin than tungstate-ions, therefore ion-exchange stage was performed in two steps: 1 - to remove CO[3]{2}- from liquor, 2 - extract WO[4]{2}-. Desorption was implemented by NH[4]Cl (50 g/l) with solid-to-liquid ratio 2,5:1 yielding ammonium paratungstate (NH[4])[2]WO[4] (APT). Technology steps for production pure tungsten powder from APT through WO[3] are well-known and described briefly. 
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