Preparation of Sodium Tungstate from Waste Catalyst Containing Tungsten and Nickel AITranslate
Abstract AITranslate
Sodium tungstate was prepared by roasting plus sodium-leaching-ion exchange and with waste tungsten-nickel hydrogenation catalyst as the raw material. The results show that the tungstate leaching rate from waste catalyst can reach 99% when the catalyst grinding size is 0. 15 ram, the ratio of Na2CO3 dosage to WO3 dosage 0.69, leaching temperature 90℃, and leaching time 1 h. The saturation ion-exchange capacity of WO3 is 332.9 gw%/L-dry resin with the method of serial column absorption. The WO3 desorption rate is 98.2% with 2 mol/L NaCl and 1 mol/L NaOH mixture solution as the desorption agent. The purity of sodium tungstate is 99% after recrystallization.
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1孔昭庆,祝修盛,田雪芹.2005年中国钨工业发展报告[J].中国钨业,2006,21(2):1-6. 被引量:6
2张涛,张德会.近几年我国钨行业宏观调控政策成效与问题分析[J].中国矿业,2010,19(1):11-13. 被引量:4
3中国钨工业“十一五”发展规划2006~2010[J].中国钨业,2007,22(1):54-59. 被引量:6
4熊雪良,谢美求,陈坚,陈泽宗.离子交换法回收废钨催化剂碱浸液中钨的研究[J].金属材料与冶金工程,2008,36(1):12-14. 被引量:7
5黄新,彭书杰,孙亚丽,李涛,唐楷,余祖孝.含钨废料中提取钨的研究[J].中国矿业,2008,17(11):77-81. 被引量:10
6秦玉楠.利用含钨废催化剂生产钨酸的工业实践[J].中国钨业,2002,17(6):40-42. 被引量:6
7张文朴.从废催化剂回收钨、钼、钴、铝的研究进展评述[J].中国资源综合利用,2005,23(11):33-35. 被引量:19
1谢美求,陈坚,熊学良,陈泽宗.废钨-镍型加氢催化剂中综合回收有价金属的研究[J].金属材料与冶金工程,2007,35(5):10-14. 被引量:3
2牛春林,周煜,谭艳山,张聪能,冯金宝,张朝康,王润永.含铼钼精矿的焙烧及烟灰中铼的回收工艺研究[J].云南冶金,2013,42(4):22-25. 被引量:11
3徐迎春,姜萍.关于提高201×7型树脂对钨交换容量的研究[J].中国钨业,2000,15(3):36-37. 被引量:9
4陈重.氧化还原滴定测定含钌加氢催化剂的活性[J].稀有金属快报,2005,24(9):31-34.
5高镁低镍硫化矿生物浸出过程中综合回收镍镁的方法[J].中国有色冶金,2016,45(3):85-85.
6金广集团技术中心不锈钢研究所三项目顺利通过科技成果鉴定[J].不锈:市场与信息,2012(12):5-5.
7王彩华,崔玉民.硫酸铝除铁研究概述[J].内蒙古石油化工,2010,36(2):30-31. 被引量:5
8谢美求,陈坚,欧阳红勇.钨镍负载型纳米加氢催化剂的研制[J].矿冶工程,2009,29(1):67-70. 被引量:2
9刘公召,阎伟,梅晓丹,李雪姣,顾齐欣.从废加氢催化剂中提取钼的研究[J].矿冶工程,2010,30(2):70-72. 被引量:18
10朱来东,鲁兴武,易超,何国才.废旧催化剂中多金属综合回收工艺研究[J].有色金属:冶炼部分,2014(7):35-37. 被引量:2
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DOI:
Chinese Library Classification Number:TF841.1[冶金工程—有色金属冶金]
Citation Information:
Sodium tungstate was prepared by roasting plus sodium-leaching-ion exchange and with waste tungsten-nickel hydrogenation catalyst as the raw material. The results show that the tungstate leaching rate from waste catalyst can reach 99% when the catalyst grinding size is 0. 15 ram, the ratio of Na2CO3 dosage to WO3 dosage 0.69, leaching temperature 90℃, and leaching time 1 h. The saturation ion-exchange capacity of WO3 is 332.9 gw%/L-dry resin with the method of serial column absorption. The WO3 desorption rate is 98.2% with 2 mol/L NaCl and 1 mol/L NaOH mixture solution as the desorption agent. The purity of sodium tungstate is 99% after recrystallization.
quote
| GB/T 7714-2015 | [1] XIONG Xue-liang, CHEN Ze-zong, XIE Mei-qiu, et al. Preparation of Sodium Tungstate from Waste Catalyst Containing Tungsten and Nickel[J]. Rare Metals and Cemented Carbides, 2011(3): 6-9. |
| MLA | [1] XIONG Xue-liang, et al., "Preparation of Sodium Tungstate from Waste Catalyst Containing Tungsten and Nickel." Rare Metals and Cemented Carbides, no. 3, 2011, pp. 6-9. |
| APA | [1] XIONG Xue-liang, CHEN Ze-zong, XIE Mei-qiu, & CHEN Jian. (2011). Preparation of Sodium Tungstate from Waste Catalyst Containing Tungsten and Nickel. Rare Metals and Cemented Carbides(3), 6-9. |
| IEEE | [1] XIONG Xue-liang, CHEN Ze-zong, XIE Mei-qiu, and CHEN Jian, "Preparation of Sodium Tungstate from Waste Catalyst Containing Tungsten and Nickel," Rare Metals and Cemented Carbides, no. 3, pp. 6-9, 2011. keywords: {waste catalyst;tungsten-nickel;sodium tungstate;roasting plus sodium;leaching;ion exchange} |
