期刊文献+

副产硫酸钙室温固相球磨制备氧化钙

Preparation of calcium oxide from by-product calcium sulfate by solid-state ball milling reaction at ambient temperature
原文传递
导出
摘要 以锰尾矿制备硫酸锰过程中副产硫酸钙为原料在室温下与碳酸氢铵进行固相球磨反应,制备出氧化钙的前驱体碳酸钙,然后将其煅烧得到氧化钙.分别考察了物料配比、球磨时间、球料质量比等因素对硫酸钙转化率的影响,采用X射线衍射和化学分析方法对产物进行了分析,并对室温固相球磨反应的机理进行了探讨.在物料配比(摩尔比)为3.5:1、球磨时间为40 min以及球料质量比为5:1时,硫酸钙的转化率可达到99.8%,将固相产物在1000℃热解1 h后所制备的氧化钙纯度为99.2%.室温球磨过程细化了反应物的颗粒尺寸,增加了反应物的接触面积,为引发反应提供了必要的能量,因此提高了化学反应的有效性. Calcium oxide(CaO) was prepared by directly pyrolyzing the precursor called calcium carbonate (CaCO3),which was synthesized by solid-state ball milling reaction between NH4HCO3 and CaSO4·2H2O,the byproduct generated during the preparation of MnSO4.The effects of NH4HCO3-to-CaSO4·2H2O molar ratio,milling time,and ball-to-feed mass ratio on the conversion of CaSO4·2H2O were investigated respectively.The product was analyzed by X-ray diffraction and chemical analytical method.The reaction mechanism was also discussed.When the NH4HCO3-to-CaSO4·2H2O molar ratio is 3.5:1,the milling time is 40 min,and the ball-to-feed mass ratio is 5:1,the conversion rate of CaSO4·2H2O reaches 99.8%.Calcium oxide,whose purity is 99.2%,can be prepared by pyrolyzing the precursor at 1000℃for 1 h.The effectiveness of the solid-state reaction is improved by refining the reactant size, increasing the contact area,and providing necessary energy during the ball-milling process at ambient temperature.
出处 《北京科技大学学报》 EI CAS CSCD 北大核心 2013年第3期347-351,共5页 Journal of University of Science and Technology Beijing
基金 国家高技术研究发展计划资助项目(2012AA062401) "十二五"国家支撑计划资助项目(2012BAB07B05) 青海省重大科技攻关项目(2007-G-150)
关键词 氧化钙 硫酸钙 固相反应 球磨 malcium oxide calcium sulfate solid state reaction ball milling
  • 相关文献

参考文献1

二级参考文献18

  • 1肖海平,周俊虎,曹欣玉,范红宇,程军,岑可法.CaSO_4在CO气氛下的平行竞争反应实验与模型研究[J].燃料化学学报,2005,33(2):150-154. 被引量:20
  • 2肖海平,周俊虎,刘建忠,曹欣玉,范红宇,岑可法.CaSO_4与CaS在N_2气氛下反应动力学[J].化工学报,2005,56(7):1322-1326. 被引量:21
  • 3沈来宏,肖军,肖睿,张辉.基于CaSO_4载氧体的煤化学链燃烧分离CO_2研究[J].中国电机工程学报,2007,27(2):69-74. 被引量:56
  • 4郑瑛,王保文,宋侃,郑楚光.化学链燃烧技术中新型氧载体CaSO_4的特性研究[J].工程热物理学报,2006,27(3):531-533. 被引量:49
  • 5Richter H, Knoche K. Reversibility of combustion processes. ACS Symposium Series, 1983, 235:71-86
  • 6Glen Jukkota, Greg Liljedahl, Nsakala ya Nsakala, et al. An ALSTOM vision of future CFB technology based power plant coneepts//18th International Conference on Fluidized Bed Combustion. Toronto, Canada, 2005
  • 7ShenLaihong(沈来宏).Chemical looping combustion of coal based on CaSO4 oxygen carrier with inherent separatton of CO2: CN, 200510040519. 2005
  • 8Jib Talukdar, Prabir Basu, Jay H Greenblatt. Reduction of the calcium sulphate in a coal-fired circulating fluidized bed furnace. Fuel, 1996, 75 (9): 1115-1123
  • 9FanHongyu(范红宇).Mutual transformation mechanism of calcium sulfate and calcium sulfide at high temperature in different reacting atmosphere [D]. Hangzhou: Zhejiang University, 2004
  • 10Satoshi Okumura, Naoto Mihara, Ken Kamiya, Shoji Ozawa, Maurice S Onyango, Yoshihiro Kojima, Hitoki Matsuda. Recovery of CaO by reductive decomposition of spent gypsum in a CO-CO2- N2 atmosphere. Ind. Eng. Chem. Res., 2003, 42:6046-6052

共引文献21

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部