中国有色金属学报(英文版)
中國有色金屬學報(英文版)
중국유색금속학보(영문판)
TRANSACTIONS OF NONFERROUS METALS SOCIETY OF CHINA
2014年
8期
2686-2693
,共8页
宋文臣%李宏%朱福兴%李昆%郑权
宋文臣%李宏%硃福興%李昆%鄭權
송문신%리굉%주복흥%리곤%정권
熔融态钒渣%氧化钙%氧化%酸浸%钒回收%节能
鎔融態釩渣%氧化鈣%氧化%痠浸%釩迴收%節能
용융태범사%양화개%양화%산침%범회수%절능
molten vanadium bearing slag%CaO%oxidation%acid leaching%vanadium recovery%energy saving effect
在实验室条件下对熔融态钒渣直接氧化钙化提钒新工艺进行研究。在反应过程中利用纯氧氧化,CaO作为添加剂,硫酸浸出熟料。采用XRD、XPS、SEM 及 EDS等手段对钒渣熟料进行分析,考察不同CaO/V2O5质量比与硫酸浓度对熟料中钒浸出的影响,并与现行焙烧工艺在能耗方面进行对比。结果表明:钒渣熟料中形成了钒的富集相,钒渣的氧化钙化产物主要为CaV2O5和Ca2V2O7,并对钒酸钙的形成机理进行了阐释;XRD和XPS分析得出熔渣中钒的氧化反应在供氧充足的情况下存在一定限制,CaO的增加能促进五价钒在熔渣中的稳定;在优化的实验条件下(CaO/V2O5质量比0.6,粒度120~150μm,浸出时间2 h,浸出温度90°C,液固比5:1 mL/g, H2SO4浓度20%,搅拌强度500 r/min),钒的浸出率能达到90%;能耗计算得到每处理1000 kg钒渣,利用新工艺可以节约能量1.85×106 kJ。实验与计算结果验证新工艺是一种节能减排的提钒手段。
在實驗室條件下對鎔融態釩渣直接氧化鈣化提釩新工藝進行研究。在反應過程中利用純氧氧化,CaO作為添加劑,硫痠浸齣熟料。採用XRD、XPS、SEM 及 EDS等手段對釩渣熟料進行分析,攷察不同CaO/V2O5質量比與硫痠濃度對熟料中釩浸齣的影響,併與現行焙燒工藝在能耗方麵進行對比。結果錶明:釩渣熟料中形成瞭釩的富集相,釩渣的氧化鈣化產物主要為CaV2O5和Ca2V2O7,併對釩痠鈣的形成機理進行瞭闡釋;XRD和XPS分析得齣鎔渣中釩的氧化反應在供氧充足的情況下存在一定限製,CaO的增加能促進五價釩在鎔渣中的穩定;在優化的實驗條件下(CaO/V2O5質量比0.6,粒度120~150μm,浸齣時間2 h,浸齣溫度90°C,液固比5:1 mL/g, H2SO4濃度20%,攪拌彊度500 r/min),釩的浸齣率能達到90%;能耗計算得到每處理1000 kg釩渣,利用新工藝可以節約能量1.85×106 kJ。實驗與計算結果驗證新工藝是一種節能減排的提釩手段。
재실험실조건하대용융태범사직접양화개화제범신공예진행연구。재반응과정중이용순양양화,CaO작위첨가제,류산침출숙료。채용XRD、XPS、SEM 급 EDS등수단대범사숙료진행분석,고찰불동CaO/V2O5질량비여류산농도대숙료중범침출적영향,병여현행배소공예재능모방면진행대비。결과표명:범사숙료중형성료범적부집상,범사적양화개화산물주요위CaV2O5화Ca2V2O7,병대범산개적형성궤리진행료천석;XRD화XPS분석득출용사중범적양화반응재공양충족적정황하존재일정한제,CaO적증가능촉진오개범재용사중적은정;재우화적실험조건하(CaO/V2O5질량비0.6,립도120~150μm,침출시간2 h,침출온도90°C,액고비5:1 mL/g, H2SO4농도20%,교반강도500 r/min),범적침출솔능체도90%;능모계산득도매처리1000 kg범사,이용신공예가이절약능량1.85×106 kJ。실험여계산결과험증신공예시일충절능감배적제범수단。
A novel process of vanadium extraction from vanadium slag in its molten state was conducted at the laboratory scale by oxidation with pure oxygen in the presence of CaO. The effect of mass ratio of CaO to V2O5 on the recovery of vanadium was studied. The sintered samples were leached by H2SO4 solution and characterized by XRD, XPS, SEM and EDS techniques. Compared with the roasting process, the energy saving effect of the proposed process was also discussed. The results showed that vanadium-rich phases were formed and vanadium mainly existed in the forms of CaV2O5 and Ca2V2O7. The formation mechanism of calcium vanadates in the molten vanadium bearing slag was explained. The XRD and XPS results implied that there was a limit to the oxidation reaction of V(IV) to V(V) under the high temperatures even though oxygen-supply was sufficient. An increase in the CaO content led to an increase in the formation of Ca2V2O7. About 90%of the vanadium recovery was obtained under optimal experiment conditions (mass ratio of CaO to V2O5 of 0.6, particle size 120 to 150μm, leaching temperature 90 °C, leaching time 2 h, H2SO4 concentration 20%, liquid to solid ratio 5:1 mL/g, stirring speed 500 r/min). The energy of 1.85×106 kJ could be saved in every 1000 kg of vanadium bearing slag using the proposed process from the theoretical calculation results. Recovery of vanadium from the molten vanadium bearing slag and utilisation of its heat energy are important not only for saving metal resources, but also for energy saving and emission reduction.