化工学报
化工學報
화공학보
JOURNAL OF CHEMICAL INDUSY AND ENGINEERING (CHINA)
2014年
9期
3464-3469
,共6页
刘作华%阿依努尔·努尔艾合买提%连欣%杜军%范兴%陶长元
劉作華%阿依努爾·努爾艾閤買提%連訢%杜軍%範興%陶長元
류작화%아의노이·노이애합매제%련흔%두군%범흥%도장원
浸取%催化%氧化
浸取%催化%氧化
침취%최화%양화
leaching%catalysis%oxidation
钒渣钠化焙烧过程低价钒氧化不充分,不能被浸出,降低了钒渣的浸出率。实验采用蒽醌磺酸钠(ADA)和栲胶作载氧体实现氧的传递,强化低价钒的氧化行为。通过X射线衍射、扫描电镜、紫外光谱以及紫外可见漫反射光谱等检测方法,分析了转炉钒渣浸出反应前后物相变化行为,探索了反应过程机理,证实了其可行性。结果表明,采用 ADA 和栲胶作载氧体,能将转炉钒渣中的低价钒氧化成可溶的高价钒,实现空气催化氧化高效浸钒。此时,钒浸出率由89.47%分别提高到92.84%和93.64%,且催化剂对体系后续工艺没有不良影响,转炉钒渣中的尾渣含钒量由1.1%分别降至0.52%和0.47%。
釩渣鈉化焙燒過程低價釩氧化不充分,不能被浸齣,降低瞭釩渣的浸齣率。實驗採用蒽醌磺痠鈉(ADA)和栲膠作載氧體實現氧的傳遞,彊化低價釩的氧化行為。通過X射線衍射、掃描電鏡、紫外光譜以及紫外可見漫反射光譜等檢測方法,分析瞭轉爐釩渣浸齣反應前後物相變化行為,探索瞭反應過程機理,證實瞭其可行性。結果錶明,採用 ADA 和栲膠作載氧體,能將轉爐釩渣中的低價釩氧化成可溶的高價釩,實現空氣催化氧化高效浸釩。此時,釩浸齣率由89.47%分彆提高到92.84%和93.64%,且催化劑對體繫後續工藝沒有不良影響,轉爐釩渣中的尾渣含釩量由1.1%分彆降至0.52%和0.47%。
범사납화배소과정저개범양화불충분,불능피침출,강저료범사적침출솔。실험채용은곤광산납(ADA)화고효작재양체실현양적전체,강화저개범적양화행위。통과X사선연사、소묘전경、자외광보이급자외가견만반사광보등검측방법,분석료전로범사침출반응전후물상변화행위,탐색료반응과정궤리,증실료기가행성。결과표명,채용 ADA 화고효작재양체,능장전로범사중적저개범양화성가용적고개범,실현공기최화양화고효침범。차시,범침출솔유89.47%분별제고도92.84%화93.64%,차최화제대체계후속공예몰유불량영향,전로범사중적미사함범량유1.1%분별강지0.52%화0.47%。
Low valency vanadium produced in the insufficient sodium roasting process affects the improvement of vanadium leaching rate. Anthraquinone-2,6-disulfonic acid disodium salt (ADA) or tannin as oxygen carrier was added into the water leaching process to transfer oxygen and to strengthen the air oxidation process of low valency vanadium. Phases of reaction system were analyzed using XRD, SEM, UV and UV-Vis DRS. The reaction mechanism of the process was also studied to prove its theoretical feasibility. Low valency vanadium was effectively oxidized by ADA or tannin, and vanadium leaching ratios increased from initial 89.47%to 92.84%and 93.64%, while vanadium contents in the leaching residue reduced from 1.1%to 0.52%and 0.47%, respectively. It also proved that catalysts had no negative effect on the consequential process.