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
2013年
10期
3076-3082
,共7页
陈德胜%赵龙胜%齐涛%胡国平%赵宏欣%李洁%王丽娜
陳德勝%趙龍勝%齊濤%鬍國平%趙宏訢%李潔%王麗娜
진덕성%조룡성%제도%호국평%조굉흔%리길%왕려나
脱硅%钒钛渣%碱浸%动力学
脫硅%釩鈦渣%堿浸%動力學
탈규%범태사%감침%동역학
desilication%titanium-vanadium slag%alkaline leaching%kinetics
研究一种选择性脱除钒钛渣中二氧化硅的工艺。利用XRD、SEM和EDS对钒钛渣和碱浸出后的样品进行表征。结果表明:钒钛渣的主要组分是黑钛石、辉石和金属铁。黑钛石为板状和颗粒状,分布于辉石中;金属铁为球型,呈蠕虫状被包裹于辉石和黑钛石中,边缘被氧化;硅主要分布在辉石中;钛和钒主要分布在黑钛石中。对搅拌速度、浸出温度、浸出时间、NaOH浓度和液固比对浸出的影响进行研究。结果表明:浸出温度和液固比对SiO2的浸出率有较大的影响,在最佳实验条件下,Si、Al、Mn和V的浸出率分别为88.2%、66.3%、27.3%和1.2%。钒钛渣碱浸脱硅动力学过程受化学反应控制,其表观活化能为46.3 kJ/mol。
研究一種選擇性脫除釩鈦渣中二氧化硅的工藝。利用XRD、SEM和EDS對釩鈦渣和堿浸齣後的樣品進行錶徵。結果錶明:釩鈦渣的主要組分是黑鈦石、輝石和金屬鐵。黑鈦石為闆狀和顆粒狀,分佈于輝石中;金屬鐵為毬型,呈蠕蟲狀被包裹于輝石和黑鈦石中,邊緣被氧化;硅主要分佈在輝石中;鈦和釩主要分佈在黑鈦石中。對攪拌速度、浸齣溫度、浸齣時間、NaOH濃度和液固比對浸齣的影響進行研究。結果錶明:浸齣溫度和液固比對SiO2的浸齣率有較大的影響,在最佳實驗條件下,Si、Al、Mn和V的浸齣率分彆為88.2%、66.3%、27.3%和1.2%。釩鈦渣堿浸脫硅動力學過程受化學反應控製,其錶觀活化能為46.3 kJ/mol。
연구일충선택성탈제범태사중이양화규적공예。이용XRD、SEM화EDS대범태사화감침출후적양품진행표정。결과표명:범태사적주요조분시흑태석、휘석화금속철。흑태석위판상화과립상,분포우휘석중;금속철위구형,정연충상피포과우휘석화흑태석중,변연피양화;규주요분포재휘석중;태화범주요분포재흑태석중。대교반속도、침출온도、침출시간、NaOH농도화액고비대침출적영향진행연구。결과표명:침출온도화액고비대SiO2적침출솔유교대적영향,재최가실험조건하,Si、Al、Mn화V적침출솔분별위88.2%、66.3%、27.3%화1.2%。범태사감침탈규동역학과정수화학반응공제,기표관활화능위46.3 kJ/mol。
A hydrometallurgical process for the selective removal of silicon from titanium-vanadium slag by alkaline leaching was investigated. X-ray diffraction, scanning electron microscopy and electron dispersive spectroscopy were used to characterize the samples. The results show that anosovite, pyroxene and metallic iron are the major components of the titanium-vanadium slag. Anosovite is presented in granular and plate shapes, and pyroxene is distributed in the anosovite crystals. Metallic iron is spheroidal and wrapped in anosovite. Silicon is mainly in the pyroxene, and titanium and vanadium are mainly in the anosovite. The effects of agitation speed, leaching temperature, leaching time, sodium hydroxide concentration and liquid-solid (L/S) mass ratio on the leaching behavior of silica from titanium-vanadium slag were investigated. The leaching temperature and L/S mass ratio played considerable role in the desilication process. Under the optimal conditions, 88.2%silicon, 66.3%aluminum, 27.3%manganese, and only 1.2% vanadium were leached out. The desilication kinetics of the titanium-vanadium slag was described by the chemical control model. The apparent activation energy of the desilication process was found to be 46.3 kJ/mol.