有色金属科学与工程
有色金屬科學與工程
유색금속과학여공정
JIANGXI NONFERROUS METALS
2013年
5期
33-38
,共6页
吴金玲%李江涛%刘旭恒%陈星宇%何利华
吳金玲%李江濤%劉旭恆%陳星宇%何利華
오금령%리강도%류욱항%진성우%하리화
钨钼混合矿%碳酸钠%热力学计算%选择性浸出
鎢鉬混閤礦%碳痠鈉%熱力學計算%選擇性浸齣
오목혼합광%탄산납%열역학계산%선택성침출
powellite%soda%thermodynamic calculation%selective leaching
针对碳酸钠选择性浸出钨钼混合矿的理论问题,选取25℃条件下的热力学数据,计算并绘制了不同总碳浓度条件下的Ca-W-Mo-C-H2O体系主要离子的浓度对数图,以及溶液中总钨、总钼的浓度与pH关系图,分析了CO32-浓度以及pH值对钨酸钙和钼酸钙混合体系选择性浸出的影响.结果表明:溶液中钨钼饱和浓度随着CO32-浓度的增加而增加,且钼的饱和浓度是钨饱和浓度的1.85倍;在总碳浓度一定的条件下,CaMoO4比CaWO4更易分解;为了避免低pH值下CO32-以HCO3-形式存在导致钨钼浸出率降低,溶液需要保持较高的碱度.通过控制溶液总碳浓度及pH值,可以达到钨钼混合矿选择性浸出钼的目的.
針對碳痠鈉選擇性浸齣鎢鉬混閤礦的理論問題,選取25℃條件下的熱力學數據,計算併繪製瞭不同總碳濃度條件下的Ca-W-Mo-C-H2O體繫主要離子的濃度對數圖,以及溶液中總鎢、總鉬的濃度與pH關繫圖,分析瞭CO32-濃度以及pH值對鎢痠鈣和鉬痠鈣混閤體繫選擇性浸齣的影響.結果錶明:溶液中鎢鉬飽和濃度隨著CO32-濃度的增加而增加,且鉬的飽和濃度是鎢飽和濃度的1.85倍;在總碳濃度一定的條件下,CaMoO4比CaWO4更易分解;為瞭避免低pH值下CO32-以HCO3-形式存在導緻鎢鉬浸齣率降低,溶液需要保持較高的堿度.通過控製溶液總碳濃度及pH值,可以達到鎢鉬混閤礦選擇性浸齣鉬的目的.
침대탄산납선택성침출오목혼합광적이론문제,선취25℃조건하적열역학수거,계산병회제료불동총탄농도조건하적Ca-W-Mo-C-H2O체계주요리자적농도대수도,이급용액중총오、총목적농도여pH관계도,분석료CO32-농도이급pH치대오산개화목산개혼합체계선택성침출적영향.결과표명:용액중오목포화농도수착CO32-농도적증가이증가,차목적포화농도시오포화농도적1.85배;재총탄농도일정적조건하,CaMoO4비CaWO4경역분해;위료피면저pH치하CO32-이HCO3-형식존재도치오목침출솔강저,용액수요보지교고적감도.통과공제용액총탄농도급pH치,가이체도오목혼합광선택성침출목적목적.
For theoretical issues of powellite soda selective leaching, equilibrium diagrams of Ca- W-Mo-C-H2O system were drawn on the basis of thermodynamic data at 25 ℃. Total concentration of ions (W, Mo)-pH relationship diagrams were depicted. The effects of system pH value and total carbon-containing ions concen-tration on mixed system selective leaching were analyzed. Along with the concentration of CO 32-increasing, the total (W, Mo)concentration in the solution was added. The saturation concentration of Mo is about 1.85 times that of W. Under a certain total carbon concentration, CaMoO4 is more likely to decompose than CaWO4. In ad-dition, the high pH value should be maintained to avoid an unexpected abundant of HCO 3- instead of CO32-mainly existing under low pH value, leading to the decrease of W and Mo leaching rate. By controlling the total carbon concentration and pH value of the solution, Mo can be obtained by the effects of W and Mo selective leaching.