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溶劑溶解鹽湖低品位固體鉀鹽的動(dòng)力學(xué)研究

發(fā)布時(shí)間:2018-09-09 14:18
【摘要】:低品位鉀礦溶浸開采時(shí),存在資源浪費(fèi)嚴(yán)重和溶浸通道被阻斷的問(wèn)題,為了使資源得到充分高效的利用,需改進(jìn)開采方式及工藝條件。通過(guò)單因素試驗(yàn)和正交試驗(yàn)進(jìn)行溶浸開采工藝條件的研究,考察了溶礦固液比、溶劑中Na Cl的質(zhì)量分?jǐn)?shù)和Mg Cl2的質(zhì)量分?jǐn)?shù)三個(gè)影響因素,確定最佳工藝條件為:溶礦固液比1:0.5;溶劑配比為氯化鈉含量為其飽和度的50%(Na Cl的質(zhì)量分?jǐn)?shù)為13.24%);氯化鎂的質(zhì)量分?jǐn)?shù)為3%;溶解時(shí)間為72h。該條件下溶礦后礦液中KCl的含量大于1.2%,且鹽礦骨架不坍塌,溶浸通道暢通,符合工藝要求。在上述實(shí)驗(yàn)結(jié)論基礎(chǔ)上研究馬海鹽礦中K+、Na+溶解性能和溶解規(guī)律,分別選取質(zhì)量分?jǐn)?shù)為13.24%(即飽和度為50%)的Na Cl溶液和Na Cl+Mg Cl2混合溶液(Na Cl、Mg Cl2質(zhì)量分?jǐn)?shù)分別為13.24%、3%)為溶劑進(jìn)行試驗(yàn),并與水作比較,從而得出其在不同溶劑中的溶解動(dòng)力學(xué)方程。測(cè)得數(shù)據(jù)繪制離子c-t圖,進(jìn)行非線性擬合后得到溶解動(dòng)力學(xué)曲線;再用龍格-庫(kù)塔微分方程組和單純形優(yōu)化法擬合求解stumm模型中的K、n兩個(gè)參數(shù),程序由matlab編寫,最終確定離子的溶解動(dòng)力學(xué)方程并得出不同溶劑中K+、Na+的溶解規(guī)律:溶劑中加入Na Cl時(shí),礦液中K+的溶解速率明顯增大,且礦液中Na+的溶解速率大幅度減小;再引入Mg2+,K+的溶解速率明顯增大,溶解速率常數(shù)K由0.1126增大到0.8749,且礦液中Na+的溶解速率常數(shù)K也保持在10-10級(jí)水平。
[Abstract]:In order to make full and efficient utilization of low grade potassium ore, there are some problems such as serious waste of resources and blocking of leaching channel. In order to make full use of the resource, the mining method and technological conditions should be improved. Through single factor test and orthogonal test to study the technological conditions of leaching and mining, three factors affecting the ratio of solute to liquid, the mass fraction of Na Cl in solvent and the mass fraction of Mg Cl2 were investigated. The optimum technological conditions are as follows: the ratio of solution to solid to liquid is 1: 0.5; the ratio of solvent to sodium chloride is 50% (Na Cl with its saturation is 13.24%); the mass fraction of magnesium chloride is 3%; and the dissolution time is 72 h. Under this condition, the content of KCl in ore solution after ore dissolution is more than 1.2, and the skeleton of salt ore does not collapse, and the leaching channel is open, which conforms to the technological requirements. On the basis of the above experimental conclusions, the solubility and dissolution law of K ~ (2 +) Na in Mahai Salt Mine are studied. Na Cl solution with 13.24% mass fraction (i.e. 50% saturation) and Na Cl Mg Cl2 mixed solution (13.24% Na Cl,Mg Cl2 mass fraction) were chosen as solvents, and compared with water, their dissolution kinetics equations in different solvents were obtained. The ion c-t diagram was drawn from the measured data and the dissolution kinetics curve was obtained after nonlinear fitting, and then the Runge-Kutta differential equation group and simplex optimization method were used to fit and solve the two parameters in the stumm model. The program was written by matlab. Finally, the dissolution kinetics equation of ions was determined and the dissolution law of K ~ (2 +) Na in different solvents was obtained. When Na Cl was added into the solution, the dissolution rate of K in ore solution increased obviously, and the dissolution rate of Na in ore solution decreased significantly. The dissolution rate of Mg2 + K increases obviously, the dissolution rate constant K increases from 0.1126 to 0.8749, and the dissolution rate constant K of Na in ore solution is kept at 10-10 level.
【學(xué)位授予單位】:青海大學(xué)
【學(xué)位級(jí)別】:碩士
【學(xué)位授予年份】:2015
【分類號(hào)】:TD871.1

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