Fe3+/Ba2+/Co2+/Zn2+/Cu2+在NH4HCO3-NH3·H2O和NaOH-Na2CO3体系中的热力学分析

通过对Fe3+/Ba2+/Co2+/Zn2+/Cu2+在NH4HCO3-NH3·H2O和NaOH-Na2CO3体系中的热力学分析,得到各金属离子总浓度(cMe)与pH值的关系,确定了2种体系中5种离子完全共沉淀的pH值范围.结果表明:在NH4HCO3-NH3·H2O体系中,Co2+、Zn2+、Cu2+3种离子和氨的配位能力很强,其中Cu2+与氨的配位能力最强,在相同的pH值条件下,Cu2+沉淀困难,5种金属离子的完全共沉淀区域由Cu2+决定.在NaOH-Na2CO3体系中,随总碳浓度(cc)的增加,Ba、Co、Zn、Cu的溶解度都随之减小,当cc=1.0 mol·L-1时,各金属离子完全共沉淀的pH值范围为7.5～11.在两种体系中,Fe的溶解度都是随pH值的增大而减小,最终达到平衡.以NaOH-Na2CO3 为沉淀剂.在pH=10.0的条件下,采用化学共沉淀法合成出了晶粒细小、粒度均匀的Y型纯相结构的平面六角铁氧体微粉.     

共沉淀法合成Zn掺杂Co2-Y平面六角铁氧体粉的热力学分析

通过对 Me(Ba2+,Zn2+,Co2+,Fe3+)-CO32--NH3H2O体系进行热力学分析,得到不同的总碳浓度(cc)和总氮浓度(cN)时各金属离子总浓度(e,t曲与pH值关系,由此确定4种金属离子共沉淀完全的pH值范围.热力学分析表明:以Na2CO3和NH3·HzO作沉淀剂,用共沉淀法合成Zn掺杂Co2-Y平面六角铁氧体粉时,体系pH值由Ba2+和Zn2+沉淀完全的酸度条件决定,而两者取决于cc和cN的相对关系;当Cc＞1.000 mol·L-1、cN＜0.100 mol·L-1时,控制pH值在8～12范围内,即町确保共沉淀完全.     

Fe^3＋/Ba^2＋/Co^2＋/Zn^2＋/Cu^2＋在NH4HCO3-NH3·H2O和NaOH-Na2CO3体系中的热力学分析

通过对Fe^3＋/Ba^2＋/Co^2＋/Zn^2＋/Cu^2＋在NH4HCO3-NH3·H2O和NaOH-Na2CO3体系中的热力学分析,得到各金属离子总浓度（cMe）与pH值的关系,确定了2种体系中5种离子完全共沉淀的pH值范围。结果表明：在NH4HCO3-NH3·H2O体系中,Co^2＋、Zn^2＋、Cu^2＋ 3种离子和氨的配位能力很强,其中Cu^2＋与氨的配位能力最强．在相同的pH值条件下,Cu^2＋沉淀困难,5种金属离子的完全共沉淀区域由Cu^2＋决定。在NaOH—Na2CO3体系中,随总碳浓度（cc）的增加,Ba,Co、Zn、Cu的溶解度都随之减小,当cc=1．0mol·L^-1时,各金属离子完全共沉淀的pH值范围为7．5～11。在两种体系中,Fe的溶解度都是随pH值的增大而减小,最终达到平衡。以NaOH-Na2CO3为沉淀剂,在pH=10．0的条件下,采用化学共沉淀法合成出了晶粒细小、粒度均匀的Y型纯相结构的平面六角铁氧体微粉。     

热力学模型研究KNO3-K2SO4-H2O和KNO3-KCl-H2O体系溶解度

用Pitzer-Simonson-Clegg热力学模型(PSC模型),分别拟合KCl-H2O、K2SO4-H2O、KNO3-H2O体系以及KNO3-K2SO4-H2O和KNO3-KCl-H2O体系水活度和溶解度实验数据,得到二元参数和三元离子相互作用参数,并以此计算3个二元盐水体系溶解度相图,及2个三元盐水体系在不同温度下的溶解度,结果表明计算值与实验值一致。     

四元体系LiNO3-Mg(NO3)2-NH4NO3-H2O相图预测及相关相变储能材料的研究

应用修正的BET热力学模型对Mg(NO3)2-NH4NO3-H2O三元体系和LiNO3-Mg(NO3)2-NH4NO3-H2O四元体系在273～320 K的相图进行预测,并找到一个相变温度较低的四元共晶点Mg(NO3)2.6H2O-LiNO3.3H2O-NH4NO3,其质量百分数组成为:25.5%的硝酸铵,28.4%的硝酸锂,13.8%的硝酸镁和32.3%的水,通过实验对共晶点组成材料的吸放热行为进行测定,发现其熔化温度为286.3 K,且DSC测试其相变热焓为192.7 J.g-1,表明该材料可用作潜在的低温相变储能材料。     

草酸共沉淀法制备YBCO粉体的热力学分析

采用草酸共沉淀法制备YBCO粉末,计算了不同pH值下草酸盐共沉淀粉末的沉淀率,并对制取YBCO前驱体粉末过程中的Ba(NO3)2-Y(NO3)3-Cu(NO3)2-H2C2O4-H2O体系进行热力学分析,采用XRD对制备的YBCO进行了分析计算。结果表明:溶液中不同草酸根离子浓度下各离子沉淀完全的最佳pH范围不同,当草酸浓度为0.1 mol·L-1,pH为2~6时,溶液中离子的沉淀率达到99%以上。随着草酸根离子浓度增大,完全沉淀时,共沉淀液中各金属离子所需的pH值范围增大。热力学计算与试验结果吻合。草酸共沉淀法制备的YBCO粉末物相纯度高,杂质少,颗粒细小,平均粒径为35.4 nm。     

γ-Al2O3/SiO2纳米颗粒混合体系表面的酸碱性质及其对重金属离子的吸附行为

运用电位滴定技术研究了γ-Al2O3/SiO2纳米颗粒混合体系的表面酸碱性质;依据滴定数据及表面配位理论恒电容模式,利用WinSGW软件计算得出了γ-Al2O3/SiO2纳米颗粒混合体系表面的酸碱反应平衡常数:≡XOH+H+≡XOH2+(lgK1=5.06±0.05);≡XOH≡XO-+H+(lgK2=-8.45±0.10);在此基础上研究了不同pH条件下重金属离子Cu2+,Pb2+,Zn2+在γ-Al2O3/SiO2纳米颗粒混合体系表面的吸附行为,并用WinSGW软件模拟得出了Cu2+,Pb2+,Zn2+在该混合悬浮液体系中的表面配位常数:≡XOH+M2+≡XOM++H+[lgK=-2.20,-1.72,-2.90(M=Cu,Pb,Zn)].     

LiCl-Li2B4O7-H2O体系在298.15 K下热力学性质的等压研究

用等压法研究了298.15 K下LiCl-Li2B4O7-H2O体系在不同LiB4O7质量摩尔浓度时的等压平衡浓度,  水活度; 计算了LiCl和Li2B4O7混合盐溶液的渗透系数等热力学性质. 用298.15 K下的实验数据对Pitzer离子相互作用模型进行了参数化研究, 拟合求取了298.15 K下Pitzer离子相互作用参数, 用获得的参数计算了LiCl和Li2B4O7在LiCl-Li2B4O7-H2O体系中的活度系数. Pitzer模型计算的渗透系数值与实验结果一致.     

Fe3+-H2O2-钙黄绿素-邻菲啰啉化学发光体系测定左旋多巴分析方法研究

提出了Fe3+-H2O2-钙黄绿素化学发光体系并用于左旋多巴的测定。在酸性介质中,Fe3+-H2O2-钙黄绿素-邻菲啰啉体系能产生明显的化学发光现象。加入左旋多巴后,对此化学发光强度具有显著的抑制作用,降低程度与体系中左旋多巴浓度呈良好的化学计量关系。据此,结合流动注射技术,建立了流动注射化学发光测定左旋多巴的方法。研究了影响化学发光强度的因素,并探讨了可能发生的机理。化学发光信号的降低值(ΔI)与左旋多巴浓度在2×10-8mol.L-1～2×10-6mol.L-1的范围内呈良好的线性关系,检出限为1.2×10-8mol.L-1。相对标准偏差为1.1%,该法用于片剂中左旋多巴含量的测定,结果令人满意。     

298.15K下Li2B4O7-H2O体系水蒸汽分压及渗透系数的等压测定和离子相互作用模型

在已有研究含硼体系的文献中仅考虑了硼酸根B4O7^-2或B(OH)4^-和H3BO3的存在，而对Li2B4O7-H2O体系具有多种硼物种聚合平衡体系的热力学性质的研究尚未见报道．本文用等压法研究了Li2B4O7-H2O体系于298．15K下浓度由稀到过饱和溶液的平衡气相蒸汽压及渗透系数．考虑了水溶液中多种硼物种的存在，以Pitzer方程为基础，建立了可描述该含硼体系的离子相互作用模型。     

MgSO4-H3BO3-H2O体系水热条件下结晶动力学

The solution of MgSO4-H3BO3-H2O system containing 20%(mass fraction)MgSO4 and 2.5% H 3BO 3 was prepared and the experimental study of its crystallization at 180℃ were carried out in a high pressured vessel. Only a solid phase MgSO4•H2O was separated out from the system. The experimetal data were fitted. With the aid of simplex optimum method and Runge-Kutta digital solution of a set of differential equations, Single-nuclear interface reaction model (MB2) was selected to describe the process of crystallization of kieserite. the dynamic equation is as follows:
-dc/dt=0.064(2.24-c) 4/3 (c-0.290)2     

LiNO_3-KNO_3-H_2O三元体系相平衡研究

本文采用等温法分别测定了KNO3-H2O体系的溶解度相图以及LiNO3-KNO3-H2O体系在273.15和298.15K的等温溶解度相图。结果表明在273.15K时LiNO3-KNO3-H2O体系的溶解度等温线有2条分支,对应的固相分别为KNO3和LiNO3·3H2O,共饱点组成为31.55wt%LiNO3和7.07wt%KNO3。该体系在298.15K的等温线有3条分支,对应的固相分别为KNO3,LiNO3和LiNO3·3H2O,2个共饱点组成分别为50.42wt%LiNO3,22.18wt%KNO3,和55.74wt%LiNO3,10.9wt%KNO3。     

Eine Analyse des Systems NaCl-KCl-Na2CO3-H2O

Ohne Zusammenfassung     

Hydrothermal phase equilibria in Ln2O3-H2O systems

Hydrothermal phase equilibria studies have been carried out in the Ln₂O₃-H₂O systems (Ln = La, Pr, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb and Lu) and the stability fields of the phases Ln(OH)₃ LnOOH and Ln₂O₃-C have been established in the pressure-temperature range of 25000 psi and 900° C. The sequioxides Ln₂O₃-C are stable only in the last four systems of Er to Lu along with the Ln(OH)₃ and LnOOH. The systems from Nd to Ho have only Ln(OH)₃ and LnOOH as stable phases and those from La to Pr have only Ln(OH)₃ as the stable phase. The unit cell parameters of trihydroxides deviate from the values reported in the literature and this is attributed to the contamination of CO₂ in the starting material.     

High-temperature equilibria and critical phenomena in the Na2CO3-NaCl-H2O and Na2CO3-Na2WO4-H2O systems

Phase equilibria in the Na₂CO₃-NaCl-H₂O and Na₂CO₃-Na₂WO₄-H₂O ternary systems formed by type 1 salts (NaCl, Na₂WO₄) and a type 2 salt (Na₂CO₃) were experimentally studied at temperatures from 425 to 500°C and pressures from 30 to 160 MPa with the contents of type 1 salts from 10 to 30 wt %. Transition from supercritical homogeneous fluid equilibria of the Na₂CO₃-H₂O system to heterogeneous equilibria of the title ternary systems was studied in the presence or absence of liquid phase immiscibility in the type 1 subsystems.     

Glass formation in the Al2(SO4)3-AlCl3-H2O system

Glass formation boundaries in the Al₂(SO₄)₃-AlCl₃-H₂O system were determined. The glass-formation abilities and crystallization resistance of samples were studied. A glass formation mechanism was suggested. Comparative analysis of the glass-formation abilities of samples of the Al₂(SO₄)₃-Al(NO₃)₃-H₂O and Al₂(SO₄)₃-AlCl₃-H₂O systems was carried out.     

Sections of the CO(NH2)2-NH4NO3-CH3CONH2-H2O quaternary system

Four sections of the urea-ammonium nitrate-acetamide-water system were studied by the visual polythermal method over wide temperature and concentration ranges. The system was found to be of the simple eutonic type. The corrosion activity of some mixtures of liquid fertilizers at various temperatures was determined.     

三元体系LiCl-LiNO3-H2O 273.15 K和323.15 K等温溶解度的测定

Solubility of the ternary system LiCl-LiNO₃-H₂O was measured at 273.15 K and 323.15 K by analyzing the equilibrated phase composition. Experimental result shows that there are three solubility branches at 273.15 K, corresponding to the solid phases LiCl·2H₂O，LiNO₃ and LiNO₃·3H₂O, respectively, while there are two solubility branches at 323.15 K, corresponding to the solid phase LiCl·H₂O and LiNO₃. The invariant point compositions are (1) 33.68wt% LiCl, 14.32wt% LiNO₃ and (2) 27.70wt% LiCl, 20.60wt% LiNO₃ at 273.15 K and (3) 39.07wt% LiCl, 16.89wt% LiNO₃ at 323.15 K. Also, the experimental results show that the solid phases in equilibrium with the solution {x(2.8LiCl+LiNO₃)-(1-x)H₂O} are LiNO₃·3H₂O or LiNO₃ at 273.15 K and LiNO₃ at 323.15 K.     

Li2SO4-Na2SO4-H2O和Li2SO4- K2SO4-H2O溶液的体积性质

本文用高精度数字式振荡管密度计测定了288K至318K温度范围内Li₂SO₄ + Na₂SO₄ + H₂O和 Li₂SO₄ + K₂SO₄ + H₂O三元体系的密度。混合溶液的离子强度范围从0.1到4.5 mol.kg_–1,混合溶液中Na₂SO₄和K₂SO₄的离子强度分数为0.2,0.4,0.6和0.8。用密度实验值拟合得到了不同温度下Pitzer离子相互作用模型混合参数θ_V和 ψ_V,模型的计算值与实验值的偏差在±0.002 g.cm_–3以内。用Pitzer模型计算了不同离子强度下三元体系的混合体积。