提取脂质的改良干柱法

报道了一种提取脂质的改良干柱法。用低毒溶剂正己烷/异丙醇(3∶2,V/V)作洗脱剂代替干柱法中毒性较强的二氯甲烷/甲醇,通过对重要提取条件的考察,建立了改良干柱法提取脂质的最佳条件,并对干柱法提取机理进行了探讨。使用7.5cm×27mmi.d.玻璃层析柱,内装2.0gCaHPO4·2H2O/Celite545(1∶9),再装入样品、无水Na2SO4、Celite545混合物制备干柱。用40mL正己烷/异丙醇(3∶2,V/V)进行洗脱,可在40min内洗脱完毕。测定了6种肉制品的脂质含量,并做了脂肪酸分析,结果与传统的氯仿/甲醇法一致,统计检验表明,两方法间不存在显著性差异,但改良干柱法洗脱剂毒性更低、试剂用量更少。     

火焰原子吸收法直接测定铅酸蓄电池用硫酸中铁

建立了火焰原子吸收光谱法直接测定H2SO4中Fe的方法。采用蓄电池用H2SO4样品直接配制标准加入法系列溶液,用火焰原子吸收光谱法直接测定蓄电池用H2SO4中的Fe含量。在选定的仪器测定条件下,采用标准加入法所测得的蓄电池用H2SO4中的Fe含量与国标法所测得的结果相比较无显著性差异,检出限为0.060μg/mL(n=13),1.00μg/mL Fe标准溶液平行测定13次,所得吸光度的相对标准偏差为3.3%(n=13)。本法可应用于H2SO4样品中Fe的测定。     

碘量法测定氯乙酰氯生产废酸液中S_2O_3~(2-)和SO_3~(2-)的含量

采用碘量法测定氯乙酸氯化法生产氯乙酰氯产生的废酸液中S2O32-和SO32-的含量。在室温,pH 4~5的条件下直接进行碘量法滴定,测得S2O32-和SO32-的总量;以废酸液中所含SO32-物质的量的3倍加入甲醛,(30±1)℃恒温条件下反应15min以掩蔽SO32-的干扰,用碘量法测得S2O32-的含量,通过计算差值得到SO32-的含量。加标回收率在99.2%~102%之间,测定值的相对标准偏差(n=10)在0.10%~0.20%之间。     

H2O2氧化-重量法测定氯乙酰氯生产废酸液中的SO42-

研究了在氯乙酰氯生产过程中产生的废酸液中的SO42-浓度的测定方法。在酸性(pH≤5.0)介质中,用过量H2O2作为氧化剂,将S2O32-和SO32-氧化为SO42-后,BaCl2沉淀重量法测总硫,根据c(SO42-)=c(总SO42-)-c(SO32-)-2c(S2O32-)关系式,计算法获得SO42-准确含量。该方法简便、可靠,对用氯化法工艺由氯乙酸生产氯乙酰氯过程中由直接水洗吸收法处理尾气所得废酸液及同类废液的分析和废液再利用,具有重要的参考意义和应用价值。     

H_2O_2氧化-重量法测定氯乙酰氯生产过程产生的废酸液中的SO_4~(2-)

研究了在氯乙酰氯生产过程中产生的废酸液中的SO42-浓度的测定方法。在酸性(pH≤5.0)介质中,用过量H2O2作为氧化剂,将S2O32-和SO32-氧化为SO42-后,BaCl2沉淀重量法测总硫,根据c(SO42-)=c(总SO42-)-c(SO32-)-2c(S2O32-)关系式,计算法获得SO42-准确含量。该方法简便、可靠,对用氯化法工艺由氯乙酸生产氯乙酰氯过程中由直接水洗吸收法处理尾气所得废酸液及同类废液的分析和废液再利用,具有重要的参考意义和应用价值。     

Biodiesel production from Jatropha curcas L.fatty acids using solid acid SO2-4/ZrO2-CeO2 as catalyst

用沉淀浸渍法制备了固体酸催化剂SO2-4/ZrO2-CeO2,用于催化小桐籽油脂肪酸与甲醇酯化制备生物柴油.考察了焙烧温度和CeO2负载量对催化剂活性的影响,并进行了单因素实验和动力学研究.研究表明,SO2-4/ZrO2 -CeO2有较高的催化活性,当甲醇与脂肪酸体积比2∶1,反应温度150℃,催化剂用量为脂肪酸质量的8％,反应60 min时,脂肪酸转化率可达0.940 3.动力学计算表明,该酯化反应的表观活化能为45.31 kJ/mol,动力学模型为-dcA/dt=38.371e(45310/RT C 1.44 A ).     

双水相萃取-高效液相色谱法测定酵母细胞中麦角固醇含量

建立了乙醇-水双水相萃取-高效液相色谱法测定酵母细胞中麦角固醇含量的分析方法。先使酵母细胞在KOH-乙醇溶液中于85℃~90℃回流皂化2 h,冷却后加入适量分相剂Na3PO4.12H2O使其形成双水相体系,经振摇萃取,麦角固醇进入乙醇相,萃取效率为95%~102%。用高效液相色谱法(HPLC)测定醇相中麦角固醇含量,采用DiamonsilTMC18色谱柱(200×4.6 mm,5μm),流动相为甲醇,流速为1.0 mL/min;紫外检测波长为281 nm,进样量为20μL。方法线性范围为30.15~2010μg/mL,检出限为1.3μg/mL;用其测得酵母细胞中麦角固醇含量为2.74 mg/g,RSD为2.1%(n=5),加标回收率为91.6%~96.9%。     

气相色谱法测定中华绒螯蟹中脂肪酸组成与含量

中华绒螯蟹中脂肪酸组成与含量的测定对评估其营养价值与品质具有重要意义,但面对种类繁多的脂肪酸提取试剂和甲酯化试剂,测定结果参差不齐,很难对中华绒螯蟹中丰富的脂肪酸准确定量。研究通过比较4种常见的脂肪提取试剂、2种脂肪酸甲酯化试剂,确定以氯仿-甲醇(1∶1, v/v)为提取试剂,含2%硫酸的甲醇溶液为甲酯化试剂,建立了测定中华绒螯蟹肌肉中脂肪酸组成与含量的气相色谱分析方法。实验按照程序升温的条件,采用DM-2560毛细管色谱柱(100 m×0.25 mm×0.20 μm)分离37种脂肪酸,氢火焰离子化检测器(FID)检测,外标法定量。37种脂肪酸在0.5~100.0 μg/mL范围内线性关系良好,其相关系数(R²)为0.9981~0.9999,检出限(LOD)与定量限(LOQ)分别为0.01~0.02 mg/100 g和0.04~0.06 mg/100 g;以棕榈酸和硬脂酸进行加标回收验证,在1、2、10 mg/100 g 3个加标水平下的加标回收率为76.0%~97.5%,相对标准偏差(RSD, n=5)为3.31%~7.90%。该方法应用于中华绒螯蟹肌肉中脂肪酸组成与含量的测定,肌肉中共测得31种脂肪酸,碳链长度为12~24,脂肪酸总含量为281.03 mg/100 g,其中油酸、二十二碳六烯酸、二十碳五烯酸等为中华绒螯蟹肌肉中主要脂肪酸。该方法操作简便,试剂、样品用量少,且定性可靠,定量准确,能检测较多的脂肪酸种类,适用于中华绒螯蟹肌肉中脂肪酸组成与含量的快速检测。     

三维超分子化合物[H_2(C_4H_(10)N_2)](SO_4)(H_2O)的制备、晶体结构及差热-热重性质研究

用MnSO4H2O和哌嗪在水-甲醇混合溶剂中反应得到了1个超分子化合物[H2(C4H10N2)](SO4)(H2O) (C4H14N2O5S)。 该晶体属单斜晶系, 空间群为P21/n, 晶胞参数为: a = 6.386(1), b = 11.695(2), c = 11.680(2) ? = 101.06(3), V = 856.1(3) 3, Z = 4, Mr =202.23 , Dc = 1.569 g/cm3, F(000) = 432, ?= 0.368 mm-1。 该化合物是由[H2(C4H10N2)]2+、SO42-、H2O通过氢键自组装而形成的。 其中[H2(C4H10N2)]2+存在2种椅式构象:一种[H2(C4H10N2)]2+与4个SO42-、2个H2O通过氢键相连, 另一种[H2(C4H10N2)]2+则与6个SO42-相连。 它们分别沿着b、c方向交替排列展开, 通过SO42-桥联成二维的层状结构;层与层之间在NH…O、CH…O、OH…O氢键的作用下互相连接, 形成了具有网状结构的三维超分子化合物。 差热及热重测试表明:该化合物从92℃开始分解,首先失去1个H2O, 然后再失去[H2(C4H10N2)]2+和SO4 2-。     

高效液相色谱法测定毛樱桃中维生素C含量

建立了高效液相色谱(HPLC)测定毛樱桃中维生素C的主要成分L-抗坏血酸和D-异抗坏血酸的方法. 以0.05 mol/L磷酸溶液∶甲醇(体积比为98∶2)作为流动相,紫外检测波长245 nm,柱温25 ℃,流速0.70 mL/min. 获得L-抗坏血酸、D-异抗坏血酸标准曲线线性较好(r为1.0),精密度(RSD)为0.6%. L-抗坏血酸加标回收率为90.83%~92.52%,D-异抗坏血酸加标回收率为91.93%~92.99%. 试验结果表明,方法测定维生素C操作简单、提取速度快、灵敏度高、回收率好,测得L-抗坏血酸的含量为8.24 mg/100 g,D-异抗坏血酸未检测出. 方法可适用于检测其他与毛樱桃相似的果蔬中L-抗坏血酸、D-异抗坏血酸的含量.     

氢氧化钾法与硫酸法制备硫酸铝钾的区别探讨

研究了氢氧化钾和硫酸溶解铝箔制备十二水合硫酸铝钾的区别,通过返滴定法测定制备过程中各阶段的铝含量,深入分析了实验过程中的相关物料守恒,发现氢氧化钾法在铝箔溶解阶段由于副反应形成Al(OH)3沉淀,导致最终产率很低,进行搅拌及降低体系浓度可很大程度上提高产率,不过仍低于硫酸法。此外,硫酸法在实验操作上也相对更简捷。因此推荐学生使用硫酸法来制备十二水合硫酸铝钾。     

Introduction of H2SO4 and H3PO4 into Crystalline Porous Organic Salts(CPOS-1) for Outstanding Proton Conductivity

To improve the proton conduction of crystalline porous organic salts(CPOS-1), H₂SO₄ and H₃PO₄ were introduced into the channel to obtain H₂SO₄@CPOS-1 and H₃PO₄@CPOS-1. Compared to CPOS-1, the proton conductivities of H₂SO₄@CPOS-1 and H₃PO₄@CPOS-1 increased two orders of magnitude and one order of magnitude at 303 K and 100% RH, respectively. It can be attributed to the increasing concentration of the protons, which dissociates from the acids.     

Three-phase extraction study of cyanex 923-n-heptane/H(2)SO(4) system

Phase behavior of the extraction system, Cyanex 923–heptane/H₂SO₄–H₂O has been studied. The third phase appeared at different aqueous H₂SO₄ concentration with varying initial Cyanex 923 concentration and temperature affects its appearance. Almost all of H₂SO₄ and H₂O are extracted into the middle phase. The H₂SO₄ concentration in the third phase increases with the increasing aqueous acid concentration (C_H2SO4,b) while the water content first increases and then reaches a constant value at C_H2SO4,b=11.3 mol l⁻¹. In the region of C_H2SO4,b higher than 5.2 mol l⁻¹, the composition of the middle phase is only related to the equilibrium concentration of H₂SO₄ in the bottom phase. H₂SO₄ and H₂O are transferred into the middle phase mainly by their coordination with Cyanex 923 when C_H2SO4,b is less than 11.3 mol l⁻¹. When C_H2SO4,b is higher than 11.3 mol l⁻¹, excess H₂SO₄ is solubilized into the polar layer of the aggregates. In the region considered, the extracted complex changes from C923 · H₂SO₄ to C923 · H₂SO₄ · H₂O and then to C923 · (H₂SO₄)₂ · H₂O.     

Mechanism of Lithium and Cobalt Recovery from Spent Lithium-ion Batteries by Sulfation Roasting Process

Different from the traditional pyrometallurgical recovery process of Li and Co from spent lithium-ion batteries, a new recovery method for Li and Co was established by converting LiCoO₂ into water-soluble metal sulfates by roasting a mixture of LiCoO₂ and NaHSO₄·H₂O. The evolution law of the mixture with increased roasting temperature was investigated by thermogravimetry-differential scanning calorimetry(TG-DSC), in situ X-ray diffraction(XRD), XRD, and X-ray photoelectron spectroscopy(XPS). The results show that the phase transition of LiCoO₂ mixed with NaHSO₄·H₂O with increased temperature proceeded as follows:LiCoO₂, NaHSO₄·H₂O→LiCoO₂, NaHSO₄→Li_1-xCoO₂, LiNaSO₄, Na₂S₂O₇, Na₂SO₄→Li_1-xCoO₂, Co₃O₄, LiNaSO₄, Na₂SO₄→Co₃O₄, LiNaSO₄. The reaction mechanism of this roasting process may be as follows:LiCoO₂+NaHSO₄·H₂O→1/2Li₂SO₄+ 1/2Na₂SO₄+1/3Co₃O₄+1/12O₂+3/2H₂O, Li₂SO₄+Na₂SO₄=2LiNaSO₄.     

Supported liquid membranes (SLM) for recovery of bismuth from aqueous solutions

In this study, the extraction of Bi(III) from synthetic solutions of 2 M H₂SO₄/0.5 M HCl by supported liquid membranes (SLM) using tri-n-octylphosphine oxide (Cyanex 921) as extractant is reported. First, the nature of the Bi(III)/Cyanex 921 solvates extracted to organic phase (in a solvent extraction system) was determined by the slope method. It was found that Bi(III) reacts with 2 molecules of Cyanex 921 to form the solvate BiCl₃·2Cyanex 921. In the recovery of Bi(III) by the SLM system, parameters that influence extraction efficiency were evaluated, including: support, feed solution and stripping solution nature, and extractant concentration in the organic phase which impregnates the support. Results indicate that Cyanex 921 dissolved in kerosene is not able to extract Bi(III) from H₂SO₄ media. Moreover, transfer of H₂SO₄ was observed. HCl addition to the feed solution up to a maximum concentration of 0.5 M increases Bi(III) extraction. Further increase in HCl concentration causes a decrease in Bi(III) transfer. Likewise, the concentration of Cyanex 921 in the SLM organic phase which produced the maximum Bi(III) extraction was found to be 0.3 M. The performance of H₂O and 0.2 M H₂SO₄ as stripping solutions was evaluated, and it was found that only H₂SO₄ enabled Bi(III) transfer.     

Interaction of photons with some solutions

The linear attenuation coefficients in aqueous solutions of some chlorides and sulphates, viz. MgCl₂·6H₂O, CaCl₂, SrCl₂·6H₂O, BaCl₂·2H₂O, Na₂SO₄, K₂SO₄ and MgSO₄·7H₂O were determined at 81, 356, 511, 662, 1173 and 1332 keV by the γ-ray transmission method in a good geometry setup. From the precision measured densities of these solutions, mass attenuation coefficients were then obtained which varied systematically with the corresponding changes in the concentrations (g/cm³) of these solutions. A comparison between experimental and theoretical values of attenuation coefficients has shown that the study has potential application for the determination of attenuation coefficients of solid solutes from their solutions without obtaining them in pure crystalline form.     

The electrolyte NRTL model and speciation approach as applied to multicomponent aqueous solutions of H2SO4, Fe2(SO4)3, MgSO4 and Al2(SO4)3 at 230–270 °C

This work presents chemical modeling of solubilities of metal sulfates in aqueous solutions of sulfuric acid at high temperatures. Calculations were compared with experimental solubility measurements of hematite (Fe₂O₃) in aqueous ternary and quaternary systems of H₂SO₄, MgSO₄ and Al₂(SO₄)₃ at high temperatures. A hybrid model of ion-association and electrolyte non-random two liquid (ENRTL) theory was employed to fit solubility data in three ternary systems H₂SO₄–MgSO₄–H₂O, H₂SO₄–Al₂(SO₄)₃–H₂O at 235–270 °C and H₂SO₄–Fe₂(SO₄)₃–H₂O at 150–270 °C. Employing the Aspen Plus™ property program, the electrolyte NRTL local composition model was used for calculating activity coefficients of the ions Al³⁺, Mg²⁺ Fe³⁺ and SO₄²⁻, HSO₄⁻, OH⁻, H₃O⁺, respectively, as well as molecular species. The solid phases were hydronium alunite (H₃O)Al₃(SO₄)₂(OH)₆, hematite Fe₂O₃ and magnesium sulfate monohydrate (MgSO₄)·H₂O which were employed as constraint precipitation solids in calculating the metal sulfate solubilities. A correlation for the equilibrium constants of the association reactions of complex species versus temperature was implemented. Based on the maximum-likelihood principle, the binary interaction energy parameters for the ionic species as well as the coefficients for equilibrium constants of the reactions were obtained simultaneously using the solubility data of the ternary systems. Following that, the solubilities of metal sulfates in the quaternary systems H₂SO₄–Fe₂(SO₄)₃–MgSO₄–H₂O, H₂SO₄–Fe₂(SO₄)₃–Al₂(SO₄)₃–H₂O at 250 °C and H₂SO₄–Al₂(SO₄)₃–MgSO₄–H₂O at 230–270 °C were predicted. The calculated results were in excellent agreement with the experimental data.     

Spectrophotometric investigation of the nature and stability of silver(II) in acidic sulphate media

A spectrophotometric study of silver(II) in sulphuric acid solution indicates the formation of two sulphate complexes, in the range 4–18M H₂SO₄, with absorbance peak maxima at 361 and 260 mμ, respectively. In 15M H₂SO₄ the molar absorptivity of silver(II) is 3.11 × 10⁴ at 361 mμ. Kinetic studies of the reduction of silver(II) by the solvent suggest a rate-determining step first order in silver(II) and yield a pseudo first-order rate constant of 1.9 × 10⁻¹min⁻¹. Further studies as a function of H₂SO₄ concentration show that the specific decomposition rate of the two complexes is identical and that changes in H₂SO₄ concentration only serve to shift the concentration equilibrium between the two complexes.     

Modelling of calcium sulphate solubility in concentrated multi-component sulphate solutions

The chemistry of several calcium sulphate systems was successfully modelled in multi-component acid-containing sulphate solutions using the mixed solvent electrolyte (MSE) model for calculating the mean activity coefficients of the electrolyte species. The modelling involved the fitting of binary mean activity, heat capacity and solubility data, as well as ternary solubility data. The developed model was shown to accurately predict the solubility of calcium sulphate from 25 to 95 °C in simulated zinc sulphate processing solutions containing MgSO₄, MnSO₄, Fe₂(SO₄)₃, Na₂SO₄, (NH₄)₂SO₄ and H₂SO₄. The addition of H₂SO₄ results in a significant increase in the calcium sulphate solubility compared to that in water. By increasing the acid concentration, gypsum, which is a metastable phase above 40 °C, dehydrates to anhydrite, and the conversion results in a decrease in the solubility of calcium sulphate. In ZnSO₄–H₂SO₄ solutions, it was found that increasing MgSO₄, Na₂SO₄, Fe₂(SO₄)₃ and (NH₄)₂SO₄ concentrations do not have a pronounced effect on the solubility of calcium sulphate. From a practical perspective, the model is valuable tool for assessing calcium sulphate solubilities over abroad temperature range and for dilute to concentrated multi-component solutions.     

Application of an electrochemical membrane reactor to the thermochemical water splitting IS process for hydrogen production

The Bunsen reaction (SO₂ + I₂ + 2H₂O = H₂SO₄ + 2HI) in the thermochemical IS process to produce hydrogen was successfully employed using an electrochemical membrane reactor. H₂SO₄ and HI were concentrated in the anode side and the cathode side of the reactor, respectively. I₂ is the dominant bulk of the recycling chemicals in this process, and I₂ concentration at the outlet of the reactor was reduced ca. 93% by using this technique. The electric energy consumption for the reaction was about 50% smaller by reducing the concentration of I₂ indicating that the IS process can be operate efficiently at low I₂ concentration. The reaction was carried out for 4 h, and the HI concentration was increased by 26%. This amount was the same within 10% as the values calculated from the total loaded electricity. In order to decrease the overpotential at the anode side, small amount of HI was added to the anode side solution. The total voltage was reduced by 0.03 V by the addition of HI.