A Study on Stoichiometry of Complexes of Tributyl Phosphate and Methyl Isobutyl Ketone with Lithium in the Presence of FeCl_3

To study the characteristic of liquid-liquid extraction equilibrium of lithium from brine sources, the complexes formed from tributyl phosphate （TBP） and methyl isobutyl ketone （MIBK） with lithium were investi- gated using FeCl3 as coextracting agent. Liquid-liquid extraction reaction mechanisms were proposed and the stoichiometry of tetrachloroferrate（III） complex with lithium was obtained by regressing the experimental data. It is found that the stoichiometry of tetrachloroferrate（III） to lithium in the complex is 1 ： 1 with either TBP or MIBK as extractant in kerosene. The stoichiometry of the complex of TBP with Li was 1 ： 1 and that of MIBK with Li was 2 ： 1. The formed complexes of TBP and MIBK with lithium are determined to be LiFeCla-TBP and LiFeC14.2MIBK, respectively, according to the rule of neutralization.

Colorimetric determination of nanomolar concentrations of silicate in natural waters after liquid-liquid extraction using methyl isobutyl ketone

A sensitive solvent extraction method for the determination of nonamolar concentrations of silicate in natural waters is developed. According to the traditional aqueous silicate method, silicomolybdenum blue formed by the reaction between silicate and ammoni- um molydate and reduced by metol-sulfite reagent is extracted by methyl isobutyl ketone. The absorbance can be enhanced substantially up to 10-folds. The detection limit of silicate is 8 nmol/dm^3 , which is one tenth smaller than the traditional method, with the precision of 4.0% at a silicate level of 50 nmol/dm^3 and 3.2% at a silicate level of 6 μmol/dm^3. Comparing the calibration curves in the distilled water and seawater, it can be seen that the salt effect also exists in the extraction method. However, the salt effect is a linear function of the salinity and can be corrected by simple calibration. The proposed method is successfully applied to the determination of silicate in natural waters. Natural concentrations of arsenate, arsenite and phosphate cause negligible interference.

Salt effect on the liquid–liquid equilibrium of the ternary (water + phenol + methyl isobutyl ketone) system: Experimental data and correlation

The effects of NaCl, KCl and Na_2SO_4 on the liquid–liquid equilibrium(LLE) data for the ternary system, water+ phenol + methyl isobutyl ketone, were determined at 0.101 MPa and 333.15 K and 343.15 K.The nonrandom two-liquid(NRTL) model was used to correlate the experimental data and to yield corresponding binary interaction parameters for these salt containing systems.The Hand and Othmer–Tobias equations were used to confirm the dependability of the determined LLE data in this work.Distribution coefficient and selectivity were used to evaluate the extraction performance of methyl isobutyl ketone with the existence of salt.The magnitude of salt effect on the water + phenol + methyl isobutyl ketone(MIBK) system is in the following order: Na_2SO_4>NaCl>KCl.

Catalytic Hydrogenation Performance of Methyl Isobutyl Ketone over Ni/γ-Al_2O_3 Catalysts

Supported nickel-based catalysts were prepared by the incipient wetness impregnation method for the selective hydrogenation of methyl isobutyl ketone to methyl isobutyl carbinol in a fixed-bed reactor. The effects of the nickel source,Ni loading, calcination time, and calcination temperature on the hydrogenation performance were studied. The experimental results showed that the Ni/γ-Al_2O_3 catalyst demonstrated the highest catalytic performance under the preparation conditions by using nickel nitrate as the nickel source with a NiO loading of 20%, followed by calcination at 440°C for 5h. In addition,this catalyst showed the largest specific surface area, best crystal structure, highest active component content, smallest particle size, and uniform distribution of NiO on the surface of the carrier. The nickel-based catalyst prepared using the optimized conditions exhibited a 96.1% conversion of methyl isobutyl ketone, with a methyl isobutyl carbinol selectivity of 99.6%. The described procedure is very effective for the preparation of methyl isobutyl carbinol using methyl isobutyl ketone as the feedstock.

Synthesis and properties of soluble poly（aryl ether sulfone ether ketone）s copolymers containing pendant methyl groups

A series of Poly（arly ether sulfone ether ketone）s containing pendant methyl groups were synthesized by the reaction of 4,4＇-[sulfonylbis （1,4-phenylene）dioxy] dibenzoyl chloride （SODBC） with 4,4＇- diphenoxy diphenylsulfone （DPODPS）, 4,4＇- di（2-methylphenoxy） diphenylsulfone （o-Me-DPODPS）, 4,4＇- di（3-methylphenoxy） diphenylsulfone （m-Me-DPODPS）, 4,4＇- di （2,6-bimethylphenoxy） biphenylsulfone（o-Me2-DPODPS） respectively, in a mixture of 1,2-dichloroethane （DCE） and N-methylpyrrolidone （NMP）. These reactions were catalyzed by anhydrous aluminum chloride （AlCl）. The characteristic of copolymers were studied by means of advanced analytical techniques such as FT-IR,1H-NMR, DSC, TGA and WAXD. The results show glass transition temperature （Tg） in the range of 193-206℃, thermally stable in excess of 434℃ and excellent solubility in polar solvents. Methyl-substituted Poly（aryl ether sulfone ketone）s had higher glass transition temperatures, lower initial decomposition temperatures than the unsubstituted ones.

采用HTLcs前驱体制备的丙酮一步法制MIBK催化剂

采用共沉淀法制备Cu Mg A1三元类水滑石,进而煅烧得到CuO MgO Al2O3催化剂用于丙酮加氢一步合成甲基异丁基酮(MIBK)反应。研究了催化剂活性组分配比及反应条件对转化率和选择性的影响,经筛选得到催化剂体系的最佳组成为:n(Cu)∶n(Mg)∶n(Al)=4∶16∶10,适宜的反应条件为:温度240℃,n(H2)∶n(丙酮)=2.5,液空速为4.8mL/h·g,在该条件下丙酮转化率达73.88%,MIBK选择性达55.23%。

USY/SAPO-5复合分子筛的制备与改性及催化合成甲基异丁基酮的工艺研究

采用水热合成法合成USY/SAPO-5复合分子筛,用金属氧化物(NiO和CuO)对其改性,通过X射线粉末衍射(XRD)和NH3程序升温脱附法(NH3-TPD)对复合分子筛进行表征。以USY/SAPO-5复合分子筛和以金属氧化物改性后的分子筛为催化剂,研究丙酮与异丙醇合成甲基异丁基酮(MIBK)的最佳工艺条件。结果表明,2种金属氧化物均能使复合分子筛催化剂的性能获得改善,NiO的改性效果比CuO好;在NiO负载量为0.9%,反应压力为2.0 MPa,反应温度为200℃,空速为1.25 h-1,n(丙酮)/n(异丙醇)为1的最佳工艺条件下,异丙醇转化率为43.1%,MIBK选择性为85.2%。

吹扫捕集-GC-MS/SIM方法检测阿莫西林中的溶剂残留

目的:建立阿莫西林中甲基异丁基酮和醋酸丁酯2种挥发性有机溶剂的残留量测定方法。方法:采用用吹扫捕集浓缩仪和色谱-质谱联用(SIM)(P&T-GC-MS/SIM)方法测定阿莫西林中甲基异丁基酮和醋酸丁酯2种挥发性有机溶剂的残留量。结果:吹扫管中2种溶剂量在0～3200 ng 范围内线性关系良好(r>0.99);吹扫管中2种溶剂量均为2400 ng 时,平行测定5次相对标准偏差分别为4.75%和0.66%;甲基异丁基酮和醋酸丁酯的检测限分别为2.9和4.8 ng。结论:方法能满足粉状和液体药品中 ng 至μg级残留溶剂的测定。

丙酮一步法合成MIBK反应体系热力学研究

对丙酮一步法合成MIBK反应体系进行热力学研究,计算了体系中主、副反应在80~260℃反应焓、反应熵、吉布斯自由能和平衡常数。结果表明:在给定温度范围内,丙酮缩合加氢体系主、副反应均为放热反应,主反应放热量相对较少。随着温度升高,主反应始终自发进行,平衡常数恒大于1;副反应平衡常数逐渐减小,当反应温度>110℃,副反应非自发进行。

磷酸三丁酯、4-甲基-2戊酮对铝锂溶液中锂的萃取行为

以磷酸三丁酯(TBP)作为主要萃取剂,4-甲基2-戊酮(MIBK)作为协助萃取剂,三氯化铁(FeCl3)作为共萃剂,以铝锂溶液体系作为试验对象,全面系统的研究了萃取剂的各组成成分、水相溶液的pH值、铁锂原子比、萃取相比、萃取时间以及静置时间对铝锂溶液中锂的萃取效果的影响。通过正交试验确定了萃取反应的最佳反应参数:萃取相比为5∶2,铁锂原子比为2∶1,pH值为1.5,TBP体积分数为70%,MIBK体积分数为15%,萃取时间为10 min。在此条件下,锂的单级萃取率可达82%,锂铝单级分离因数可达51。对萃取分离过程的反应机理进行了研究,深入探索了铁锂共萃取效应,确定了反应产生的萃合物形态为LiFeCl4·2TBP·MIBK,并探究了萃合物形成过程中的键合方式。该萃取方法经济高效,适用于铝锂溶液中锂的分离。

甲基异丁基酮行业发展现状及趋势

介绍了甲基异丁基酮行业发展现状;重点分析了甲基异丁基酮生产技术、全球主要企业及产能、国内下游消费、价格变化和原料供给等情况;据此,提出了甲基异丁基酮行业未来高质量发展的5点建议。

(S)-N-甲基脯氨醇催化甲基乙烯基酮与苯甲醛的不对称Baylis-Hillman反应的理论研究

采用密度泛函DFT-B3LYP方法在6-31+G*基组下研究了(S)-N-甲基脯氨醇催化甲基乙烯基酮与苯甲醛的不对称Baylis-Hillman反应,得到了反应中各物种的优化构型及其电子能量,获得了反应势能面,同时考虑水和1,4-二氧六环的溶剂效应,解释了该不对称反应的立体选择性。

双液相体系中Cr([MIMPS]_3PW_(12)O_(40))_3催化降解纤维素为5-羟甲基糠醛的研究

研究了在水-有机溶剂双液相体系中用离子液体1-甲基-3-(3-磺酸基丙基)咪唑磷钨酸化铬(Cr([MIMPS]3PW12O40)3)催化降解纤维素为5-羟甲基糠醛(5-HMF)的反应;考察了催化剂的类型和用量、溶剂比、反应时间和温度等因素对产物收率的影响.实验结果表明,催化剂用量为0.1 g,反应温度为140℃,反应4 h,水和四甲基二戊酮的体积比为5∶5时,5-HMF和还原糖的收率分别为52.5%和77.8%.

Pd/HZSM-5催化剂催化加氢丙酮合成甲基异丁基酮

以HZSM-5为载体,采用浸渍法制备系列Pd/HZSM-5催化剂,在高压连续流动固定床反应器中考察Pd/HZSM-5催化剂催化加氢丙酮一步法合成甲基异丁基酮性能,并对工艺条件进行优化。结果表明,当HZSM-5载体上Pd负载质量分数为0.5%时,在反应温度140℃、氢压1 MPa、空速0.48 h-1和氢酮物质的量比为1条件下,Pd/HZSM-5催化剂催化活性较高,丙酮转化率为45.91%,甲基异丁基酮选择性为94.33%。采用XRD、H2-TPD、SEM、EDS和TGA等对催化剂进行表征,结果表明,负载质量分数0.5%的Pd在HZSM-5分子筛表面分散均匀,且0.5%Pd/HZSM-5催化剂具有较高氢吸附能力,失活的主要原因为催化剂表面积炭,采用流化床反应器取代传统的固定床反应器可以很好的解决催化剂积炭问题。

间接原子吸收光度法测定微量S^(2-)

研究了用间接原子吸收分光光度法测定微量S^(2-).在pH=4.5的含S^(2-)溶液中,加入定量过量的Cu^(2+),使其形成CuS沉淀,多余的Cu^(2+)用戊黄原酸钾配合,然后用甲基异丁基甲酮(MlBK)溶剂萃取配合物.不需分离,直接喷雾有机相溶液测定配合铜.S^(2-)的灵敏度为0.01μg/mL/1％,变动系数2.7％.

Equilibrium and kinetic data of adsorption and separation for zirconium and hafnium onto MIBK extraction resin

The equilibrium and kinetics of methyl isobutyl ketone(MIBK) extraction resin for adsorption and separation of zirconium and hafnium were studied under the different conditions of acidity,initial total concentrations of zirconium and hafnium and temperature.The equilibrium data of both zirconium and hafnium are found to follow the Freundlich adsorption isotherm,and the Freundlich isotherm constants(KF) are 3.53 and 0.64 mg/g,respectively.The equilibrium data of zirconium also fit the Langmuir adsorption isotherm,and the saturation adsorption capacity(Qmax) and the Langmuir isotherm constant(KL)are 75.93 mg/g and-0.012 7 L/g,respectively.The obtained kinetic data of both zirconium and hafnium are found to fit the HO pseudo-second-order kinetic model,and the rate constants of pseudo-second-order equation(k2) are-0.019 and 0.41 g/(mg·min),respectively.Column tests show that the MIBK extraction resin could be used as efficient adsorbent material for separating hafnium from zirconium.

Study on the Removal of MIBK from Aqueous Solution by Vacuum Membrane Distillation

Methyl isobutyl ketone(MIBK) is widely used as extraction agent in hydrometallurgy. As it has a definite solubility in water, so when using MIBK as extraction agent, there will be MIBK in stripping solutions inevitably, which not only pollutes working conditions, but also affects the quality of ultimate product. In order to remove MIBK from aqueous solutions, the means of flat vacuum membrane distillation(VMD) is studied in the paper. The area of the membrane used in the study is 0.02 m 2, the initial volume of feed is 2 L, each experiment was conducted over a time period of 60 120 min. The influences of the factors such as temperature(34.8 55.0 ℃); pressure in the permeate side(10.67 14.67 kPa) and feed flow rate(27.8 69.4 mL/s) were experimentally studied. Increasing the temperature or reducing the pressure in the permeate side results in a faster removal of MIBK; however there is a decrease in removal factor β , increasing the feed flow rate results in a faster removal of MIBK and an increase of removal factor β , especially in the range of lower flow rate. The study indicates that the aim of MIBK removal and recycle from dilute aqueous solutions can be achieved by VMD.

Comparative study of degradation of toluene and methyl isobutyl ketone(MIBK)in aqueous solution by pulsed corona discharge plasma

Effectiveness of pulsed power plasma for the degradation of two toxic volatile organic compounds(VOCs),toluene and methyl isobutyl ketone(MIBK),in aqueous solution was evaluated.The plasma degradation of MIBK has been studied for the first time.The influence of initial concentration of target compound,solution pH and scavengers on percentage degradation was evaluated.100%removal of 200 mg/L of toluene and MIBK was achieved both in liquid and gaseous phases after 12 and 16 min of plasma treatment,respectively.The first order rate constant of toluene and MIBK degradation(for 200 mg/L each)was 0.421 and 0.319 min~(-1)respectively when they were treated individually,and these values decreased slightly during degradation of their mixture.MIBK degradation was slower than toluene and it might be due to semi volatile and hydrophilic nature of MIBK.The effect of initial concentration of toluene and MIBK showed different degradation patterns.Highest degradation of both the compounds was obtained in neutral pH and in absence of scavengers.·OH radical was the major reactive species involved in their degradation.Their degradation in real environmental matrices showed that removal reduced significantly in secondary effluent due to scavenging of reactive species by various ions and organic matter.The total number of degradation intermediates identified in case of toluene and MIBK was 11 and 14 respectively and formate was the one recalcitrant byproduct generated.The degradation pathway of toluene and MIBK involving reactions of reactive oxygen and nitrogen species and reductive species is proposed.

Fabrication of Pd-based metal-acid-alkali multifunctional catalysts for one-pot synthesis of MIBK

The one-pot synthesis of methyl isobutyl ketone（MIBK） from acetone using multifunctional catalysts is an important sustainable organic synthesis method with high atom and energy efficiency.Herein. we report a series of Pd supported on mixed metal oxide（MMO） catalysts with controllable acidic/basic/metallic sites on the surface. We study the relationship between the nature, synergy,and proximity of active sites and the catalytic performance of the multifunctional catalyst in the tandem reaction, in detail. In the existence of Lewis acid and base sites, the catalysts with medium-strength acidic/basic sites show preferred activity and/or MIBK selectivity. For multifunctional catalysts, the catalytic properties are more than just a collection of active sites, and the Pd/Mg_3Al-MMO catalyst possessing 0.1% Pd loading and ~0.4 acid/base molar ratio exhibits the optimal 42.1% acetone conversion and 37.2% MIBK yield, which is among the best reported so far for this tandem reaction under similar conditions. Moreover, the proximity test indicates that the intimate distance between acidic/basic/metallic sites can greatly shorten the diffusion time of the intermediate species from each active site, leading to an enhancement in the catalytic performance.

Removal of organic solvent from cathodic electrophoretic emulsion paint by vacuum steam stripping

The production of environmental friendly emulsion paint is of great significance. Vacuum steam stripping of methyl isobutyl ketone （MIBK） and methyl ethyl ketone （MEK） from cathodic electrophoretic emulsion was studied. The effects of mass ratio of vapor to feed （V/F）, vacuum degree and feed temperature on removal rate of MIBK and MEK, emulsion size and solid volume fraction of the emulsion were investigated, and the removal of MIBK and MEK from cathodic electrophoretic emulsion by vacuum desorption was also studied. The results show that removal rates of both MIBK and MEK increase with the increase of V/F, vacuum degree and feed temperature. Removal rates of MIBK and MEK are 98.3% and 93.6%, respectively, at the operating condition V/F of 0.7, feed temperature of 27℃ and vacuum degree of 90 kPa. The emulsion size of cathodic electrophoretic emulsion increases slightly with feed temperature when temperature is below 42 ℃, and increases rapidly with feed temperature when temperature is above 42℃. Solid volume fraction increases by 10% as vacuum degree increases from 0 to 90 kPa at V/F of 0.7 and feed temperature of 27 ℃. Compared with vacuum desorption, vacuum steam stripping can get a higher removal rate of MIBK and MEK under the same feed flow, vacuum degree and feed temperature.