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Ultrasonic Assisted Microchannel Extraction of Fe(III) from Wet-Process Phosphoric Acid 超声波辅助微通道萃取湿法磷酸中铁(III)的研究
IF 0.7 4区 工程技术 Q4 CHEMISTRY, MULTIDISCIPLINARY Pub Date : 2019-01-01 DOI: 10.15261/SERDJ.26.51
Shuai Zhang, Xingbin Lv, Qi Xia, Jiangpo Zhang, Jianjun Chen, Daijun Liu
An ultrasonic assisted microchannel extraction (UAME) method was developed for the extraction of Fe(III) from wet-process phosphoric acid with di(2-ethylhexyl)phosphoric acid (D2EHPA). The influences of ultrasonic power, extractant concentration, water phase velocity and the ratio of the organic and aqueous phases (O/A) on the extraction rate of Fe(III) were systematically studied. The results showed that the extraction efficiency of Fe(III) reached 91.08%, which was significantly higher than that for ultrasound extraction and microchannel extraction respectively. Response surface methodology was adopted to obtain the optimal conditions and to evaluate the significance of variables affecting the extraction efficiency. The extraction efficiency of Fe(III) reached 92.24% under the following optimum conditions: extractant concentration, 2.1 mol/L; aqueous phase velocity, 0.055 mL/min; ratio of organic phase and aqueous phase, 2.98.
采用超声辅助微通道萃取(UAME)法,用二(2-乙基己基)磷酸(D2EHPA)从湿法磷酸中提取铁(III)。系统研究了超声功率、萃取剂浓度、水相速度和有机水相比(O/A)对Fe(III)提取率的影响。结果表明,Fe(III)的提取效率达到91.08%,显著高于超声提取和微通道提取。采用响应面法确定最佳提取条件,并对影响提取效率的变量进行显著性评价。在萃取剂浓度为2.1 mol/L的条件下,Fe(III)的萃取率可达92.24%;水相流速0.055 mL/min;有机相与水相之比为2.98。
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引用次数: 0
Extraction Behavior of Precious Metals in Hydrochloric-acid Media Using a Novel Amine Extractant Bearing a Furan Group 含呋喃基新型胺萃取剂在盐酸介质中萃取贵金属的行为
IF 0.7 4区 工程技术 Q4 CHEMISTRY, MULTIDISCIPLINARY Pub Date : 2019-01-01 DOI: 10.15261/SERDJ.26.69
T. Oshima, Seishiro Iwao, Naoki Matsuo, K. Ohe
Amine extractants are effective for extracting precious metals in hydrochloric-acid media. We developed a novel secondary-amine extractant 2-ethylhexylfurfurylamine (EH-A-F). EH-A-F showed a higher Pd(II) extractability compared with many secondary-amine compounds, such as di(2-ethylhexyl)amine. Because the Pd(II) extraction from solutions of lower hydrochloric-acid concentration is small, Pd(II) and Au(III) can be extracted selectively from the trivalent metal ions Fe(III), Ga(III), and In(III). Because the extractability of hydrochloric acid using EH-A-F was lower than that of a competitive amine compound, benzyl 2ethylhexylamine, EH-A-F was found to show a higher Pd(II) extractability because of its moderate basicity. Slope analysis for Pd(II) extraction showed that the complex stoichiometry was 2:1 for EH-A-F and Pd(II). The Pd(II) extracted by using EH-A-F was stripped quantitatively by using aqueous thiourea solution.
胺萃取剂是一种有效的萃取盐酸介质中贵金属的萃取剂。研制了一种新型仲胺萃取剂- 2-乙基己基糠胺(EH-A-F)。EH-A-F比二(2-乙基己基)胺等许多仲胺类化合物具有更高的Pd(II)提取率。由于Pd(II)在较低盐酸浓度溶液中的萃取量较小,Pd(II)和Au(III)可以选择性地从三价金属离子Fe(III)、Ga(III)和In(III)中萃取出来。由于EH-A-F对盐酸的可萃取性低于竞争性胺类化合物苯二乙基己胺,因此EH-A-F的碱性适中,具有较高的Pd(II)可萃取性。萃取Pd(II)的斜率分析表明,EH-A-F与Pd(II)的络合化学计量比为2:1。用硫脲水溶液对EH-A-F提取的Pd(II)进行定量剥离。
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引用次数: 3
Multifunctional Effect of the Polymer Extractant Thiomethylbenzoxazoyl-α-Methylstyrene on the Extraction of Au(III) 聚合物萃取剂硫甲基苯并恶唑-α-甲基苯乙烯萃取金(III)的多功能效应
IF 0.7 4区 工程技术 Q4 CHEMISTRY, MULTIDISCIPLINARY Pub Date : 2019-01-01 DOI: 10.15261/SERDJ.26.91
Takafumi Hanada, Minako Iwakuma, M. Goto
Takafumi HANADA1, Minako IWAKUMA3 and Masahiro GOTO1,2 1Department of Applied Chemistry, Graduate School of Engineering, 2Center for Future Chemistry, Kyushu University, 744 Motooka, Nishi-ku, Fukuoka 819-0395, Japan; 3Department of Chemical Engineering, National Institute of Technology, Miyakonojo College, 473-1 Yoshio-cho, Miyakonojo City, Miyazaki 8858567, Japan (Received January 14, 2019; Accepted February 22, 2019)
2九州大学工程研究生院应用化学系,2未来化学研究中心,日本福冈西区元冈744号,819-0395;3日本宫崎市宫崎市国立工学院化学工程系,宫崎市吉雄町473-1,日本宫崎市8858567(2019年1月14日收到);接受2019年2月22日)
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引用次数: 1
Extraction of Cephalosporin Antibiotics with Aqueous Two-phase Systems Composed of Water-miscible Organic Solvents and Salts 水溶有机溶剂和盐组成的双水相萃取头孢菌素类抗生素
IF 0.7 4区 工程技术 Q4 CHEMISTRY, MULTIDISCIPLINARY Pub Date : 2019-01-01 DOI: 10.15261/SERDJ.26.63
M. Matsumoto, T. Ueda
The -lactam antibiotics such as penicillin and cephalosporin account for over 65% of the market. Development of a more effective separation technique is desired to extract and purify the biologically active cephalosporin antibiotics. In this study, to recover cephalosporin antibiotics, cephalosporin C and cephalexin, an aqueous two-phase system (ATPS) composed of a water-miscible organic solvent and salts was used. For cephalosporin C extraction with the ATPS, the extent of extraction of cephalosporin C was small because of its high hydrophilicity. For cephalexin, which is more hydrophobic, it was successfully extracted with ATPS. From binodal experiments, tetrahydrofuran (THF), 1-propanol and acetone were selected as the candidates for the extraction solvent. In the extraction experiments, THF was found to be suitable because it gave the highest extractability of cephalexin and the lowest water content in the top (solvent) phase among the candidates. When the initial volume ratio of water to solvent was unity, the maximum distribution ratio was 3.13. The value of the distribution ratio increased up to 9.87 with increasing initial volume ratio. The ATPS composed of a water-miscible organic solvent and salt was found to be promising for purification of antibiotics under such mild conditions.
-内酰胺类抗生素如青霉素和头孢菌素占市场份额的65%以上。开发一种更有效的分离技术来提取和纯化具有生物活性的头孢菌素类抗生素。本研究采用水混溶有机溶剂和盐组成的双水相体系(ATPS)回收头孢菌素类抗生素、头孢菌素C和头孢氨苄。对于ATPS法提取头孢菌素C,由于其亲水性高,头孢菌素C的提取率很小。对于疏水性较强的头孢氨苄,用ATPS法成功提取。通过双极性实验,选择四氢呋喃(THF)、1-丙醇和丙酮作为候选萃取溶剂。在提取实验中,发现THF是合适的,因为它在候选物中具有最高的头孢氨苄提取率和最低的顶相(溶剂)含水量。当初始水与溶剂体积比为1时,最大分配比为3.13。随着初始体积比的增大,分配比增大至9.87。在这种温和的条件下,由水混溶有机溶剂和盐组成的ATPS有望用于抗生素的纯化。
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引用次数: 3
Mechanism of Palladium(II) Adsorption from Nitric Acid Solutions by a Styrene-Divinylbenzene Copolymer Functionalized with N,N,N-Trimethylglycine N,N,N-三甲基甘氨酸功能化苯乙烯-二乙烯基苯共聚物对硝酸溶液中钯的吸附机理
IF 0.7 4区 工程技术 Q4 CHEMISTRY, MULTIDISCIPLINARY Pub Date : 2019-01-01 DOI: 10.15261/SERDJ.26.11
Tomoya Suzuki, H. Narita, Takeshi Ogata, Hideya Suzuki, T. Matsumura, Tohru Kobayashi, H. Shiwaku, T. Yaita
The ability of AMP03, a styrene–divinylbenzene copolymer functionalized with N,N,N -trimethylglycine moieties, to adsorb Pd(II) from HNO 3 solutions was investigated to elucidate the affinity of N,N,N -trimethylglycine for Pd(II). AMP03 effectively adsorbed Pd(II) from 0.10–0.50 M solutions in HNO 3 , and the adsorption ability decreased with increasing HNO 3 concentration owing to competitive adsorption of the acid. In contrast, the presence of added NO 3− increased the Pd(II) adsorption ability of the copolymer. On the basis of slope analysis of data for Pd(II) and HNO 3 at adsorption equilibrium, the Pd(II)/NO 3− /ligand stoichiometry of the adsorbed Pd(II) species was determined to be 1 : 2 : 1. Structural studies performed by means of Fourier transform infrared spectroscopy and extended X-ray absorption fine structure spectroscopy revealed that the N,N,N -trimethylglycine moieties on AMP03 and NO 3− coordinated to Pd(II) via their oxygen atoms. The adsorption selectivity of AMP03 for Pd(II), Ni(II), Cu(II), and Fe(III) was compared with the selectivities of commercially available carboxylic acid and iminodiacetic acid resins. AMP03 selectively adsorbed Pd(II) over Ni(II), Cu(II), and Fe(III) compared with that of the other resins. Our results suggest that AMP03 can be used for selective recovery of Pd(II) from HNO 3 solution.
研究了N,N,N -三甲基甘氨酸功能化的苯乙烯-二乙烯基苯共聚物AMP03吸附hno3溶液中Pd(II)的能力,以阐明N,N,N -三甲基甘氨酸对Pd(II)的亲和力。在hno3溶液中,AMP03能有效吸附0.10 ~ 0.50 M溶液中的Pd(II),随着hno3浓度的增加,由于酸的竞争吸附,AMP03的吸附能力下降。相反,no3−的存在提高了共聚物对Pd(II)的吸附能力。通过对Pd(II)和hno3吸附平衡态数据的斜率分析,确定了Pd(II)/ no3−/配体的化学计量比为1:1:2:1。利用傅里叶变换红外光谱和扩展x射线吸收精细结构光谱进行的结构研究表明,AMP03和NO 3 -上的N,N,N -三甲基甘氨酸部分通过氧原子与Pd(II)配位。比较了AMP03对Pd(II)、Ni(II)、Cu(II)和Fe(III)的吸附选择性与市售羧酸树脂和亚氨基二乙酸树脂的吸附选择性。与其他树脂相比,AMP03在Ni(II)、Cu(II)和Fe(III)上选择性吸附Pd(II)。结果表明,AMP03可用于从hno3溶液中选择性回收Pd(II)。
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引用次数: 3
Separation of Model Petroleum Heavy Fraction by Equilibrium Extraction 平衡萃取法分离模拟石油重馏分
IF 0.7 4区 工程技术 Q4 CHEMISTRY, MULTIDISCIPLINARY Pub Date : 2019-01-01 DOI: 10.15261/SERDJ.26.35
H. Habaki, Tomonori Masuda, R. Egashira
For the separation of petroleum-derived heavy fractions by solvent extraction, the liquid-liquid equilibrium extraction of model heavy fractions, binary and multicomponent model oils, with aqueous methanol solutions was measured, and the effects of nitrogen heterocyclic and other coexisting compounds on the equilibrium extraction were studied. The distribution coefficient increased in the following order of the group compounds; alkanes, aromatics and heterocyclic compounds when the carbon numbers in the molecules of interest were same, and it decreased with an increase in the carbon number of the compound among the respective groups. The coefficients for indoles and quinolines were comparable, and those of carbazoles were smaller. The liquid-liquid equilibrium of nitrogen heterocyclic compounds with the multicomponent system was similar with that with the binary system, and the approximate trend of liquid-liquid equilibrium in the multicomponent system could be evaluated based on the results of simpler systems.
以溶剂萃取法分离石油衍生重馏分为研究对象,测定了甲醇水溶液对模型重馏分、二元和多组分模型油的液液平衡萃取,并研究了氮杂环和其他共存化合物对平衡萃取的影响。基团化合物的分布系数依次增大;烷烃、芳烃和杂环化合物在碳数相同的情况下,随基团间碳数的增加而减小。吲哚类和喹啉类的系数具有可比性,而咔唑类的系数较小。氮杂环化合物在多组分体系中的液-液平衡与二元体系的液-液平衡相似,多组分体系中液-液平衡的近似趋势可以根据更简单体系的结果来评价。
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引用次数: 0
Separation of Scandium from Yttrium in Aqueous Chloride Media by Solvent Extraction with an Acidic Phosphinate Extractant 酸性膦酸盐萃取剂溶剂萃取在氯水介质中分离钪和钇
IF 0.7 4区 工程技术 Q4 CHEMISTRY, MULTIDISCIPLINARY Pub Date : 2019-01-01 DOI: 10.15261/SERDJ.26.99
J. Moon, Emi Yamada, S. Nishihama, K. Yoshizuka
Separation of scandium (Sc) from yttrium (Y) in aqueous chloride media was investigated by solvent extraction with bis(2,4,4-trimethylpentyl)phosphinic acid (Cyanex 272). Conventional slope analysis method revealed the extraction equilibrium formulation of the metals. Sc is more strongly extracted than Y by Cyanex 272, and the separation factor of the metals is quite high at 2.82 × 105. Complete stripping of Sc from the loaded organic solution of Cyanex272 could not be achieved, even with a high concentration of hydrochloric acid. Addition of 1-octanol as a modifier to the organic phase decreased the extractability of Sc, leading to successful stripping of Sc from the loaded organic solution.
研究了双(2,4,4-三甲基戊基)膦酸(Cyanex 272)溶剂萃取法在氯水介质中分离钪(Sc)和钇(Y)。传统的斜率分析方法揭示了金属的萃取平衡公式。在cyanex272中,Sc的萃取力比Y强,分离系数高达2.82 × 105。即使使用高浓度的盐酸,也不能从负载的Cyanex272有机溶液中完全剥离Sc。在有机相中加入1-辛醇作为改性剂降低了Sc的可萃取性,导致Sc从负载的有机溶液中成功剥离。
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引用次数: 2
Extraction Behavior of Metal Cations Using 8-Quinolinol as an Extractant in Cyclopentyl Methyl Ether 8-喹啉醇萃取环戊基甲基醚中金属阳离子的萃取行为
IF 0.7 4区 工程技术 Q4 CHEMISTRY, MULTIDISCIPLINARY Pub Date : 2019-01-01 DOI: 10.15261/SERDJ.26.1
T. Oshima, Takao Koyama, K. Ohe, Noriyasu Otsuki
To date, many kinds of chelating extractants have been developed, however, many of the good extractants are insoluble in aliphatic solvents. In the present study, cyclopentyl methyl ether (CPME) was assessed as a solvent for extractants to develop new solvent extraction systems. Many of the extractants (100 mM) were soluble in CPME. The extraction behavior of metal ions using a typical chelating extractant, 8-quinolinol (HQ) in CPME, was studied. The extraction profiles of metal ions using HQ in CPME were similar to those in toluene, whereas metal ions were extracted using HQ in 1-octanol and chloroform under lower pH conditions. The extraction reaction of In(III) using HQ in CPME was confirmed by slope analysis. A 3 : 1 complex between HQ and In(III) was formed in CPME by a proton exchange reaction, and the extraction equilibrium constant was determined. In(III), extracted using HQ in CPME, was quantitatively recovered using mineral acids. From the results, CPME was found to be a potential alternative solvent to other toxic organic solvents for the development of a solvent extraction system.
迄今为止,已经开发出多种螯合萃取剂,但许多好的萃取剂不溶于脂肪族溶剂。本研究将环戊基甲基醚(CPME)作为萃取剂的溶剂,以开发新的溶剂萃取体系。许多萃取剂(100 mM)可溶于CPME。研究了典型螯合萃取剂8-喹啉醇(HQ)对CPME中金属离子的萃取行为。在较低的pH条件下,HQ在1-辛醇和氯仿中提取金属离子的效果与在甲苯中提取金属离子的效果相似。通过斜率分析证实了在CPME中HQ萃取In(III)的反应。通过质子交换反应,在CPME中形成了HQ与In(III)之间的1:1配合物,并确定了萃取平衡常数。在(III)中,用CPME中的HQ提取,用无机酸定量回收。结果表明,CPME是一种潜在的替代有毒有机溶剂的溶剂萃取体系。
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引用次数: 2
Silver Extraction with Sulfide Type Trident Compounds 硫化物型三叉戟化合物萃取银
IF 0.7 4区 工程技术 Q4 CHEMISTRY, MULTIDISCIPLINARY Pub Date : 2018-01-01 DOI: 10.15261/SERDJ.25.71
K. Ohto, Takuyou Yoshinaga, Hiroaki Furugou, Shintaro Morisada, H. Kawakita, K. Inoue
A sulfide type trident molecule together with a monopodal compound has been prepared to investigate the extraction behavior of silver. The present trident molecule has a weaker extraction ability than thiol and dithioether derivatives of previously reported tripodal extraction reagents. On the contrary, it exhibited a higher extraction ability than the corresponding monopodal molecule due to the structural effect of the trident framework. Both sulfide molecules did not exhibit any pH dependency for silver extraction. The trident molecule showed a 1 : 1 stoichiometry (trident molecule : silver), while the monopodal molecule gave a 2 : 1 stoichiometry (monopodal molecule : silver). The coordination site of the trident molecule was confirmed by 1 H-NMR spectra before and after silver loading. The signal shifts for the protons of the methylene groups bounded to the sulfur atoms for the trident and monopodal compounds before and after silver loading were correlated with the formation of complexes. From the comparison of both molecules, the peak shift for the trident molecule included contributions not only from the functional groups but also from the structure of the trident framework.
制备了一个硫化物型三叉戟分子和一个单极性化合物,研究了银的萃取行为。目前的三叉戟分子的萃取能力比以前报道的三叉戟萃取试剂的硫醇和二硫醚衍生物弱。相反,由于三叉戟框架的结构效应,它表现出比相应的单极性分子更高的提取能力。两种硫化物分子对银的萃取没有任何pH依赖性。三叉戟分子呈1:1的化学计量(三叉戟分子:银),单极分子呈2:1的化学计量(单极分子:银)。负载银前后的1h - nmr谱证实了三叉戟分子的配位。负载银前后,三叉戟和单极性化合物与硫原子结合的亚甲基质子的信号位移与配合物的形成有关。从两种分子的比较可以看出,三叉戟分子的峰移不仅包括官能团的贡献,还包括三叉戟框架结构的贡献。
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引用次数: 2
Rapid and Selective Concentration of Lycopene Z -isomers from Tomato Pulp by Supercritical CO 2 with Co-solvents 超临界co2助溶剂快速富集番茄红素Z -异构体
IF 0.7 4区 工程技术 Q4 CHEMISTRY, MULTIDISCIPLINARY Pub Date : 2018-01-01 DOI: 10.15261/SERDJ.25.47
Yoichi Watanabe, M. Honda, Takuma Higashiura, Tetsuya Fukaya, S. Machmudah, Wahyudiono, H. Kanda, M. Goto
Yo WATANABE1, Masaki HONDA2,*, Takuma HIGASHIURA3, Tetsuya FUKAYA3, Siti MACHMUDAH4, WAHYUDIONO1, Hideki KANDA1 and Motonobu GOTO1,* 1Department of Materials Process Engineering, Nagoya University, Furo-cho, Chikusa-ku, Nagoya 4648603, Japan; 2Graduate School of Bioagricultural Sciences, Nagoya University, Furo-cho, Chikusa-ku, Nagoya 464-8601, Japan; 3Innovation Division, Kagome Company, Limited, Nishitomiyama, Nasushiobara 329–2762, Japan; 4Chemical Engineering Department, Sepuluh Nopember Institute of Technology, Kampus ITS Sukolilo, Surabaya 60111, Indonesia (Received April 26, 2017; Accepted June 26, 2017)
watanabyo 1, hondamasaki 2,*, higashiuma a3, fukayteya a3, Siti MACHMUDAH4, wahydion1, Hideki KANDA1, Motonobu GOTO1,* 1名古屋大学材料工艺工程系,日本名古屋4648603;2名古屋大学生物农业科学研究生院,日本名古屋464-8601;3 . Kagome株式会社创新事业部,日本总务原市西宫329-2762;4 Sepuluh十一月理工学院化学工程系,Sukolilo校区,印尼泗水60111(收于2017年4月26日;2017年6月26日录用)
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引用次数: 17
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Solvent Extraction Research and Development, Japan
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