Phase behavior for the poly[2-(2-ethoxyethoxy)ethyl acrylate] and 2-(2-ethoxyethoxy)ethyl acrylate in supercritical solvents

Pressure-composition (p, x) isotherms were obtained for the carbon dioxide + 2-(2-ethoxyethoxy)ethyl acrylate [2-(2-EE)EA] system at five temperatures (313.2 K, 333.2 K, 353.2 K, 373.2 K, and 393.2 K) and pressure up to 22.86 MPa. The carbon dioxide + 2-(2-EE)EA system exhibits type-I phase behavior with a continuous mixture critical curve. The experimental results for carbon dioxide + 2-(2-EE)EA mixtures are correlated using the Peng–Robinson equation of state (PR-EOS) using mixing rule including two adjustable parameters. The critical property of 2-(2-EE)EA is estimated with the Joback–Lyderson method.Experimental data up to 485 K and 206.6 MPa are reported for binary and ternary mixtures of poly(2-(2-ethoxyethoxy)ethyl acrylate) [P(2-(2-EE)EA)] + carbon dioxide + 2-(2-EE)EA, P(2-(2-EE)EA) + carbon dioxide + dimethyl ether (DME), P(2-(2-EE)EA) + carbon dioxide + propylene and P(2-(2-EE)EA) + carbon dioxide + 1-butene systems. High-pressure cloud-point data are also reported for P(2-(2-EE)EA) in supercritical carbon dioxide, propane, propylene, butane, 1-butene, and DME at temperature to 474 K and a pressure range of (8.45–206.6) MPa. Cloud-point behavior for the P(2-(2-EE)EA) + carbon dioxide + 2-(2-EE)EA system were measured in changes of the pressure–temperature (p, T) slope and with 2-(2-EE)EA mass fraction of 0.0 wt%, 5.9 wt%, 14.9 wt%, 30.3 wt% and 60.2 wt%. With 0.650 2-(2-EE)EA to the P(2-(2-EE)EA) + carbon dioxide solution, the cloud point curves take on the appearance of a typical lower critical solution temperature boundary. The P(2-(2-EE)EA) + carbon dioxide + (0.0–46.6) wt% DME systems change the (p, T) curve from upper critical solution temperature region to lower critical solution temperature region as the DME mass fraction increases. Also, the impact by propylene and 1-butene mass fraction for the P(2-(2-EE)EA) + carbon dioxide + propylene and 1-butene system is measured at temperatures to 454 K and a pressure range of (75.7 to 119.6) MPa.     

Measurement of VLE data of carbon dioxide (CO2) + methyl iodide (CH3I) system for the direct synthesis of dimethyl carbonate using supercritical CO2 and methanol

Isothermal vapor⿿liquid equilibrium data for the binary system carbon dioxide + methyl iodide were measured at temperatures from 283.15 to 323.15 K at 10 K intervals. Data in the two-phase region were measured by using a circulation-type equilibrium apparatus and gas chromatography. This binary mixture system showed positive deviation from the Raoult's law and no azotrope observance. The experimental data were correlated with the Peng⿿Robinson equation of state (PR-EoS) using the Wong⿿Sandler (W⿿S) mixing rule, which was combined with the nonrandom two-liquid (NRTL) excess Gibbs free energy model and Peng⿿Robinson equation of state (PR-EoS) using the Universal mixing rule (UMR) as well as with the UNIQUAC model. The calculated results with this combination of equations show positive agreement with experimental data taken within this study.     

The pH of CO2-saturated water at temperatures between 308 K and 423 K at pressures up to 15 MPa

We report pH measurements for CO₂-saturated water in the pressure range from (0.28 to 15.3) MPa and temperatures from (308.3 to 423.2) K. Commercially available pH and Ag/AgCl electrodes were used together with a high pressure equilibrium vessel operating under conditions of precisely controlled temperature and pressure. The results of the study indicate that pH decreases along an isotherm in proportion to −log₁₀(x), where x is the mole fraction of dissolved CO₂ in H₂O. The expanded uncertainty of the pH measurements is 0.06 pH units with a coverage factor of 2. The reported results are in good agreement with the literature in pressure ranges up to 16 MPa at temperatures below 343 K. An empirical equation has been developed to represent the present results with an expanded uncertainty of 0.05 pH units. We also compare our results with a chemical equilibrium model and find agreement to within 0.1 pH unit.     

(S)-2-(ethyl propionate)-(O-ethyl xanthate)- and (S)-2-(Ethyl isobutyrate)-(O-ethyl xanthate)-mediated RAFT polymerization of vinyl acetate

(S)-2-(Ethyl propionate)-(O-ethyl xanthate) (X1) and (S)-2-(Ethyl isobutyrate)-(O-ethyl xanthate) (X2) were used as the reversible addition-fragmentation chain transfer (RAFT) agents for the radical polymerization of vinyl acetate (VAc). The former showed the better chain transfer ability in the polymerization at 60°C. Kinetic study with both RAFT agents showed pseudo-first order kinetics up to around 85% monomer conversion. Molecular weight of the resulting polymer increased linearly with increase in the monomer conversion up to around 85%. The observed molecular weights calculated from ¹H-NMR spectrum [M_n(NMR)] are close to the corresponding theoretical molecular weights [M_n(theor)]. The corresponding polydispersity index (PDI) of the resulting polymers remained almost constant at around 1.2 up to ∼ 65% monomer conversion and then increased gradually with the further increase in the monomer conversion. Chain-end analysis of the resulting polymers by ¹H-NMR showed clearly that polymerization started with the radical forming out of the xanthate mediator. The negligible homo-chain extension and the hetero-chain extension involving synthesis of poly(VAc)-b-poly(NVP) diblock copolymer were occurred. © 2012 Wiley Periodicals, Inc. J Appl Polym Sci, 2012     

The homo and copolymerisation of 2-(dimethylamino)ethyl methacrylate in supercritical carbon dioxide

This paper describes the free radical dispersion homopolymerisation of 2-(dimethylamino) ethyl methacrylate (DMA) and copolymerisation of DMA with methyl methacrylate (MMA) in supercritical carbon dioxide (scCO₂). The polymerisations are performed in the presence of two commercially available stabilisers, poly(dimethylsiloxane) monomethacrylate macromonomer (PDMS-mma) and the carboxylic acid terminated perfluoropolyether (Krytox 157FSL). Dry, fine powdered polymer product was produced for the copolymer under optimised conditions, but only aggregated solid is formed for homo poly(DMA). The effect of reaction time, stabiliser, copolymer composition and reaction pressure on the yield, molecular weight and morphology of the copolymers has been investigated.     

2-氰基-2-对硝基苯基乙酸乙酯的合成研究

实验选用氨基钠、三苯甲醇钠和叔丁醇钠作催化剂，以代替高危险性的催化剂氢化钠来合成20氰基－2－对硝基苯基乙酸乙酯。经过实验，筛选出最佳反应条件：以二甲基亚砜作溶剂，三苯甲醇钠为催化剂，50℃时粗产品的收率达68．16％，比文献值高约10％。     

2-硬脂酰胺乙基乙基取代苯基磷酸酯的合成和生物活性

烷氧基磷酰二氯与取代苯酚、N-硬脂酰乙醇胺反应制备得到了6个新的标题化合物,其结构用核磁、元素分析进行了表征,并对它们的植物生长调节和杀菌活性进行了测定。     

Phase equilibria of (CO2 + H2O + NaCl) and (CO2 + H2O + KCl): Measurements and modeling

We report experimental measurements of the phase behavior of (CO₂ + H₂O + NaCl) and (CO₂ + H₂O + KCl) at temperatures from 323.15 K to 423.15 K, pressure up to 18.0 MPa, and molalities of 2.5 and 4.0 mol kg⁻¹. The present study was made using an analytical apparatus and is the first in which coexisting vapor- and liquid-phase composition data are provided. The new measurements are compared with the available literature data for the solubility of CO₂ in brines, many of which were measured with the synthetic method. Some literature data show large deviations from our results.The asymmetric (γ–φ) approach is used to model the phase behavior of the two systems, with the Peng–Robinson equation of state to describe the vapor phase, and the electrolyte NRTL solution model to describe the liquid phase. The model describes the mixtures in a way that preserves from our previous work on (CO₂ + H₂O) the values of the Henry's law constant and the partial molar volume of CO₂ at infinite dilution Hou et al. [22]. The activity coefficients of CO₂ in the aqueous phase are provided. Additionally, the correlation of Duan et al. [14] for the solubility of CO₂ in brines is tested against our liquid-phase data.     

甲基丙烯酸2-(二乙氧基硫代磷酰氧基)乙基酯的合成及应用

以甲基丙烯酸-β-羟乙酯(HEMA)与O,O-二乙基硫代磷酰氯为原料,在三乙胺作缚酸剂,氯化亚铜(CuCl)作催化剂的条件下,合成了甲基丙烯酸2-(二乙氧基硫代磷酰氧基)乙基酯(DPTEM)阻燃剂,再与丙烯腈共聚得到了阻燃聚丙烯腈共聚物。在n(HEMA)/n(三乙胺)=1,m(CuCl)/m(HEMA)=0.01~0.02,反应温度0~5℃条件下,DPTEM的产率达82%;通过FTIR、1HNMR、MS测试技术表征了DPTEM的结构,证明产品结构正确。丙烯腈共聚物中w(DPTEM)=25%时,极限氧指数(LOI)值可达27。该工艺已通过中试,正在进行扩大化生产。     

N，N-双（2-（1,3-二氧异吲哚-2-基）乙基）丙烯酰胺的合成与表征

以邻苯二甲酸酐(PA)、二乙烯三胺(DETA)为原料,经亲电加成-消除反应合成有机中间体双(2-邻苯二甲酰亚胺)胺(DETA-2PA),其再与丙烯酰氯(AC)发生酰胺化反应合成有机中间体N,N-双[2-(1,3-二氧异吲哚-2-基)乙基]丙烯酰胺(AC-DETA-2PA)。通过FTIR、1HNMR、元素分析、HRMS、HPLC对产物结构进行了确证,并用TGA、荧光光谱对产物的性能进行了测试。考察了反应温度、反应时间、n(AC)∶n(DETA-2PA)及催化剂用量4个因素对合成AC-DETA-2PA胺值的影响。通过响应面设计对AC-DETA-2PA的合成工艺进行了优化,确定其较佳合成工艺条件为:n(AC)∶n(DEETA-2PA)=1.6∶1.0,反应温度为25℃,催化剂氢化钠用量占反应物(AC和DETA-2PA)总质量的8.46%,反应时间4h。在该条件下,AC-DETA-2PA的胺值可达2.96 mg KOH/g。     

不对称合成(R)-2-羟基-4-苯基丁酸乙酯的动力学

采用10,11-二氢辛可尼定修饰的Pt/Al2O3催化体系,不对称加氢合成(R)-2-羟基-4-苯基丁酸乙酯,研究了各因素影响反应速率和光学收率的一般规律.根据推测的机理,建立了未修饰体系中加氢反应的本征动力学模型,结合实验数据选定了较佳的模型.假设不对称加氢反应总速率包括反应物在催化剂表面修饰位上和未修饰位上两部分的加氢速率,建立了不对称加氢的动力学模型,经拟合得到参数并进行了验证和讨论.     

N-丙基-N-[2-(2,4,6-三氯苯氧基)乙基]氨基甲酰氯分析方法的研究

介绍了N-丙基-N-[2,4,6-三氯苯氧基)乙基]氨基甲酰氯的化学分析法,该方法操作简单,且具有较好的精密度和准确度,可用于N-丙基-N-[2-(2,4,6-三氯苯氧基)乙基]氨基甲酰氯的质量控制分析。     

Diffusion and controlled release characteristics of pH-sensitive poly(2-(dimethyl amino)ethyl methacrylate-co-2-hydroxyethylacrylate) hydrogels

The authors describe a facial development of pH-responsive hydrogels composed of 2-(dimethylamino)ethylmethacrylate and 2-hydroxyethylacrylate via free-radical polymerization at 29°C. The hydrogels were characterized by FTIR, SEM, and XRD studies. The diffusional exponent (n), hydrogel network parameters such as average molecular weight between crosslinks (M_c), and polymer-solvent interaction (χ) were calculated by using swelling data. The hydrogels were encapsulated with 5-fluorouracil, the in vitro release data indicated that the maximum drug release was significantly achieved in pH 1.2 rather than in pH 7.4 and it was enhanced up to 30 h. These results suggested that the gels are highly useful for anticancer drug delivery applications.     

相转移催化合成1-(2,4-二氯苯基)-2-(1-咪唑基)-乙醇的研究

以1-(2,4-二氯苯基)-2-氯-乙醇和咪唑为原料,采用聚乙二醇-400作相转移催化剂合成了1-(2,4-二氯苯基)-2-(1-咪唑基)-乙醇。通过正交试验法考察了催化剂用量、反应温度、反应时间等因素对1-(2,4-二氯苯基)-2-(1-咪唑基)-乙醇收率的影响,确定了最佳的工艺条件。结果表明,聚乙二醇-400使反应选择性高、条件温和、操作简便,收率可达84.6%。     

新型先导化合物2-(2-氯-4-三氟甲基苯氧基)-4-三氟甲基噻唑-5-甲酸乙酯的设计、合成与生物活性

以3-氨基-4,4,4-三氟甲基丁烯酸乙酯为原料,经环化、氯化、醚化制得新型先导化合物2-（2-氯-4-三氟甲基苯氧基）-4-三氟甲基噻唑-5-甲酸乙酯,其结构经红外、核磁、高分辨质谱确认。生物活性测定结果表明新型先导化合物在600g／hm^2剂量下对叶蝉和二点叶螨的防效均为100％;在300g／hm^2剂量下对马铃薯晚疫病的防效为90％。     

Phase behavior on the binary and ternary mixtures of poly(cyclohexyl acrylate) and poly(cyclohexyl methacrylate) in supercritical CO2

High‐pressure phase behavior was measured for the CO₂–cyclohexyl acrylate and CO₂–cyclohexyl methacrylate system at 40, 60, 80, 100, and 120°C and pressure up to 206 bar. This system exhibits type I phase behavior with a continuous mixture‐critical curve. The experimental results for the CO₂–cyclohexyl acrylate and CO₂–cyclohexyl methacrylate system were modeled using the Peng–Robinson equation of state. Experimental cloud‐point data, at a temperature of 250°C and pressure of 2800 bar, were presented for ternary mixtures of poly(cyclohexyl acrylate)–CO₂–cyclohexyl acrylate and poly(cyclohexyl methacrylate)–CO₂–cyclohexyl methacrylate systems. Cloud‐point pressures of poly(cyclohexyl acrylate)–CO₂–cyclohexyl acrylate system were measured in the temperature range of 40 to 180°C and at pressures as high as 2200 bar with cyclohexyl acrylate concentrations of 22.5, 27.4, 33.2, and 39.2 wt %. Results showed that adding 45.6 wt % cyclohexyl acrylate to the poly(cyclohexyl acrylate)–CO₂ mixture significantly changes the phase behavior. This system changed the pressure–temperature slope of the phase behavior curves from the upper critical solution temperature (UCST) region to the lower critical solution temperature (LCST) region with increasing cyclohexyl acrylate concentration. Poly(cyclohexyl acrylate) did not dissolve in pure CO₂ at a temperature of 250°C and pressure of 2800 bar. Also, the ternary poly(cyclohexyl methacrylate)–CO₂–cyclohexyl methacrylate system was measured below 187°C and 2230 bar, and with cosolvent of 27.4–46.7 wt %. Poly(cyclohexyl methacrylate) did not dissolve in pure CO₂ at 240°C and 2500 bar. Also, when 53.5 wt % cyclohexyl methacrylate was added to the poly(cyclohexyl methacrylate)–CO₂ solution, the cloud‐point curve showed the typical appearance of the LCST boundary. © 2004 Wiley Periodicals, Inc. J Appl Polym Sci 94: 1117–1125, 2004     

非水滴定法对氨噻肟酸乙酯含量的测定

根据氮噻肟酸乙酯中含有氨基呈弱碱性的特点，采用冰乙酸作溶剂，以高氯酸标准溶液，在非水条件下进行滴定，经试验证明，此方法简便、快速、灵敏。具有较高的准确度和灵敏度。     

Effect of the octadecyl acrylate concentration on the phase behavior of poly(octadecyl acrylate)/supercritical CO2 and C2H4 at high pressures

Pressure–composition isotherms were measured for the CO₂/octadecyl acrylate system at 45.0, 80.0, and 100.0°C and at pressures up to 307 bar. This system exhibited type I phase behavior with a continuous mixture‐critical curve. The solubility of octadecyl acrylate for the CO₂/octadecyl acrylate system increased as the temperature increased at a constant pressure. The experimental results for the CO₂/octadecyl acrylate system were modeled with the Peng–Robinson equation of state. A good fit of the data was obtained with the Peng–Robinson equation of state with one adjustable parameter for the CO₂/octadecyl acrylate system. Experimental cloud‐point data for the poly(octadecyl acrylate)/CO₂/octadecyl acrylate system were measured from 36 to 193°C and at pressures up to 2100 bar, and the added octadecyl acrylate concentrations were 11.9, 25.9, 28.0, 35.0, and 40.0 wt %. Poly(octadecyl acrylate) dissolved in pure CO₂ up to 250°C and 2100 bar. Also, adding 45.0 wt % octadecyl acrylate to the poly(octadecyl acrylate)/CO₂ solution significantly changed the phase behavior. This system changed the pressure–temperature slope of the phase‐behavior curves from an upper critical solution temperature (UCST) region to a lower critical solution temperature region as the octadecyl acrylate concentration increased. Cloud‐point data to 150°C and 750 bar were examined for poly(octadecyl acrylate)/C₂H₄/octadecyl acrylate mixtures at octadecyl acrylate concentrations of 0.0, 15.0, and 45.0 wt %. The cloud‐point curve of the poly(octadecyl acrylate)/C₂H₄ system was relatively flat at 730 bar between 41 and 150°C. The cloud‐point curves of 15.0 and 45.0 wt % octadecyl acrylate exhibited positive slopes extending to 35°C and approximately 180 bar. © 2002 Wiley Periodicals, Inc. J Appl Polym Sci 86: 372–380, 2002     

相转移催化合成复盆子酮肟

在相转移催化剂聚乙二醇－６００的存在下，复盆子酮与盐酸羟胺室温下反应１小时，制成复盆子酮肟，产率几乎达到定量。     

琥珀酸单-2-(吡啶-2-基)乙醇酯的合成与植物生长调节活性研究

丁二酸酐与2-乙醇吡啶经酯化反应,合成具有植物生长调节活性的新化合物琥珀酸单-2-(吡啶-2-基)乙醇酯。室内活性试验表明,其对玉米有促进生长的作用;进一步田间试验表明,其能够提高小麦产量、千粒重以及穗粒数,且对小麦安全,能够达到甚至略好于市售生长调节剂胺鲜酯(DA-6)的生长促进效果。该化合物合成方法简单,易于工业化生产。