镁掺杂纳米羟基磷灰石的制备及其在载药方面的应用

通过逐步沉淀反应一锅法制备了一系列不同含量的镁掺杂纳米羟基磷灰石。通过硝酸镁、硝酸钙不同的投料物质的量比调控纳米颗粒的形态和尺寸。通过透射电子显微镜（TEM）、X射线衍射（XRD）等分析手段对镁掺杂纳米羟基磷灰石进行物理化学性能表征,用MTT法评价其体外细胞毒性。研究结果表明：镁掺杂纳米羟基磷灰石呈现束状纳米纤维形态、比表面积大、细胞毒性较低;将其作为载体负载抗癌药物顺铂,具有很好的载药能力,载药量可达54%,该载药纳米颗粒还具备缓释特性（72 h释药量达到41.72%）和很好抑制癌细胞生长的效果。     

镁掺杂纳米羟基磷灰石的制备及其在载药方面的应用

通过逐步沉淀反应一锅法制备了一系列不同含量的镁掺杂纳米羟基磷灰石。通过硝酸镁、硝酸钙不同的投料物质的量比调控纳米颗粒的形态和尺寸。通过透射电子显微镜(TEM)、X射线衍射(XRD)等分析手段对镁掺杂纳米羟基磷灰石进行物理化学性能表征,用MTT法评价其体外细胞毒性。研究结果表明:镁掺杂纳米羟基磷灰石呈现束状纳米纤维形态、比表面积大、细胞毒性较低;将其作为载体负载抗癌药物顺铂,具有很好的载药能力,载药量可达54%,该载药纳米颗粒还具备缓释特性(72 h释药量达到41.72%)和很好抑制癌细胞生长的效果。     

叶酸功能化介孔碳纳米球负载阿霉素的细胞靶向传递及可控释放

以粒径90 nm的介孔碳纳米球作为靶向传药载体, 采用酸化处理改进了材料表面的亲疏水性及在溶液中的分散性, 通过壳寡糖功能化, 并利用EDC-NHS将叶酸修饰到介孔碳纳米球表面. 通过共聚焦激光扫描显微镜及流式细胞仪对实验体系的系统研究, 结果表明基于叶酸功能化的介孔碳纳米球能够有效提高负载药物对于HeLa细胞的跨膜转运效率, 叶酸阳性表达的HeLa细胞对于叶酸修饰的介孔碳纳米小球的吞噬效率明显高于叶酸阴性表达的MCF-7细胞. 对HeLa细胞毒性的定量分析表明叶酸的靶向作用在提高介孔碳纳米球内吞效率的同时, 进一步提高了阿霉素对于HeLa细胞的毒性.     

多孔羟基磷灰石纳米球作为抗坏血酸载体的研究

利用超声辅助的化学共沉淀法制备了羟基磷灰石纳米材料, 并实现了其对抗坏血酸的包载. 采用透射电镜、氮气吸附孔径分析仪、X射线粉末衍射仪、傅里叶红外光谱仪和紫外分光光度计等对所得纳米材料的微观形貌、孔径分布、物相、表面官能团和负载抗坏血酸量进行了表征和分析, 并在超声辅助条件下进行了药物释放动力学研究. 结果表明, 在抗坏血酸存在的条件下, 利用声化学方法可以制得多孔的羟基磷灰石纳米球, 其平均直径约为140 nm, 平均孔直径约为15 nm, 可实现对抗坏血酸的包载. 此外, 在超声辅助的条件下, 该纳米球具有持续释药的能力, 不同的超声功率能改变载药粒的释药速度, 表明这种多孔羟基磷灰石纳米球是一种具有很大应用前景的骨组织药物载体.     

原位复合法制备层状结构的壳聚糖/羟基磷灰石纳米材料

用原位复合法制备了高性能的壳聚糖/羟基磷灰石(CS/HA)纳米复合材料.用预先沉积的壳聚糖膜将含有羟基磷灰石前驱体的壳聚糖溶液与凝固液隔离,同时控制壳聚糖沉积与羟基磷灰石前驱体转化为羟基磷灰石的过程,使其缓慢且有序地进行.当pH值改变时,质子化的壳聚糖分子链在负电层诱导下有序沉积并形成层状结构与羟基磷灰石原位生成CS/HA,并实现二者分子级复合.XRD和TEM测试证实原位生成的磷酸盐是羟基磷灰石,且其颗粒长约为100nm,宽30～50nm.SEM结果表明,用原位复合法制备的材料具有层状结构,CS/HA(质量比100/5)纳米复合材料弯曲强度高达86MPa,比松质骨的高3～4倍,相当于密质骨的1/2,有望用于可承重部位的组织修复材料.     

成骨肿瘤细胞在纳米氧化钛陶瓷表面的生物活性研究

以羟基磷灰石和氧化镁为晶粒生长抑制剂制备的纳米氧化钛陶瓷为研究对象, 采用体外成骨细胞Ros17/28与材料复合培养的方法, 通过MTT法、荧光染色法和SEM细胞形貌观察等手段综合判断细胞在材料表面的活性, 以此评价纳米氧化钛陶瓷的生物活性. 结果表明, 以羟基磷灰石为晶粒生长抑制剂的氧化钛陶瓷晶体颗粒尺寸达到纳米级, 其生物活性超出了以氧化镁为晶粒生长抑制剂的氧化钛陶瓷和纯羟基磷灰石陶瓷, 具有优异的生物相容性, 是生物活性陶瓷.     

纳米羟基磷灰石/丝素蛋白复合支架材料的降解特性及生物相容性研究

应用共混法制备了纳米羟基磷灰石/丝素蛋白复合支架材料, 通过体外降解和细胞培养实验研究了复合支架材料的降解特性和生物相容性. 体外降解实验结果显示, 复合支架材料具有稳定的降解能力; 在降解过程中, 羟基磷灰石由于与降解液发生钙、磷等离子的交换, 使其结晶得到了进一步生长和完善. 利用细胞计数法、四甲基偶氮唑盐(MTT)比色法和碱性磷酸酶(ALP)活性测定等分析了复合支架材料的生物相容性, 结果表明, MG63细胞在复合支架材料上具有良好的粘附、增殖能力, 并可引起早期的骨分化. 因此, 纳米羟基磷灰石/丝素蛋白复合支架作为骨组织工程的支架材料具有良好的应用前景.     

有机/无机复合介孔膜的合成及其生物酶吸附行为研究

以正硅酸四乙酯(TEOS)为硅源、三嵌段共聚物(F127)为表面活性剂, 聚碳酸酯膜为硬模板, 并采用抽滤法在聚碳酸酯膜内的亚微米级孔道中组装介孔氧化硅从而制备出有机(聚碳酸酯)/无机(介孔氧化硅)复合介孔膜. 通过扫描电镜、能量分散光谱以及透射电镜等实验表征了该有机/无机复合介孔膜的组成、结构及形貌. 研究结果表明: 通过该方法可以在聚碳酸酯膜内孔道中形成长度为9 μm、直径为200 nm的一维氧化硅棒状材料, 且该棒状材料具有无序蠕虫状和有序体心立方的混合介孔结构, 有序体心立方介孔的平均孔径约为8.5 nm. 另外, 初步考察了该复合介孔膜对生物酶的物理吸附行为, 结果表明其对肌红蛋白酶的单位吸附负载量为5.85 mg/g.     

新型介孔羟基磷灰石/壳聚糖-万古霉素药物释放系统复合材料的制备及体外抗菌和成骨能力

采用冷冻干燥法合成了介孔羟基磷灰石(HA)/壳聚糖(CS)-万古霉素(VCM)药物释放系统复合材料, 利用SEM, XRD和FTIR等方法对材料进行了表征. 结果证实CS与HA混合复合材料具有良好的孔径和孔隙率, 万古霉素吸附于复合材料的表面和内部. 细胞毒性实验[噻唑蓝(MTT)比色法]结果表明, 材料可以促进成骨细胞增殖且具有良好的细胞相容性. 体外抑菌实验结果证实此材料可长时间抑制耐甲氧西林金葡菌(MRSA)的生长, 具有良好的抑菌和杀菌能力. 细胞黏附实验结果表明, 成骨细胞附着于材料表面增殖并通过孔道延伸. 实时聚合酶链式反应(RT-PCR)实验结果表明, 在成骨相关标志产物胶原蛋白-1(COL-1)及骨形态发生蛋白-2(BMP-2)基因上均有较高的表达, 表明材料在体外可以促进成骨细胞生长, 具有良好的成骨能力.     

In This Issue

正封面:面向能源、环境、绿色化工等领域的广泛需求,近年来多种新型多孔材料问世,其中介孔材料、杂化多孔固体如金属有机骨架结构等具有有序孔道结构的催化材料得到蓬勃发展,本期"新型多孔催化材料"专栏,封面选载了3篇报道,分别为可高效催化甲醇电催化氧化且抗CO中毒的介孔碳负载PtRu等合金催化剂、低温氧化甲醛的三维有序介孔MnO_2材料、具有优异硝基苯催化加氢活性的MIL-101负载NiPd核壳纳米催化剂.     

Electromembrane extraction of peptides--fundamental studies on the supported liquid membrane

A large screening of different components in the supported liquid membrane (SLM) in electromembrane extraction (EME) was performed to test the extraction efficiency on eight model peptides. Electromembrane extraction from a 500 μL acidified aqueous sample containing the model peptides in the concentration 10 μg/mL was used. Extraction time was 5 min with an electric potential of 10 V and 900 rpm agitation of the sample vial. The samples were extracted through a hollow fiber-based SLM with different compositions of organic solvents and carriers. A small volume of acidified acceptor solution (25 μL) was after extraction analyzed directly, or with some dilution, on CE or HPLC. This article has identified mono- or di-substituted phosphate groups as the prominent group of carrier molecules needed to obtain acceptable recoveries. For the organic solvents, primary alcohols and ketones have shown promise regarding recovery and reproducibility, with some differences in selectivity. A new composition of the SLM, namely 2-octanone and tridecyl phosphate (90:10 w/w) has proved to give higher extraction recoveries and lower standard deviation than SLMs previously reported in the literature.     

Stability and efficiency of supported liquid membranes in electromembrane extraction—a link to solvent properties

The current work presents a large systematic screening of 61 possible organic solvents used as supported liquid membranes (SLM) in electromembrane extraction (EME). For each organic solvent, recovery, current across the SLM, and stability considerations have been investigated and correlated to relevant solvent properties through partial least square regression analysis. The five unpolar basic drugs pethidine, haloperidol, methadone, nortriptyline, and loperamide were used as model analytes. Efficient EME solvents were found to have a low water solubility (<0.5 g L^?1) and belonged to cluster 2 of a Kamlet–and–Taft-based solvent classification system (high dipole moments and proton acceptor properties). These parameters were especially found in nitroaromatic compounds and ketones. Small molecules with low log P value and high water solubility were unsuitable, as they tended to give unstable extractions, caused by a high current across the SLM. This was often combined with substantial solvent-related interferences and the generation of an electroosmotic flow across the SLM, with resulting acceptor solution expansion. Large molecules with a high log P value were classified as inefficient. For these solvents, no current was measured across the SLM and no analytes were extracted. This is the first time systematic knowledge on the SLM in EME has been gathered and investigated, and the presented results could be highly beneficial for future development and optimization of EME.     

Optical resolution of various amino acids using a supported liquid membrane encapsulating a surfactant-protease complex

We have encapsulated a surfactant-protease complex (the main protease used being alpha-chymotrypsin) in an organic phase of a supported liquid membrane (SLM) for the optical resolution of various amino acids. L-Isomers of amino acids were enantioselectively permeated through the SLM. The mechanism of the amino acid permeation through the SLM was considered to be as follows; an L-amino acid was enantioselectively esterified with ethanol by a surfactant-protease complex encapsulated in the SLM, and the resulting L-amino acid ethyl ester dissolved into the organic phase of the SLM and diffused across the SLM. Another surfactant-alpha-chymotrypsin complex in the receiving phase catalyzed ester hydrolysis to produce the initial L-amino acid and ethanol, which are water-soluble. Thus, the L-amino acid was selectively transported to the receiving phase through the SLM on the basis of the molecular recognition of the surfactant-protease complex in the SLM. It was found that the catalytic activity and enantioselectivity of the surfactant-protease complex governed the permeate flux of amino acids and the enantiomeric excess in the membrane separation.     

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.     

Environmental and bioanalytical applications of hollow fiber membrane liquid-phase microextraction: a review

In hollow fiber membrane liquid-phase microextraction (LPME), target analytes are extracted from aqueous samples and into a supported liquid membrane (SLM) sustained in the pores in the wall of a small porous hollow fiber, and further into an acceptor phase present inside the lumen of the hollow fiber. The acceptor phase can be organic, providing a two-phase extraction system compatible with capillary gas chromatography, or the acceptor phase can be aqueous resulting in a three-phase system compatible with high-performance liquid chromatography or capillary electrophoresis. Due to high enrichment, efficient sample clean-up, and the low consumption of organic solvent, substantial interest has been devoted to LPME in recent years. This paper reviews important applications of LPME with special focus on bioanalytical and environmental chemistry, and also covers a new possible direction for LPME namely electromembrane extraction, where analytes are extracted through the SLM and into the acceptor phase by the application of electrical potentials.     

Combined use of supported liquid membrane and solid-phase extraction to enhance selectivity and sensitivity in capillary electrophoresis for the determination of ochratoxin A in wine

This paper proposes a novel strategy to enhance selectivity and sensitivity in CE, using supported liquid membrane (SLM) and off-line SPE simultaneously. The determination of ochratoxin A (OA) in wine has been used to demonstrate the potential of this methodology. In the SLM step, the donor phase (either a 20 mL volume of a standard solution at pH 1 or a wine sample at pH 8) was placed in a vial, where a micromembrane extraction unit accommodating the acceptor phase (1 mL water, pH 11) in its lumen was immersed. The SLM was constructed by impregnating a porous Fluoropore Teflon (PTFE) membrane with a water-immiscible organic solvent (octanol). In the off-line SPE step, the nonpolar sorbent (C-18, 4 mg) selectively retained the target ochratoxin, enabling small volumes of acceptor phase (1 mL) to be introduced. The captured analytes were eluted in a small volume of methanol (0.1 mL). This procedure resulted in sample cleanup and concentration enhancement. The method was evaluated for accuracy and precision, and its RSD found to be 5%. The LODs for OA in the standard solutions and wine samples were 0.5 and 30 microg/L, respectively. The results obtained demonstrate that SLM combined with off-line is a good alternative to the use of immunoaffinity columns prior to CE analysis.     

Rapid and efficient microwave-assisted synthesis of highly sulfated organic scaffolds

Sulfation of multiple hydroxylated small organic molecules is fraught with problems of poor yield, multitude of products, and long reaction times. We have developed a rapid microwave-based method for synthesis of highly sulfated small organic molecules, which affords the per-sulfated product in moderate to excellent yields and high purity. The method is expected to be of value in the discovery of per-sulfated organic molecules as mimics of glycosaminoglycans, which are being increasingly recognized as modulators of key physiological functions.     

A supported liquid membrane encapsulating a surfactant-lipase complex for the selective separation of organic acids

We have developed a novel, lipase-facilitated, supported liquid membrane (SLM) for the selective separation of organic acids by encapsulating a surfactant-lipase complex in the liquid membrane phase. This system exhibited a high transport efficiency for 3-phenoxypropionic acid and enabled the selective separation of organic acids due to the different solubilities of the acids in the organic phase and the variable substrate specificity of the surfactant-lipase complex in the liquid membrane phase. We found that various parameters, such as the amount of surfactant-lipase complex in the SLM, the lipase concentration in the receiving phase, and the ethanol concentration in the feed phase, affected the transport behavior of organic acids. The optimum conditions were 5 g L(-1) of the surfactant-CRL complex in the SLM (CRL=lipase from Candida rugosa), 8 g L(-1) of PPL in the receiving phase (PPL=lipase from porcine pancreas), and an ethanol concentration of 50 vol %. Furthermore, we achieved high enantioselective transport of (S)-ibuprofen attributable to the enantioselectivity of the surfactant-CRL complex.     

Kinetic aspects of hollow fiber liquid-phase microextraction and electromembrane extraction

In this paper, extraction kinetics was investigated experimentally and theoretically in hollow fiber liquid-phase microextraction (HF-LPME) and electromembrane extraction (EME) with the basic drugs droperidol, haloperidol, nortriptyline, clomipramine, and clemastine as model analytes. In HF-LPME, the analytes were extracted by passive diffusion from an alkaline sample, through a (organic) supported liquid membrane (SLM) and into an acidic acceptor solution. In EME, the analytes were extracted by electrokinetic migration from an acidic sample, through the SLM, and into an acidic acceptor solution by application of an electrical potential across the SLM. In both HF-LPME and EME, the sample (donor solution) was found to be rapidly depleted for analyte. In HF-LPME, the mass transfer across the SLM was slow, and this was found to be the rate limiting step of HF-LPME. This finding is in contrast to earlier discussions in the literature suggesting that mass transfer across the boundary layer at the donor–SLM interface is the rate limiting step of HF-LPME. In EME, mass transfer across the SLM was much more rapid due to electrokinetic migration. Nevertheless, mass transfer across the SLM was rate limiting even in EME. Theoretical models were developed to describe the kinetics in HF-LPME, in agreement with the experimental findings. In HF-LPME, the extraction efficiency was found to be maintained even if pH in the donor solution was lowered from 10 to 7–8, which was below the pK_a-value for several of the analytes. Similarly, in EME, the extraction efficiency was found to be maintained even if pH in the donor solution increased from 4 to 11, which was above the pK_a-value for several of the analytes. The two latter experiments suggested that both techniques may be used to effectively extract analytes from samples in a broader pH range as compared to the pH range recommended in the literature.     

Continuous flow liquid membrane extraction: a novel automatic trace-enrichment technique based on continuous flow liquid-liquid extraction combined with supported liquid membrane

Combining the continuous flow liquid-liquid extraction (CFLLE) and supported liquid membrane (SLM) extraction, a novel aqueous-aqueous extraction technique that we termed continuous flow liquid membrane extraction (CFLME) is developed for trace-enrichment. The analyte was firstly extracted into the organic phase in the CFLLE step, then transported onto the organic liquid membrane that formed on the surface of the micro porous membrane of the SLM equipment. Finally, it passed through the liquid membrane and was trapped by the acceptor. Aspects related to CFLME were studied by using dichloromethane as liquid membrane, and sulfonylurea herbicides as model compounds. An enrichment factor of over 1000 was obtained when 10 μg l⁻¹ of MSM was enriched for 120 min by this technique. The drawbacks of only a few organic solvents can be selected as liquid membrane with a limited lifetime in SLM operation was overcome. In this CFLME method, almost all solvents that used in the conventional liquid-liquid extraction (LLE) can be adopted and the lifetime of liquid membrane is no longer a problem.