NaX分子筛填充PDMS膜对丙烯／丙烷分离性能的研究

采用了对丙烯／丙烷有吸附选择性的NaX型分子筛填充PDMS,通过真空涂敷法涂敷至PPESK／PEI中空纤维基膜上,制备了NaX／PDMS中空纤维复合膜。研究了固化温度、固化时间、涂敷时间（抽真空时间）、NaX填充含量对丙烯／丙烷分离性能的影响。实验结果表明,室温下,在固化温度80℃,固化时间80min,涂敷时间6min,NaX填充含量30％时,复合膜对丙烯,丙烷的分离性能最佳,分离系数达到2．68。为丙烯／丙烷的分离提供了一种新的可能性,开辟了一条研制高性能丙烯／丙烷分离有机膜的新途径。     

羟基化PPESK复合膜的制备及性能研究

采用NaBH₄对杂萘联苯聚芳醚砜酮(PPESK)支撑膜进行羟基化亲水改性,通过间苯二胺和均苯三甲酰氯的界面聚合反应制备复合膜。利用傅里叶变换红外光谱仪(FT-IR)、水接触角仪、扫描电子显微镜(SEM)和X射线光电子能谱仪(XPS)研究羟基化改性对膜表面的形貌结构、原子组成的影响,并测定复合膜对2 000 mg·L^-1 Na₂SO₄水溶液的分离性能。结果表明：羟基化改性的PPESK-OH支撑膜的亲水性增强;PPESK-OH复合膜的聚酰胺层的交联度较高;PPESK-OH复合膜和PPESK复合膜的脱盐率接近,PPESK-OH复合膜的水通量较PPESK复合膜增大了约38%。     

丙烷脱氢制丙烯低温分离工艺分析

为确立丙烷脱氢制丙烯工艺中低温分离单元的最佳制冷流程,采用PRO/Ⅱ8.2化工流程模拟软件,对低温分离单元进行模拟计算,考察了温度和压力对低温分离效果的影响,分析并确立了最佳分离温度和压力范围;在分离效果相同的前提下,分别比较了丙烯+乙烯级联制冷、丙烯预冷+混合制冷和丙烯预冷+富氢气膨胀制冷3种制冷流程的公用工程消耗以及各自的优缺点。结果表明:产品压缩机出口压力对分离效果影响较小,在确保下游装置能够正常操作的情况下,分离压力应尽可能低;分离温度是影响分离效果的主要因素,较为经济的分离温度为-90—-100℃;相对于其他2种流程,丙烯+乙烯级联制冷流程具有技术成熟、能耗低和操作简单等优点,更适合于丙烷脱氢制丙烯工艺。     

PPESK／PS共混物流变性能的研究

以溶液共沉淀的方法制备了含二氮杂萘联本结构的聚芳醚砜酮（PPESK）。聚苯乙烯（PS）共混物，用毛细管流变仪测定了共混物的流为性能。结果表明，在本实验条件下，PPESK／PS共混物熔体属假塑性非牛顿汉体，其熔体粘度随PS含量的增加、温度的升高、剪切速率的增大而下降。PS的加入有利于改善PPESK的熔融加工流动性。     

CS/PS中空纤维复合膜脱除丙烯中微量水分的研究

采用涂敷法制备了壳聚糖(CS)／聚砜(PS)中空纤维复合膜,考察了气相丙烯中脱除微量水分的蒸汽渗透性能。分析讨论了PS基膜、CS脱乙酰度(DD)、CS的浓度、交联剂种类及其用量和热处理温度对膜蒸汽渗透性能的影响。结果表明,在一定的制膜条件及渗透工艺条件下,对于水分含量为0．3127％的气相丙烯,水渗透通量为9．89g／m^2．h;分离因子为1412．5。     

聚芳醚砜酮纤维的热性能

采用DSC、TG测定了含联苯结构聚芳醚砜酮 (PPESK)纤维的热性能 ,结果表明 ,纤维的玻璃化温度随砜酮比的增大而提高 ,纤维的起始分解温度大于 463℃。当砜酮比为 15 / 85 ,5 0 / 5 0 ,75 / 2 5时 ,纤维的玻璃化温度分别为 2 5 7.62 ,2 78.64 ,2 79.71℃ ;热分解活化能分别为 15 0 .8,2 19.9,195 .5kJ/mol;热分解反应级数分别为 1,1.76,1级     

工艺参数对静电纺PPESK微纳米纤维膜性能的影响

通过溶液静电纺丝法制备了聚芳醚砜酮(PPESK)微纳米纤维膜,借助于扫描电子显微镜和拉伸试验机分别对纤维膜的形貌和力学性能进行了表征,用正交试验对微纳米纤维膜的制备工艺参数进行了优化。结果表明,在给定条件下,对纤维直径影响由大到小的工艺参数依次为:溶液浓度给料速度纺丝电压。纤维直径最小的工艺条件为:溶液浓度19%,纺丝电压10 k V,给料速度为0.04 mm/min。对纤维膜拉伸强度影响由大到小的工艺参数依次为:给料速度纺丝电压溶液浓度。纤维拉伸强度最大的工艺条件为:溶液浓度24%,纺丝电压14 k V,给料速度0.04 mm/min。     

原料丙烯中丙烷含量升高对装置生产的影响

从生产装置的实际出发，总结了原料丙烯中丙烷含量升高对装置生产控制、经济技术指标的影响，指出不影响聚丙烯装置运行的最低丙烯纯度为99．36％。     

间位苯基取代聚芳醚砜醚酮酮的合成与性能研究

以4,4′-二苯氧基二苯砜(DPODPS)、对苯二甲酰氯(TPC)和间苯二甲酰氯(IPC)为单体,无水AlCl3/二氯乙烷(DCE)/N,N-甲基甲酰胺(DMF)为催化溶剂体系,通过低温溶液共缩聚反应,合成系列聚芳醚砜醚酮酮(PESEKKs),用IR、DSC、WAXD、TG等技术对聚合物进行了结构和性能的表征,研究结果表明,随着高分子主链中间位苯基结构单元的增加,对共聚玻璃化转变温度(Tg)和热分解温度(Td)影响不大,熔融温度(Tm)和结晶则逐渐降低,但仍保持良好的耐热性,溶解性等到很大改善。     

耐高温含氟聚芳醚酮和聚芳醚砜的合成与性能研究

通过三步反应合成新的含氟双酚单体3,4-二氟苯基对苯二酚,由该含氟双酚单体、4-氟苯基对苯二酚、邻苯基对苯二酚分别与4,4′-二氟二苯酮、4,4′-二氯二苯砜经亲核缩聚反应,制备了一系列新型聚芳醚酮和聚芳醚砜。采用 FT-IR、DSC、TGA及XRD手段等对聚合物的结构和性能进行了表征和研究,结果表明：合成的聚芳醚酮和聚芳醚砜具有优异的耐热性能,玻璃化转变温度分别在150~159 ℃和177~196 ℃之间,氮气中5 %热失重温度分别在527 ℃和507 ℃以上。合成的聚芳醚酮和聚芳醚砜具有良好的溶解性,室温下能溶解在N-甲基吡咯烷酮、二甲基乙酰胺、氯仿等有机溶剂中。     

分子印迹纤维膜富集分离白藜芦醇的研究

以白藜芦醇为模板分予,聚偏氟乙烯中空纤维膜为支撑体,采用自由基热聚合法制各自藜芦醇分子印迹复合膜,对膜分离性能进行了测试。结果表明,当萃取剂为纯甲醇时,物质透过膜的魁很少,印迹膜体现出对模板分子的吸附选择性;当萃取剂为0．3％冰醋酸．甲醇时,印迹膜呈现对模板分子的透过选择性。     

纳米Al2O3粒子对PVDF中空纤维膜的改性研究

文章介绍了在聚偏氟乙烯铸膜液中添加了无机钠米Al2O3粒子,采用相转化法制备了Al2O3/PVDF复合中空纤维膜。使用电镜对膜的微观结构进行了分析,初步研究了无机粒子在膜孔形成的过程中所起的作用和机理。并且对膜的孔隙率、最大孔径、力学性能和截留率进行了分析。结果表明复合膜的性能与纯PVDF膜的相比有显著提高,最大孔径从0.75μm降至0.39μm,水通量和截留率分别从10.09 L/m2.h和19.12%提高到28.25 L/m2.h和71.00%,断裂应力从3.09 MPa提高到3.41 MPa。     

PVDF-TiO2复合中空纤维膜的制备与表征

将纳米二氧化钛(TiO₂)粒子与4类制膜添加剂复配处理,采用相转化法制备聚偏氟乙烯(PVDF)-TiO₂复合中空纤维膜,讨论了纳米TiO₂粒子对复合膜结构和性能的影响。通过扫描电子显微镜、X射线衍射、能谱分析、热重分析、拉伸试验、接触角测定和超滤实验分别表征了复合膜的微观孔结构、晶相结构和复合均匀性、热稳定性、机械性能、亲水性、超滤性能以及抗污染性能。结果表明：通过添加TiO₂粒子复配添加剂,复合膜的性能得到有效改善。复配添加剂中w(TiO₂)为2%(占PVDF固含量的质量分数)时,纯水通量由348 L/(m²·h)提高至377 L/(m²·h),牛血清蛋白截留率由68%提高至90%,断裂强度和抗污染性能提高,复合膜综合性能优异。     

Effect of Hydrogen Reduction of Silver Ions on the Performance and Structure of New Solid Polymer Electrolyte PEI/Pebax2533/AgBF4 Composite Membranes

In this paper, the effect of hydrogen reduction of silver ions on the performance and structure of new solid polymer electrolyte polyetherimide (PEI)/Pebax2533 (Polynylon12/tetramethylene oxide block copolymer, PA12-PTMO)/AgBF₄ composite membranes is investigated. For PEI/Pebax2533/AgBF₄ composite membranes prepared with different AgBF₄ concentration, the permeances of propylene and ethylene increase with the increase of AgBF₄ concentration due to the carrier-facilitated transport, resulting in a high selectivity. But for propylene/propane mixture, the mixed-gas selectivity is lower than its ideal selectivity. The hydrogen reduction strongly influences the membrane performance, which causes the decrease of propylene permeance and the increase of propane permeance. With the increase of hydrogen reduction time, the membranes show a clearly color change from white to brown, yielding a great selectivity loss. The data of X-ray diffraction and FT-IR prove that silver ions are reduced to Ag⁰ after hydrogen reduction, and aggregated on the surface of PEI/Pebax2533/AgBF₄ composite membranes.     

中空纤维PVA/PAN复合膜填料的乙醇水溶液精馏性能

以乙醇/水溶液为分离对象,中空纤维PVA/PAN复合膜作为精馏填料,考察了不同膜组件的传质分离效率。实验结果表明:各种组件的分离效率均随塔釜加热功率的增加而减小;和大多数中空纤维膜接触器一样,其总传质系数Ky随中空纤维膜组件填充密度φ的增加而减少;相比于传统精馏填料而言,用中空纤维膜做精馏填料分离乙醇水溶液的分离效果更好,可以在常规填料不能操作的液泛线以上进行操作。当塔釜加热功率为120 W,45根中空纤维膜封装在内径为1.6 cm玻璃管中的传质单元高度(HTU)为5.64 cm。     

聚偏氟乙烯中空纤维膜的开发与应用进展

介绍了中空纤维膜的性能,生产的主要技术工艺与最佳的操作条件及有关进展情况。阐述了国内外研究开发的现状与发展趋势,并探讨了扩大应用范围等的前景与市场需求。     

气体分离用聚砜中空纤维膜的活化涂敷技术

主要探讨了一些表面活性剂对气体分离用聚砜中空纤维膜表面涂敷上的作用。结果表明 ,其中TO 80对提高H2 /N2 分离系数的效果最佳。     

Mathematical Model for the Extraction of Neodymium from Nitrate Media using Hollow Fiber Supported Liquid Membrane Operated in a Recycling Mode

A mathematical model for facilitated extraction of Neodymium (Nd³⁺) ions from nitrate media using microporous hollow fiber supported liquid membrane (HFSLM) operated in a recycling mode is presented. Extractant N,N,N′, N′-tetraoctyl diglycolamide (TODGA) diluted with n-dodecane was used as the membrane phase. Di-n-hexyl octanamide (DHOA) has been used as a phase modifier for the extractant. The model developed is not specific to the case considered and has a more general and wide applicability. The model has been developed using equilibrium-based approach. The complexation and de-complexation reactions were assumed to be fast and at equilibrium. Mass balance equations for both acid (HNO₃) and TODGA were also incorporated in the model. It was observed that the model results are in good agreement with the experimental data when diffusivity of metal-complex (D _m ) and acid-complex (D _hm ) through the membrane phase in the pore is 6 × 10^?12 m²/s and 1.2 × 10^?10 m²/s. Once the values of D _m and D _hm are estimated by simulation for one set of data, there are no further fitting parameters in the model. The model can then be used in a truly predictive mode for all the remaining data sets.     

The Transport of Copper(II) through Hollow Fiber Renewal Liquid Membrane and Hollow Fiber Supported Liquid Membrane

Abstract

In this paper, hollow fiber renewal liquid membrane (HFRLM) and hollow fiber supported liquid membrane (HFSLM) were used to simultaneously remove and recover copper(II) from aqueous solutions, and the transport performance of these two techniques were compared under the similar conditions for the system of CuSO₄ +D2EHPA in kerosene +HCl. The results showed that the HFRLM process was more stable than the HFSLM process. The HFRLM process had a higher overall mass transfer coefficient than that of HFSLM process in single-pass experiments. These were because the renewal effect of the liquid membrane layer could reduce the mass transfer resistance of the lumen side and replenish the loss of the membrane liquid in the HFRLM process. The transport results were better in the HFRLM process than that in the HFSLM process with recycling experiments. Therefore, HFRLM technique is a promising method for simultaneous removal and recovery of heavy metal from aqueous solutions.