超稠油污水处理技术的研究

以河油田曙I区社84污水处理站含超稠油污水为对象，选用最新研制开发的HL－005高效除油剂，研究了药剂浓度及复合比例对污水的处理效果。结果表明，在现有工艺条件下，使用该药A与C两组分复合先对污水进行预处理,然后A与B两组分复合对预处理后的水质进行净化，在技术上是可行的，完全达到水质净化指标。     

The kinetics of desorption in the presence of a gas phase of the desorbing molecule: CO/Re(001)

TPD/Exchange from CO/Re(001) in a gas ambience showed that the absolute rate of desorption depends on the gas pressure and has a first plus second order rate law. It is proposed that desorption is a two step process from the adsorbed state to a stable intermediate which is itself weakly adsorbed.     

中温耐热炻瓷色釉的研制

详细介绍了中温耐热炻瓷的研制配方及工艺参数，并初步分析了耐热炻瓷的机理，该耐热炻瓷热稳定性通过了260—20℃热交换一次不裂，符合客户使用要求。     

新型组合工艺对微污染原水中有机污染物和消毒副产物前体物的去除

本采用中试试验装置研究了生物陶粒过滤一微絮凝砂滤一活性炭吸附组合工艺，对微污染原水中有机污染物和消毒副产物前体物的去除效果。在原水UV254为0．047～0．065cm^-1，DOC为2．70～4．10mg／L，TOC为3．50～5．00mg／L的条件下，组合工艺对UV254，DOC、TOC平均去除率分别为98．4％、74．1％、69．2％。色-质联机分析结果表明，经组合工艺处理水中有机物由54种降至25种。组合工艺出水中三卤甲烷总含量不及常规工艺出水中该物质含量的五分之一。组合工艺能有效控制和消除水中有机物的污染，提供安全的优质饮用水。     

Decolorization of reactive brilliant red X-3B by heterogeneous photo-Fenton reaction using an Fe–Ce bimetal catalyst

Decolorization of reactive brilliant red X-3B was studied by using an Fe–Ce oxide hydrate as the heterogeneous catalyst in the presence of H₂O₂ and UV. The decolorization rate was in the order of UV–Fe–Ce–H₂O₂ > UV–Fe³⁺–H₂O₂ > UV–H₂O₂ > UV–Fe–Ce ≥ Fe–Ce–H₂O₂ > Fe–Ce. Under the conditions of 34 mg l⁻¹ H₂O₂, 0.500 g l⁻¹ Fe–Ce, 36 W UV and pH 3.0, 100 mg l⁻¹ X-3B could be decolorized at efficiency of more than 99% within 30 min. The maximum dissolved Fe during the reaction was 1 mg l⁻¹. From the fact that the decolorization rate of the UV–Fe–Ce–H₂O₂ system was significantly higher than that of the UV–Fe³⁺–H₂O₂ system at Fe³⁺ = 1 mg l⁻¹, it is clear that the Fe–Ce functioned mainly as an efficient heterogeneous catalyst. UV–vis, its second derivative spectra, and ion chromatography (IC) were employed to investigate the degradation pathway. Fast degradation after adsorption of X-3B is the dominant mechanism in the heterogeneous catalytic oxidation system. The first degradation step is the breaking down of azo and CN bonds, resulting in the formation of the aniline- and phenol-like compounds. Then, the breaking down of the triazine structure occurred together with the transformation of naphthalene rings to multi-substituted benzene, and the cutting off of sulphonic groups from the naphthalene rings. The last step includes further decomposition of the aniline structure and partial mineralization of X-3B.     

Effect of solution properties on nanofibrous structure of electrospun poly(lactic‐co‐glycolic acid)

Electrospinning of poly(lactic‐co‐glycolic acid) (PLGA) in chloroform or 1,1,1,3,3,3‐hexafluoro‐2‐propanol (HFIP) was investigated, focusing on its solution parameters, to develop nonwoven biodegradable nanofibrous structures for tissue engineering. PLGA nanofibers were obtained by electrospinning of 15 wt % PLGA solution and the resulting average fiber diameters were varied with the range of 270–760 nm, depending on solution property. When small amounts of benzyl triethylammonium chloride (BTEAC) was added to the PLGA/chloroform solution, the average diameter was decreased from 760 to 450 nm and the fibers were densely amounted in a straight shape. In addition, the average fiber diameter (270 nm) of nanofibers electrospun from polar HFIP solvent was much smaller than that (760 nm) of nanofibers electrospun from nonpolar chloroform solvent. Therefore, it could be concluded that conductivity or dielectric constant of the PLGA solution was a major parameter affecting the morphology and diameter of the electrospun PLGA fibers. © 2005 Wiley Periodicals, Inc. J Appl Polym Sci 99: 1214–1221, 2006     

催化无基体法制备碳纳米管

用一种新的催化裂解法 ,制备出了直径在 2 0～ 30nm ,长度为 2 0 0 μm的碳纳米管。在此方法中 ,繁琐的催化剂制备工艺被省略 ,催化剂前驱体在载气带动下直接进入反应器。另外还发现两类结构独特的碳纳米管。     

超临界水中氧化钙催化泥炭制氢

使用间歇式超临界水反应器,以氧化钙作为催化剂和CO_2化学固定剂,详细考察了Ca/C摩尔比、反应温度、停留时间、压力等条件对泥炭在超临界水中转化制氢的影响。在873 K,Ca/C比为0.61时,CO_2几乎被完全固定,在气相产物中只有氢气、甲烷和低碳烃,碳转化率由未添加CaO时的66.6％提高到82.4％,氢气的产率由2.2 mmol·g~(-1)提高到6.9 mmol·g~(-1)。当反应温度由773 K提高到923 K时,泥炭的裂解反应加剧,气体产物的收率由5.5 mmol·g~(-1)提高到19.5 mmol·g~(-1),但是氢气所占比例由55.4％下降到34.8％。与温度相比,压力和在终温停留时间的影响相对较小。     

多孔塑料管材挤出工艺和机头模具

扼要介绍了多孔塑料管材的用途、性能、制造方法、配方、生产工艺和机头模具的设计     

复合溶液膜吸收CO2的性能及其对膜孔润湿的影响

利用自行搭建的CO₂膜吸收实验台，采用聚丙烯（PP）膜组件，以质量分数10%的N-甲基二乙醇胺（MDEA）作为主体胺溶液，添加不同配比的哌嗪（PZ）、乙醇胺（MEA）、甘氨酸钾（PG），考察CO₂脱除效率和传质速率的变化，比较不同复配比的复合溶液表面张力以及对PP膜的浸润性，并以10%MDEA+10%PG混合溶液作为吸收液进行长时间实验。结果表明：添加少量的添加剂对MDEA溶液膜吸收CO₂均有显著的促进作用，当配比小于0.2时，促进作用大小为PZ>MEA>PG；当配比大于0.2时，促进作用大小为PZ>PG>MEA；PZ和MEA均随着添加配比的增加，溶液表面张力减小，而PG相反；表面张力小的溶液对膜浸润性较强，容易造成膜润湿；添加剂质量分数均为10%时，对膜溶胀性和疏水性以及膜孔结构影响大小为PZ>MEA>PG；在20天内，PG/MDEA混合溶液作用下的CO₂脱除效率从89.56%下降为83.09%，对PP的疏水性影响较小，膜组件可以稳定运行。吸收液表面张力对膜吸收法脱除CO₂性能的影响显著。所得结果可为膜吸收CO₂吸收剂复配提供依据，并可为揭示膜吸收CO₂过程中膜润湿导致膜失效的机理以及抑制膜润湿提供实验数据。