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991.
甲壳质纤维的制备及应用 总被引:10,自引:0,他引:10
甲壳质及其衍生物具有天然的生物活性及良好的成膜成纤性能 ,已被广泛地应用到医药、纺织、食品、化工等多个领域。介绍了甲壳素纤维的制备、性能 ,并简述其在纺织领域中的应用 相似文献
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995.
Keiichi Tomishige Yutaka Furusawa Yoshiki Ikeda Mohammad Asadullah Kaoru Fujimoto 《Catalysis Letters》2001,76(1-2):71-74
CeO2–ZrO2 solid solution catalysts are very effective for the selective synthesis of dimethyl carbonate from methanol and CO2. The activity was much dependent on the calcination temperature. The higher the calcination temperature, the higher the activity of the catalyst for DMC formation, though the BET surface area is lower on the catalyst calcined at higher temperature. 相似文献
996.
在对本菲尔脱碳装置运行现状和化热钾碱技术分析总结的基础上,提出用WD-3活化剂对本菲尔脱碳系统进行改造的方案。结果表明,在脱碳溶液中加入0.65%WD-3即可在保证净化度情况下使脱碳半贫液循环量减少10%以上,同时吨氨活化剂的损耗低于0.015kg,溶液体系发泡性能也有所改善,达到了节能降耗的目的,使活化热钾碱脱碳技术水平上了一个新台阶。 相似文献
997.
正渗透—纳滤耦合处理苦咸水脱盐工艺 总被引:1,自引:0,他引:1
以2 000 mg/L氯化钠模拟苦咸水,采用二价无机盐作为汲取液,研究了正渗透淡化苦咸水时的水通量;通过软件计算和试验研究了不同组成汲取液的纳滤性能,并且设计了二级纳滤系统用于汲取液的回收。结果表明:相同浓度时硫酸镁汲取液正渗透水通量最低,而氯化镁汲取液水通量最高;相反在纳滤过程中,硫酸镁汲取液性能最佳,氯化镁最差;稀释硫酸钠汲取液浓度为30 g/L时,二级纳滤过程可以将汲取液浓缩至初始浓度(60 g/L),并制得浓度低于500 mg/L的产水。 相似文献
998.
在NiMoP浸渍液中添加不同含量乙二醇,制备了一系列NiMoP/Al2O3催化剂,以二苯并噻吩为模型化合物,考察有机添加剂乙二醇对NiMoP/Al2O3催化剂加氢脱硫性能的影响。结果表明,乙二醇的加入显著提高催化剂的加氢脱硫性能,乙二醇中的羟基与Ni物质的量比为5∶1时,催化剂的加氢脱硫活性最高。乙二醇明显改善NiMoP/Al2O3催化剂的加氢性能。 相似文献
999.
《分离科学与技术》2012,47(15):2303-2314
Polyvinylidene fluoride (PVDF) hollow fiber ultrafiltration membranes consisted of TiO2 and different molecular weight (Mw) of polyvinylpyrrolidone (PVP) (i.e., 10, 24, 40, and 360 kDa) were prepared to treat synthesized oily wastewater. The membrane performances were characterized in terms of pure water flux, permeate flux, and oil rejection while their morphological properties were studied using SEM, AFM, and tensile tester. Results show that the PVDF-TiO2 composite membrane prepared from PVP40k was the best performing membrane owing to its promising water flux (72.2 L/m2.h) coupled with good rejection of oil (94%) when tested with 250 ppm oily solution under submerged condition. It is also found that with increasing PVP Mw, the membrane tended to exhibit higher PVP and protein rejection, greater mechanical strength, smaller porosity, and a smoother surface layer. Regarding the effect of pH, the permeate flux of the PVDF-PVP40k membrane was reported to increase with increasing pH from 4 to 7, followed by decrease when the pH was further increased to 10. Increasing oil concentration in the feed solution was reported to negatively affect the water flux of PVDF-PVP40k membrane, owing to the formation of thicker oil layer on the membrane surface which increased water transport resistance. A simple backflushing process on the other hand could retrieve approximately 60% of the membrane original flux without affecting the oil separation efficiency. Based on the findings, the PVDF-TiO2 membrane prepared from PVP40k can be potentially considered for oily wastewater treatment process due to its good combination of permeability and selectivity and reasonably high water recovery rate. 相似文献
1000.
Xuesong SHANG Jianrong LI Xiaowei YU Jinsheng CHEN Chi HE 《Frontiers of Chemical Science and Engineering》2012,6(1):38
An effective method for the regeneration of thermally deactivated commercial monolith SCR catalysts was investigated. Two types of regenerated solutions, namely NH4Cl (1 mol/L) and dilute H2SO4 (0.5 mol/L), were employed to treat the used catalyst. The effects of temperature and the regeneration process on the structural and textural properties of the catalysts were determined by X-ray diffraction, scanning electron microscopy, N2 adsorption/desorption, elemental analysis and Fourier transform infrared spectroscopy. The results suggest that the anatase phase of the used catalyst is maintained after exposure to high temperatures. Some of the catalytic activity was restored after regeneration. The catalyst regenerated by aqueous NH4Cl had a higher activity than that of the catalyst treated by dilute H2SO4. The main reason is that the NH3 generated from the decomposition of NH4Cl at high temperatures can be adsorbed onto the catalyst which promotes the reaction. The aggregated V2O5 were partially re-dispersed during the regeneration process, and the intrinsic oxidation of ammonia with high concentrations of O2 is a factor that suppresses the catalytic activity. 相似文献