氧分压对IWO薄膜表面形貌及光电性能的影响

掺钨氧化铟(In2O3:W,IWO)薄膜是一种新型的透明导电氧化物(TCO)薄膜,其中W与In之间存在着较高的价态差,使得IWO薄膜与其他TCO薄膜相比,在相同的电阻率条件下具有载流子浓度低、迁移率高和近红外区透射率高的特点.利用直流磁控溅射法制备了IWO薄膜,利用X射线衍射、扫描电子显微镜、霍尔效应及分光光度计表征了薄膜的表面形貌及光电性能.在工作压力1 Pa、氧分压为2.4×10-1Pa的条件下,实验中制备的IWO薄膜最佳电阻率为6.3×10-4Ω.cm,最高载流子迁移率为34 cm2V-1s-1,载流子浓度达到2.9×1020cm-3,可见光平均透射率约为85%,近红外平均透射率大于80%.     

炉内氧气含量对竹材炭化的影响

竹材炭化过程中,炭化温度和炭化时间是两个重要的工艺参数,但还必须考虑炉内的氧气含量。通过调节进入炉内的氮气和空气流量,并采用氧传感器实时测定并控制炉内氧分压,研究了炉内氧含量对竹材炭化的影响。结果表明：炉内氧分压增加,得炭率下降。因此传统土窑炭化时应严格控制进入炉内的氧气含量,形成缺氧的高温热解环境,防止竹炭自燃,使竹材在平衡氧分压（中性）或还原性高温气氛中炭化。     

无机非整比复合物脱铅剂制备中烧结氧分压的影响

本文探讨了在制备一种新型无机非整比固体复合物脱铅剂过程中，烧结时氧分压对其内部缺陷结构及其最终的吸附性能的影响．在高氧分压区，脱铅剂中点缺陷Ｖ′ｃａ占主导地位且正比于Ｐｏ２１／４，这一点通过测量脱铅剂电导率给予了有力证明．从而说明无机非整比化合物脱铅剂中点缺陷是形成表面吸附活性位的基础；是决定其吸附性能的关键因素．借助缺陷化学知识对其脱铅机理进行了新的探索     

氧分压对Ni/HfO_x/TiN阻变存储单元阻变特性的影响

采用射频磁控溅射的方法,基于不同氧分压制备的氧化铪构建了Ni/HfO_x/TiN结构阻变存储单元.研究发现,随着氧分压的增加,薄膜表面粗糙度略有降低;另一方面,阻变单元功耗降低,循环耐受性能可达10~3次,且转变电压分布的一致性得到改善.结合电流-电压曲线线性拟合结果及外加温度测试探究了器件的转变机理,得出在低阻态的传导机理为欧姆传导机理,在高阻态的传导机理为肖特基发射机理,并根据氧空位导电细丝理论,对高低阻态的阻变机理进行了详细的理论分析.     

利用固体电解质氧浓差电池测定铝镇静钢中的铝量

铝镇静钢的质量与其含铝量的控制有极其重要关系,本文根据钢液中氧活度α[o]与含铝量[Al]sol间存在的平衡关系,利用固体电解质氧浓差电池快速测定α[o],并对应于取样分析[Al]sol量,建立实测的α[o]—[Al]sol关系。从而,可通过直接测定钢液中氧的活度来测定钢液中含铝量,并通过测氧达到控制铜中铝量,确保钢质量的目的。     

高海拔隧道施工氧含量变化及供氧方法

论文针对高海拔隧道低压缺氧威胁施工安全的问题,基于氧气质量守恒和等效气管氧分压两种方法分析了高海拔隧道施工供氧标准,并在海拔4232m的雀儿山隧道开展洞口与掌子面温度、气压和氧含量长期监测。结果表明：实测洞口氧气密度比理论分析低4.93%,而实测气管氧分压比理论分析低0.6%,等效气管氧分压方法更适用于高海拔缺氧程度预测。洞口与掌子面温度和大气压力呈夏季高、冬季低的季节性波动,隧道掘进1500m以后,在保证良好通风条件下,掌子面比洞口气管气氧分压平均低0.46kPa,随着推进距离继续增大,气管氧分压降低不明显。现场测试发现弥散式供氧方法能够有效增加施工区域的氧气含量,但供氧需求量大,施工建议采取弥散式供氧、个人携氧与移动式吸氧车供氧相结合的方式,保障隧道施工人员的氧气需求。     

氢离子对血红蛋白-氧亲和力影响的拉曼光谱研究

静脉采血,分离并制备血红蛋白溶液,用拉曼光谱方法观察不同pH时H+对血红蛋白-氧结合状态与能力的影响。结果显示:在514.5nm激光的激发下,当pH为7.4时,随着氧分压降低,血红蛋白在1 375,1 562,1 585和1 638cm-1峰强均逐渐减弱,其中以1 375和1 638cm-1峰渐变最明显且相关性显著。以氧分压为横坐标,拉曼峰强为纵坐标,对pH为5.7,7.4和8.0时的血红蛋白在1 375和1 638cm-1峰的强度及其氧分压进行线性拟合,结果显示2处的拟合效果均良好,拉曼峰强度/氧分压的斜率关系表现为K8.0>K7.4>K5.7,表明pH越低血红蛋白的氧亲和力越低,越有利于向组织释放氧气。研究表明,应用拉曼光谱技术可检测血红蛋白与氧的亲和力,通过对血红蛋白-氧亲和力的量化检测,可以观察pH对血氧结合状态的影响,为血氧分压的监测以及氢离子和二氧化碳等血氧亲和力调节因子调节能力的研究提供新的研究方法与理论基础。     

氧分压对固体氧化物电解池性能的影响

High-temperature (700–900 ℃) steam electrolysis based on solid oxide electrolysis cells (SOECs) is valuable as an efficient and clean path for large-scale hydrogen production with nearly zero carbon emissions, compared with the traditional paths of steam methane reforming or coal gasification. The operation parameters, in particular the feeding gas composition and pressure, significantly affect the performance of the electrolysis cell. In this study, a computational fluid dynamics model of an SOEC is built to predict the electrochemical performance of the cell with different sweep gases on the oxygen electrode. Sweep gases with different oxygen partial pressures between 1.01 × 10³ and 1.0 × 10⁵ Pa are fed to the oxygen electrode of the cell, and the influence of the oxygen partial pressure on the chemical equilibrium and kinetic reactions of the SOECs is analyzed. It is shown that the rate of increase of the reversible potential is inversely proportional to the oxygen partial pressure. Regarding the overpotentials caused by the ohmic, activation, and concentration polarization, the results vary with the reversible potential. The Ohmic overpotential is constant under different operating conditions. The activation and concentration overpotentials at the hydrogen electrode are also steady over the entire oxygen partial pressure range. The oxygen partial pressure has the largest effect on the activation and concentration overpotentials on the oxygen electrode side, both of which decrease sharply with increasing oxygen partial pressure. Owing to the combined effects of the reversible potential and polarization overpotentials, the total electrolysis voltage is nonlinear. At low current density, the electrolysis cell shows better performance at low oxygen partial pressure, whereas the performance improves with increasing oxygen partial pressure at high current density. Thus, at low current density, the best sweep gas should be an oxygen-deficient gas such as nitrogen, CO₂, or steam. Steam is the most promising because it is easy to separate the steam from the by-product oxygen in the tail gas, provided that the oxygen electrode is humidity-tolerant. However, at high current density, it is best to use pure oxygen as the sweep gas to reduce the electric energy consumption in the steam electrolysis process. The effects of the oxygen partial pressure on the power density and coefficient of performance of the SOEC are also discussed. At low current density, the electrical power demand is constant, and the efficiency decreases with growing oxygen partial pressure, whereas at high current density, the electrical power demand drops, and the efficiency increases.     

沉积速率和氧分压对HfO2薄膜残余应力的影响

采用ZYGO MarkIII-GPI数字波面干涉仪对以K9玻璃为基底的电子束蒸发方法制备的HfO₂薄膜中的残余应力进行了研究,讨论了沉积速率、氧分压这两种工艺参量对HfO₂薄膜残余应力的影响.实验结果表明：在所有的工艺条件下,薄膜的残余应力均为张应力;随着沉积速率的升高,氧分压的减小,薄膜的堆积密度逐渐增大,而残余应力呈减小趋势.同时用X射线衍射技术测量分析了不同工艺条件下HfO₂薄膜的晶体结构,探讨了HfO₂薄膜晶体 关键词： 残余应力 2薄膜')" href="#">HfO₂薄膜 沉积速率 氧分压     

氧分压对TiO2薄膜微观结构与光吸收性能的影响

采用直流磁控溅射法在不同氧分压下制备TiO2薄膜;研究氧分压对TiO2薄膜的表面形貌、晶体结构、化学组分及光吸收性能的影响.研究结果表明Ti在所有样品中均以 4价态存在;随着氧分压的增大,TiO2薄膜颗粒逐渐变大,薄膜的结晶质量随着氧分压的增大逐渐提高;在吸收光谱中,300 nm 附近的紫外吸收峰随着氧分压的增大而减弱,在330～465 nm 范围内出现1 个吸收谷,且该吸收谷随着氧分压的增大而减小,当氧分压达到0.8 Pa时,吸收谷基本消失.