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1)  thin electrolyte film
薄层液膜
1.
A study on corrosion inhibition of 16Mn steel under thin electrolyte film with H_2S;
16Mn钢在含H_2S的薄层液膜下的缓蚀研究
2.
The effect of CO2 on the atmospheric corrosion of A3 steel under thin electrolyte film has been studied using an electrochemical technique, combined with observation of the surface by SEM and analysis of corrosion product by XRD.
通过电化学法并结合 XRD及 SEM;研究了大于临界相对湿度条件下, CO_2浓度对 A3钢在薄层液膜下大气腐蚀的影响电化学实验结果表明,A3钢的大气腐蚀速率随CO_2浓度的上升而增加。
2)  thin layer electrolyte
薄层液膜
1.
A suit of electrochemical cell which was used to investigate the corrosion behavior of metals under different thin layer electrolyte was designed.
设计了用于研究金属材料在薄层液膜下腐蚀行为的参比电极后置式三电极电化学测量电池 ,并用此研究了铜在薄层液膜下的阳极极化行为 。
3)  thin layer
薄膜,薄膜层
4)  nutrient film technique
薄层营养液膜技术(NFT)
5)  thin electrolyte film
薄液膜
1.
Combined with x-ray diffraction and scanning electron microscopy, the corrosion mechanisms for zinc under thin electrolyte film was discussed.
使用石英晶体微天平(QCM:quartz crystal microbalance)为主要手段研究了在 85%RH相对湿度)和 NaCI存在的条件下,金属Zn在不同CO2浓度下的大气腐蚀动力学,同时结合 X射线衍射(XRD)和扫描电镜(SEM)研究了Zn在薄液膜下的大气腐蚀机理,并用扫描电子显微#(SEM)对腐蚀产物进行形貌分析,阐述了腐蚀产物的保护特征。
2.
This thesis we designed two experiment setups which are "the thin electrolyte film experiment and indoor wet-dry cycle experiment" to simulate the atmospheric corrosion.
本论文采用自行设计的金属大气腐蚀的“室内薄液膜和室内干湿循环”模拟研究装置,同时采用电化学阻抗谱(electrochemical impedance spectroscopy,EIS)、电化学噪声(electrochemical noise,EN)技术、极化曲线(Potentiodynamicpolarization)等电化学技术,并结合SEM/EDX等材料结构测试手段,对常见的典型金属材料2024-T3铝合金、09CuPCrNi和Q400NQRL耐候钢等的大气腐蚀行为进行了理论探讨和室内模拟加速实验研究。
3.
Corrosion behavior of pure magnesium was investigated by means of cathodic polarization curve and electrochemical impedance spectroscopy(EIS)under aerated and deaerated thin electrolyte films(TEF)with various thicknesses.
用电化学法研究了纯镁在未除氧和除氧的下不同厚度薄液膜下的腐蚀行为。
6)  latex film
乳液薄膜
1.
Thermo-sensitive latex films were in sequence prepared with such latex particles and small amount of the binder polymer,PVA1788.
将该乳液与水溶性成膜树脂聚乙烯醇(PVA1788)配合使用并制备了乳液薄膜。
补充资料:降液管清液层高度
分子式:
CAS号:

性质:又称降液管清液层高度。板式塔降液管内的液柱液面到下层塔板的垂直距离。如图中的Hd(图暂缺)。为保持板式塔正常操作,避免发生液泛,降液管液柱高度不能超过一定限度。一般应满足Hd≤(0.4~0.6)(HT+hw),式中HT为塔板间距,hw为堰高,系数一般取0.5,易起泡物系取0.4,不易起泡物系取0.6。

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