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1)  H2S and CO2
H2S和CO2
2)  CO_2 and H_2S
CO2和H2S
1.
The harmfulness of coexistence of CO_2 and H_2S in oil and nature gas jointly corroding tubular goods is expounded.
阐述了石油天然气中CO2和H2S共同存在时对油管钢联合腐蚀的危害性,分析了CO2和H2S腐蚀的研究方向与发展趋势。
3)  H_2S and CO_2 environment
H2S和CO2环境
4)  CO_2/H_2S corrosion
CO2/H2S腐蚀
1.
In order to find out the relation between corrosion time and the cathode reaction of CO_2/H_2S corrosion of tubular steels,a autoclave,together with EIS,is used to study the cathode process of CO_2/H_2S corrosion of tubular steel N80 in simulated oil well produced water under 180psi CO_2 and 2psi H_2S at 100 ℃.
为了找出油管钢CO2/H2S腐蚀的阴极反应与腐蚀时间的关系,采用高温高压釜装置,辅以交流阻抗谱(EIS)测试技术,在100℃时,CO2分压180 psi和H2S分压2 psi的条件下,对N80油管钢在模拟油田采出液中CO2/H2S腐蚀的阴极过程进行了研究。
2.
Autoclave test,together with weight loss method,XRD,SEM and EDS,were used to study CO_2/H_2S corrosion behavior of tubular steel P110 in simulated oil well produced water at 90 ℃.
采用高温高压釜试验,辅以失重法、X射线衍射、扫描电镜和电子能谱分析,对90℃时油管钢P110在模拟油井采出液中的CO2/H2S腐蚀行为进行了研究。
5)  RNH 2-CO 2-H 2S-H 2O
RNH2-CO2-H2S-H2
6)  CO2/H2S corrosion
CO2/H2S腐蚀
1.
The CO2/H2S corrosion behavior of tubular steel N80 at different H2S partial pressures(0.
12 MPa)下N80油管钢的CO2/H2S腐蚀行为进行了研究。
2.
In order to find out the relation between corrosion time and the anode reaction of CO2/H2S corrosion of tubular steels,a autoclave,together with EIS,is used to study the anode process of CO2/H2S corrosion of tubular steel N80 in simulated oil well produced water under 180psi CO2 and 2psi H2S at 100℃.
为了找出油管钢CO2/H2S腐蚀的阳极反应与腐蚀时间的关系,采用高温高压釜装置,辅以交流阻抗谱(EIS)测试技术,在100℃,CO2分压241kPa(180psi)和H2S分压13。
3.
Autoclave test, together with weight loss method, XRD, SEM and EDS, was used to study CO2/H2S corrosion behavior of tubular steel P110 in oil well produced water at 90℃.
采用高温高压釜试验,辅以失重法、X射线衍射、扫描电镜和电子能谱分析,对90℃时油管钢P110在模拟油井采出液中的CO2/H2S腐蚀行为进行了研究。
补充资料:[3-(aminosulfonyl)-4-chloro-N-(2.3-dihydro-2-methyl-1H-indol-1-yl)benzamide]
分子式:C16H16ClN3O3S
分子量:365.5
CAS号:26807-65-8

性质:暂无

制备方法:暂无

用途:用于轻、中度原发性高血压。

说明:补充资料仅用于学习参考,请勿用于其它任何用途。
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