研究了新型缓蚀剂在不同侵蚀介质中的有效性

IF 0.3 Q4 ENGINEERING, PETROLEUM Nafta-Gaz Pub Date : 2023-07-01 DOI:10.18668/ng.2023.07.05
H. Gurbanov, G. Talybov, Mehpara B. Adygezalova, Y. X. Zhang
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引用次数: 0

摘要

首先在实验室条件下测试了新型S-1试剂在pH分别为2.0、4.0、6.0的介质以及分别加入和组合的二氧化碳和硫化氢介质中的防腐效果。在不含硫化氢和二氧化碳的腐蚀介质中,S-1试剂的保护作用较弱。但随着介质酸度和试剂浓度的增加,缓蚀剂的防腐效率也随之提高。在pH = 2.0,试剂浓度为30 mg/l时效果最好。在此条件下,该试剂的防腐效果可达97%。在不含二氧化碳和硫化氢的pH = 4.0和pH = 6.0培养基中,最优浓度为30 mg/l时,抑制剂的保护效果分别为66%和64%。在加入二氧化碳的培养基中,抑制剂S-1的保护作用在pH = 2.0时减弱,在pH = 4.0和pH = 6.0时增强。同时,随着介质中二氧化碳压力的增加,抑制剂S-1的保护作用增强。当介质中加入硫化氢时,会使缓蚀剂S-1的腐蚀速率和保护效率提高。而在不加缓蚀剂的介质中,硫化氢浓度增加到CH2S = 400 mg/l时,在所有ph值下腐蚀速率都有所增加。在不加缓蚀剂的介质中加入1000 mg/l的硫化氢,腐蚀介质中腐蚀速率有所下降,而在缓蚀剂浓度Cinh = 10 mg/l时,腐蚀介质的保护作用略有下降。随着缓蚀剂S-1在介质中的浓度随着二氧化碳和氢气的加入而增加,其防腐效果也随之增强。在Cinh = 10 ~ 30 mg/l范围内,当PCO2 = 0.5 atm, CH2S = 200 mg/l时,估计保护效果为38 ~ 99%,当CH2S = 1000 mg/l时,估计保护效果为17 ~ 79%。在PCO2 = 1.0 atm时,缓蚀剂S-1的防腐效果分别为22-95%和14-76%,在PCO2 = 2.0 atm时,缓蚀剂S-1的防腐效果分别为44-92%和15-75%。在侵蚀性介质中,二氧化碳和硫化氢的共存导致抑制剂S-1的保护作用比只含二氧化碳的介质增强,而比含硫化氢的介质减弱。在硫化氢存在的情况下,二氧化碳压力的增加会导致抑制剂S-1的保护作用下降。在硫化氢浓度为1000 mg/l的培养基中,抑制剂S-1的保护作用比在硫化氢浓度为200 mg/l的培养基中要低。这种情况在无二氧化碳介质中也可以观察到。
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Study of the effectiveness of the new inhibitor in different aggressive media
"The corrosion protection effect of the new S-1 reagent in media with the pH values of 2.0, 4.0, 6.0, as well as carbon dioxide and hydrogen sulfide added separately and combined to the mentioned media, was first tested under laboratory conditions. The protective effect of reagent S-1 was weak in the corrosion medium without hydrogen sulfide and carbon dioxide. However, as the acidity of the medium and the concentration of the reagent increases, the corrosion protection efficiency of the inhibitor also increases. The highest effect is observed at pH = 2.0 and reagent concentration of 30 mg/l. The corrosion protection effect of the reagent reaches 97% under these conditions. In the media with pH = 4.0 and pH = 6.0 without carbon dioxide and hydrogen sulfide, the protective effect of the inhibitor at the optimal concentration of 30 mg/l is 66% and 64%, respectively. In the medium with added carbon dioxide, the protective effect of inhibitor S-1 decreases at pH = 2.0 and, on the contrary, increases at the values of pH = 4.0 and pH = 6.0. Also, as the pressure of carbon dioxide in the medium increases, the protective effect of inhibitor S-1 increases. When hydrogen sulfide is added to the medium, it causes an increase in the corrosion rate and the protection efficiency of inhibitor S-1. However, in the medium without inhibitor, the increase of hydrogen sulfide concentration only up to CH2S = 400 mg/l is accompanied by an increase in the corrosion rate at all values of pH. The addition of 1000 mg/l of hydrogen sulfide to the corrosion medium leads to the decrease in the corrosion rate in the medium without inhibitors and a slight decrease in the protective effect at the concentration of the inhibitor Cinh = 10 mg/l. As the concentration of inhibitor S-1 increases in the medium with the addition of carbon dioxide and hydrogen, its corrosion protection effect also increases. In the range of Cinh = 10–30 mg/l, when PCO2 = 0.5 atm and CH2S = 200 mg/l, the protective effect is estimated at 38–99%, and when CH2S = 1000 mg/l, it is estimated at 17–79%. At PCO2 = 1.0 atm, the value of protective effect is 22–95% and 14–76%, and finally at PCO2 = 2.0 atm, the value of the corrosion protection effect of inhibitor S-1 is estimated at 44–92% and 15–75%, respectively. The coexistence of carbon dioxide and hydrogen sulfide in an aggressive medium leads to an increase in the protective effect of inhibitor S-1 compared to the medium containing only carbon dioxide, and reduces it in comparison to the medium with hydrogen sulfide. An increase in carbon dioxide pressure in the presence of hydrogen sulfide causes a decrease in the protective effect of inhibitor S-1. The protective effect of inhibitor S-1 is lower in the medium with hydrogen sulfide concentration of 1000 mg/l compared to a concentration of 200 mg/l. This case is also observed in the carbon dioxide free medium."
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来源期刊
Nafta-Gaz
Nafta-Gaz ENGINEERING, PETROLEUM-
CiteScore
0.80
自引率
60.00%
发文量
81
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